WO2013003982A1 - Third-type absorption heat pump - Google Patents

Third-type absorption heat pump Download PDF

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Publication number
WO2013003982A1
WO2013003982A1 PCT/CN2011/001118 CN2011001118W WO2013003982A1 WO 2013003982 A1 WO2013003982 A1 WO 2013003982A1 CN 2011001118 W CN2011001118 W CN 2011001118W WO 2013003982 A1 WO2013003982 A1 WO 2013003982A1
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WO
WIPO (PCT)
Prior art keywords
generator
solution
heat exchanger
absorption
new
Prior art date
Application number
PCT/CN2011/001118
Other languages
French (fr)
Chinese (zh)
Inventor
李华玉
Original Assignee
Li Huayu
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Li Huayu filed Critical Li Huayu
Priority to PCT/CN2011/001118 priority Critical patent/WO2013003982A1/en
Publication of WO2013003982A1 publication Critical patent/WO2013003982A1/en

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B27/00—Machines, plants or systems, using particular sources of energy
    • F25B27/02—Machines, plants or systems, using particular sources of energy using waste heat, e.g. from internal-combustion engines
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B15/00—Sorption machines, plants or systems, operating continuously, e.g. absorption type
    • F25B15/008—Sorption machines, plants or systems, operating continuously, e.g. absorption type with multi-stage operation
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00—Adapting or protecting infrastructure or their operation
    • Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
    • Y02A30/274—Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62—Absorption based systems
    • Y02B30/625—Absorption based systems combined with heat or power generation [CHP], e.g. trigeneration

Definitions

  • the invention belongs to the technical field of low temperature waste heat utilization heat pump.
  • the temperature difference between the high-temperature driving heat and the heated medium corresponds to the single-effect, double-effect and multi-effect of the solution high-temperature generation process; taking into account the diversity of parameters and quantities of waste heat resources, and waste heat
  • the temperature difference between the cooling medium and the cooling medium corresponds to the single-effect, double-effect, multi-effect, 1.5-level and regenerative single-effect, regenerative double-effect, regenerative multi-effect and regenerative heat generation process. Equation 1. Level 5; combined with the combination of the two aspects, the series of the third type of absorption heat pump is obtained.
  • the main object of the present invention is to provide a third type of absorption heat pump, and the specific contents of the invention are as follows:
  • the third type of absorption heat pump is composed of a first generator, a second generator, an absorber, a first condenser, a second condenser, an evaporator, a solution pump, a refrigerant pump, a throttle valve, a first solution heat exchanger and a second solution heat exchanger -
  • the first generator has a concentrated solution line connected to the second generator via the solution pump, the first solution heat exchanger and the second solution heat exchanger
  • the second generator further has a concentrated solution line connected to the absorber via the second solution heat exchanger, and the absorber and the dilute solution line are connected to the first generator via the first solution heat exchanger, and the first generator is also cold
  • the refrigerant vapor passage is in communication with the first condenser, the first condenser and the refrigerant liquid pipeline are connected to the evaporator via the refrigerant liquid pump, and the second generator and the refrigerant vapor passage are connected to the second condenser, the second The condenser
  • the third type of absorption heat pump is a single-effect-single-effect third-class absorption heat pump mentioned in item 1, adding a second solution pump, a third solution heat exchanger, an absorption-generator, and a minute a steam chamber, a third condenser, a second evaporator, a second refrigerant liquid pump and a third refrigerant liquid pump, wherein the absorber has a dilute solution line connected to the first generator via the first solution heat exchanger to be adjusted to The absorber has a dilute solution line connected to the absorption-generator via the third solution heat exchanger, and the absorption-generator and the dilute solution line are connected to the first generator via the first solution heat exchanger, and the first generator is The concentrated solution pipeline is connected to the second generator through the first solution pump, the first solution heat exchanger and the second solution heat exchanger to adjust the first generator to have a concentrated solution pipeline through the first solution pump, the first solution The heat exchanger and the absorption-generator are connected to the steam
  • the third type of absorption heat pump is a single-effect-single-effect third-type absorption heat pump mentioned in the first item, adding a second solution pump, a third solution heat exchanger, an absorption-generator, and a minute a steam chamber, a third condenser, a second refrigerant liquid pump and a third solution pump, wherein the absorber has a dilute solution line connected to the first generator through the first solution heat exchanger to adjust the absorber to a dilute solution line
  • the third solution pump and the third solution heat exchanger are in communication with the absorption-generator, and the absorption-generator and the dilute solution line are connected to the first generator via the first solution heat exchanger, and the first generator is rich
  • the solution line is connected to the second generator via the first solution pump, the first solution heat exchanger and the second solution heat exchanger to adjust the first generator to have a concentrated solution line through the first solution pump, the first solution heat exchange And the absorption-generator is connected to the steam distribution chamber, and
  • the refrigerant vapor passage is connected to the third condenser, and the third condenser and the refrigerant liquid pipeline are connected to the evaporator via the second refrigerant liquid pump, and the evaporator adds a refrigerant vapor passage to communicate with the absorption-generator.
  • the third condenser also has a cooling medium line communicating with the outside to form a single-effect-recovery single-effect third-type absorption heat pump.
  • the third type of absorption heat pump is a single-effect-single-effect third-type absorption heat pump mentioned in the first item, adding a second solution pump, a third solution heat exchanger, an absorption-generator, and a minute a steam chamber, a third condenser, a second evaporator, a second refrigerant liquid pump or a second throttle valve, the first generator has a concentrated solution pipeline through the first solution pump, the first solution heat exchanger and the first The two solution heat exchanger is connected to the second generator to be adjusted to be a first generator having a concentrated solution line connected to the absorption-generator via the first solution pump and the first solution heat exchanger, and the absorption-generator and the dilute solution tube Passing through the first solution heat exchanger to communicate with the first generator, and connecting the absorber with the dilute solution line through the first solution heat exchanger to the first generator to adjust the absorber to have a dilute solution line through the third solution heat
  • the exchanger and the absorption-generator are
  • the vapor channel of the agent is in communication with the third condenser, the third condenser and the coolant liquid pipeline are connected to the first evaporator via the second refrigerant liquid pump, or the third condenser and the refrigerant liquid pipeline are passed through the second
  • the throttle valve is in communication with the first condenser, the absorption-generator or the heated medium line is in communication with the outside, the third condenser and the cooling medium line are in communication with the outside, and the second evaporator has a residual heat medium conduit Connected with the outside to form a single-effect-recovery single-effect third-class absorption heat pump; wherein, 1 without the second evaporator, the first condenser has a refrigerant liquid pipeline through the first refrigerant liquid pump and the first The evaporator is connected, the first evaporator adds a refrigerant vapor channel to communicate with the absorption-generator; 2 when there is no third condenser, the steam distribution chamber
  • the third type of absorption heat pump is a single-effect-single-effect third-type absorption heat pump mentioned in item 1, adding a third generator, a third solution heat exchanger and a second throttle valve,
  • the first generator is further provided with a concentrated solution pipeline after the first solution pump and the first solution heat exchanger, and is further connected to the third generator via the third solution heat exchanger, and the third generator further has a concentrated solution pipeline
  • the three-solution heat exchanger is in communication with the absorber
  • the second generator has a refrigerant vapor passage connected to the second condenser to be adjusted to be a second generator having a refrigerant vapor passage connected to the third generator, and then the third generator is further
  • the refrigerant liquid pipeline is widened in the second section
  • the second condenser is connected - the refrigerant vapor generated by the second generator is used as the driving heat medium of the third generator, and the third generator and the refrigerant vapor passage are connected with the second condenser to form
  • the third type of absorption heat pump is a single-effect-single-effect third-type absorption heat pump mentioned in item 1, adding a third generator, a third solution heat exchanger and a second throttle valve,
  • the first generator has a concentrated solution pipeline connected to the second generator via the solution pump, the first solution heat exchanger and the second solution heat exchanger to adjust the first generator to have a concentrated solution pipeline through the solution pump, first
  • the solution heat exchanger, the second solution heat exchanger and the third solution heat exchanger are in communication with the second generator, and the second generator has a concentrated solution line connected to the absorber via the second solution heat exchanger to be adjusted to the second
  • the generator has a concentrated solution pipeline connected to the third generator via the third solution heat exchanger, and the third generator and the concentrated solution pipeline communicate with the absorber via the second solution heat exchanger, and the second generator is cooled
  • the refrigerant vapor passage is connected to the second condenser to be adjusted to be the second generator having the refrigerant vapor passage communicating with the third generator,
  • the third type of absorption heat pump is a third type of absorption heat pump according to item 6, wherein the solution throttle valve is added, and the first generator has a concentrated solution line through the first solution pump and the first solution.
  • the heat exchanger, the second solution heat exchanger and the third solution heat exchanger are connected to the second generator to be adjusted to have a first solution having a concentrated solution line through the first solution pump, the first solution heat exchanger, and the second solution.
  • the heat exchanger is then connected to the third generator via the solution throttle valve and then communicated with the second generator via the third solution heat exchanger to form a double-effect-single-effect third-type absorption heat pump.
  • the third type of absorption heat pump is a single-effect-single-effect third-type absorption heat pump mentioned in item 1, adding a third generator, a third solution heat exchanger, a second solution pump, and a a two-throttle valve, the first generator has a concentrated solution pipeline connected to the second generator through the first solution pump, the first solution heat exchanger and the second solution heat exchanger to adjust the first generator to have a concentrated solution tube
  • the first solution pump, the first solution heat exchanger and the second solution heat exchanger are in communication with the third generator, and the third generator further has a concentrated solution line through the second solution pump and the third solution heat exchanger
  • the second generator is connected, and the second generator has a concentrated solution pipeline connected to the absorber through the second solution heat exchanger to adjust the second generator to have a concentrated solution pipeline through the third solution heat exchanger and the second solution heat
  • the exchanger is in communication with the absorber, the second generator has a refrigerant vapor passage connected to the second condenser, and the second generator has a
  • the third type of absorption heat pump is a third type of absorption heat pump according to item 8, which increases the throttle section of the solution, and the first generator has a concentrated solution pipeline through the first solution pump and the first solution.
  • the heat exchanger and the second solution heat exchanger are connected to the third generator to be adjusted so that the first generator has a concentrated solution line directly after passing through the first solution pump, the first solution heat exchanger and the second solution heat exchanger
  • the second generator is in communication and is again in communication with the third generator via the solution throttle to form a double-effect single-effect third type absorption heat pump.
  • the third type of absorption heat pump in the third type of absorption heat pump according to item 5, adding a fourth generator, a fourth solution heat exchanger and a third throttle valve, the first solution heat exchanger
  • the concentrated solution line is connected to the fourth generator via the fourth solution heat exchanger
  • the fourth generator and the concentrated solution line are connected to the absorber via the fourth solution heat exchanger
  • the third generator has refrigerant vapor.
  • the passage is connected to the second condenser to be adjusted to be a third generator having a refrigerant vapor passage communicating with the fourth generator, and then the fourth generator is further connected to the second condenser via the third throttle valve,
  • the four generators also have a refrigerant vapor passage communicating with the second condenser to form a three-effect-single-effect third-type absorption heat pump.
  • the third type of absorption heat pump is a third type of absorption heat pump according to item 6, wherein the fourth generator, the fourth solution heat exchanger and the third throttle valve are added, and the second solution is heat exchanged.
  • the machine has a concentrated solution pipeline through the third solution heat exchanger and the first
  • the second generator is connected to the second solution heat exchanger, and the concentrated solution pipeline is connected to the second generator via the fourth solution heat exchanger and the third solution heat exchanger, and the third generator has a concentrated solution pipeline.
  • the two solution heat exchanger is connected to the absorber to be adjusted so that the third generator has a concentrated solution line connected to the fourth generator via the fourth solution heat exchanger, and the fourth generator has a concentrated solution line through the second solution heat
  • the exchanger is in communication with the absorber, and the third generator has a refrigerant vapor passage communicating with the second condenser to be adjusted to a third generator having a refrigerant vapor passage communicating with the fourth generator, the fourth generator having a refrigerant liquid
  • the pipeline is connected to the second condenser via a third throttle valve, and the fourth generator has a refrigerant vapor passage communicating with the second condenser to form a three-effect-single-effect third-type absorption heat pump.
  • the third type of absorption heat pump is a third type of absorption heat pump according to item 8, adding a fourth generator, a fourth solution heat exchanger, a third throttle valve and a third solution pump,
  • the second solution heat exchanger has a concentrated solution line connected to the third generator and is adjusted to be a second solution heat exchanger having a concentrated solution line connected to the fourth generator, and the fourth generator has a concentrated solution line through the third
  • the solution pump and the fourth solution heat exchanger are in communication with the third generator, and the second generator has a concentrated solution line connected to the absorber via the third solution heat exchanger and the second solution heat exchanger to be adjusted to the second generator
  • the concentrated solution pipeline communicates with the absorber through the third solution heat exchanger, the fourth solution heat exchanger and the second solution heat exchanger, and the third generator has a refrigerant vapor passage connected to the second condenser to be adjusted to
  • the third generator has a refrigerant vapor passage connected to the fourth generator, and the fourth generator further has a refrigerant liquid
  • the third type of absorption heat pump is the third type of absorption heat pump according to the first item, wherein the fourth generator, the fourth solution heat exchanger and the second throttle valve are added, the first generator a solution pump and a first solution heat exchanger are further provided with a concentrated solution line and then communicated with the fourth generator via the fourth solution heat exchanger, and the fourth generator further has a concentrated solution line through the fourth solution heat exchanger and
  • the absorber is connected to communicate the second generator with the refrigerant vapor passage and the second condenser, and the second generator has a refrigerant vapor passage connected with the fourth generator, and then the fourth generator has a refrigerant liquid pipeline
  • the second throttle valve is in communication with the second condenser - the refrigerant vapor generated by the second generator acts as a driving heat medium for the fourth generator, and the fourth generator and the refrigerant vapor passage communicate with the second condenser to form Double-effect-recovery single-effect third-class absorption heat pump.
  • the third type of absorption heat pump in the third type of absorption heat pump according to item 1, adds a fourth generator, a fourth solution heat exchanger and a second throttle valve, and the first generator has a rich
  • the solution line is connected to the second generator via the first solution pump, the first solution heat exchanger and the second solution heat exchanger to adjust the first generator to have a concentrated solution line through the first solution pump, the first solution heat exchange
  • the second solution heat exchanger and the fourth solution heat exchanger are in communication with the second generator, and the second generator has a concentrated solution line connected to the absorber via the second solution heat exchanger to be adjusted to have a second generator
  • the concentrated solution pipeline is connected to the fourth generator via the fourth solution heat exchanger, and the fourth generator and the concentrated solution pipeline are connected to the absorber via the second solution heat exchanger, and the second generator has a refrigerant vapor passage
  • the second condenser is connected to the second condenser, and the second generator has a refrigerant vapor passage communicating with the fourth generator, and then
  • the refrigerant vapor produced by the second generator is used as the fourth hair Driver's heat medium, a fourth generator, the refrigerant vapor channel communicating with the second condenser to form a double effect - a third heat recovery single effect absorption heat pump.
  • the third type of absorption heat pump is the third type of absorption heat pump according to item 14, wherein the solution throttle valve is added, and the first generator has a concentrated solution line through the first solution pump and the first solution.
  • the heat exchanger, the second solution heat exchanger and the fourth solution heat exchanger are connected to the second generator to be adjusted to have a first solution having a concentrated solution line through the first solution pump, the first solution heat exchanger, and the second solution.
  • the heat exchanger is then connected to the fourth generator via the solution throttle valve and then communicated with the second generator via the fourth solution heat exchanger to form a double-effect-recovery single-effect third-type absorption heat pump.
  • the third type of absorption heat pump is a third type of absorption heat pump according to item 1, adding a fourth generator, a fourth solution heat exchanger, a second section flow and a third solution pump,
  • the first generator has a concentrated solution line through the first solution pump, the first a solution heat exchanger and a second solution heat exchanger are connected to the second generator to be adjusted to have a first solution having a concentrated solution line through the first solution pump, the first solution heat exchanger and the second solution heat exchanger and
  • the fourth generator is connected, the fourth generator has a concentrated solution pipeline connected to the second generator via the third solution pump and the fourth solution heat exchanger, and the second generator has a concentrated solution pipeline through the second solution for heat exchange
  • the second generator has a concentrated solution line connected to the absorber through the fourth solution heat exchanger and the second solution heat exchanger, and the second generator has a refrigerant vapor channel and a second condenser
  • the communication is adjusted so that the second generator has a refrigerant vapor passage communicating with the fourth generator,
  • the third type of absorption heat pump is a third type of absorption heat pump according to item 16, which increases the throttle section of the solution, and the first generator has a concentrated solution pipeline through the first solution pump and the first solution.
  • the heat exchanger and the second solution heat exchanger are connected to the fourth generator to be adjusted so that the first generator has a concentrated solution line directly after passing through the first solution pump, the first solution heat exchanger and the second solution heat exchanger
  • the second generator is in communication and reconnected via the solution throttle valve to the fourth generator to form a double effect-single effect third type absorption heat pump.
  • the third type of absorption heat pump in the third type of absorption heat pump according to item 13, adding a fifth generator, a third throttle valve and a fifth solution heat exchanger, the first solution heat exchanger
  • the concentrated solution line is connected to the fifth generator via the fifth solution heat exchanger
  • the fifth generator and the concentrated solution line are connected to the absorber via the fifth solution heat exchanger
  • the fourth generator has refrigerant vapor.
  • the passage is connected to the second condenser to be adjusted to be the fourth generator having the refrigerant vapor passage communicating with the fifth generator, and then the fifth generator is further connected to the second condenser via the third throttle valve,
  • the five generators also have a refrigerant vapor passage communicating with the second condenser to form a three-effect-recovery single-effect third-type absorption heat pump.
  • the third type of absorption heat pump is a third type of absorption heat pump according to item 14, wherein the fifth generator, the third section of the flow and the fifth solution heat exchanger are added, and the second solution is heat exchanged.
  • the concentrated solution line is connected to the second generator via the fourth solution heat exchanger to be adjusted to the second solution heat exchanger, and the concentrated solution line is passed through the fifth solution heat exchanger and the fourth solution heat exchanger and the second occurrence Connected to the fourth generator having a concentrated solution line connected to the absorber via the second solution heat exchanger to be adjusted to a fourth generator having a concentrated solution line connected to the fifth generator via the fifth solution heat exchanger,
  • the fifth generator further has a concentrated solution pipeline connected to the absorber via the second solution heat exchanger, and the fourth generator has a refrigerant vapor passage communicating with the second condenser to adjust the fourth generator to have a refrigerant vapor passage and After the fifth generator is connected, the fifth generator further has a refrigerant liquid pipeline connected to the second condenser via
  • the third type of absorption heat pump is a third type of absorption heat pump according to item 16, wherein the fifth generator, the third throttle valve, the fourth solution pump and the fifth solution heat exchanger are added,
  • the second solution heat exchanger has a concentrated solution line connected to the fourth generator and is adjusted to be a second solution heat exchanger having a concentrated solution line connected to the fifth generator, and the fifth generator and the concentrated solution line are passed through a fourth
  • the solution pump and the fifth solution heat exchanger are in communication with the fourth generator, and the second generator has a concentrated solution line connected to the absorber via the fourth solution heat exchanger and the second solution heat exchanger to be adjusted to the second generator
  • the concentrated solution pipeline is connected to the absorber through the fourth solution heat exchanger, the fifth solution heat exchanger and the second solution heat exchanger, and the fourth generator has a refrigerant vapor passage connected to the second condenser to be adjusted to
  • the fourth generator has a refrigerant vapor passage connected to the fifth generator
  • the fifth generator has a refrigerant liquid
  • a third type of absorption heat pump in the third type of absorption heat pump according to any one of items 2-3, wherein the third generator, the fourth solution heat exchanger and the second throttle valve are added
  • the second solution pump is connected with the concentrated solution pipeline through the third solution heat exchanger and is further connected to the third generator via the fourth solution heat exchanger, and the third generator and the concentrated solution pipeline are further heated by the fourth solution.
  • the converter is in communication with the absorber, and the second generator has a refrigerant vapor passage communicating with the second condenser to adjust the second generator to have a refrigerant vapor passage communicating with the third generator, and the third generator is further provided with a refrigerant liquid
  • the pipeline is connected to the second condenser via the second throttle valve - the refrigerant vapor generated by the second generator acts as a driving heat medium for the third generator, and the third generator also has a refrigerant vapor passage and a second condenser Connected to form a double-effect-recovery single-effect third-class absorption heat pump.
  • a third type of absorption heat pump in the third type of absorption heat pump according to any one of items 2-3, wherein the third generator, the fourth solution heat exchanger and the second throttle valve are added And the second solution pump has a concentrated solution pipeline connected to the second generator through the third solution heat exchanger and the second solution heat exchanger to adjust to a second solution pump having a concentrated solution pipeline through the third solution heat exchanger,
  • the second solution heat exchanger and the fourth solution heat exchanger are in communication with the second generator, and the second generator has a concentrated solution line connected to the absorber via the second solution heat exchanger to adjust the second generator to have a concentrated solution
  • the pipeline is connected to the third generator via the fourth solution heat exchanger, and the third generator and the concentrated solution pipeline are connected to the absorber via the second solution heat exchanger, and the second generator has a refrigerant vapor passage and a second
  • the second condenser is connected to adjust to the second generator having the refrigerant vapor passage communicating with the third generator, and then the third generator is further connected to the second con
  • the third type of absorption heat pump is the third type of absorption heat pump according to item 22, wherein the solution throttle valve is added, and the second solution pump has a concentrated solution line through the third solution heat exchanger, The two solution heat exchanger and the fourth solution heat exchanger are connected to the second generator to be adjusted to be the second solution pump.
  • the concentrated solution line is passed through the third solution heat exchanger and the second solution heat exchanger, and then the solution is throttled separately.
  • the broadband is connected to the third generator and communicated with the second generator via the fourth solution heat exchanger to form a double-effect-recovery single-effect third-type absorption heat pump.
  • a third type of absorption heat pump which is the third type of absorption heat pump according to any one of items 2-3, wherein the third generator, the fourth solution heat exchanger, and the second throttle valve are added a third solution pump or a fourth solution pump, wherein the second solution pump has a concentrated solution line connected to the second generator via the third solution heat exchanger and the second solution heat exchanger to adjust to a second solution pump having a concentrated solution
  • the pipeline is connected to the third generator via the third solution heat exchanger and the second solution heat exchanger, and the third generator has a concentrated solution pipeline via the third solution pump or the fourth solution pump, the fourth solution heat exchanger Connected with the second generator, the second generator has a concentrated solution line connected to the absorber through the second solution heat exchanger, and the second generator has a concentrated solution line through the fourth solution heat exchanger and the second solution
  • the heat exchanger is in communication with the absorber, and the second generator has a refrigerant vapor passage communicating with the second condenser to adjust the second generator to have a refrigerant
  • the third type of absorption heat pump is the third type of absorption heat pump according to item 24, wherein the solution throttle valve is added, and the second solution pump has a concentrated solution line through the third solution heat exchanger and the first
  • the two solution heat exchanger is connected to the third generator to be adjusted to be the second solution pump.
  • the concentrated solution line is directly connected to the second generator and then passed through the solution section after passing through the third solution heat exchanger and the second solution heat exchanger.
  • the flow valve is in communication with the third generator to form a double-effect regenerative single-effect third-class absorption heat pump.
  • the third type of absorption heat pump is the third type of absorption heat pump according to item 21, wherein the fourth generator, the fifth solution heat exchanger and the third throttle valve are added, and the second solution pump is passed through
  • the three-solution heat exchanger is further provided with a concentrated solution pipeline and is further connected to the fourth generator via the fifth solution heat exchanger, and the fourth generator and the concentrated solution pipeline are connected to the absorber through the fifth solution heat exchanger, and the first
  • the third generator has a refrigerant vapor passage connected to the second condenser and is adjusted to be a third generator having a refrigerant vapor passage connected to the fourth generator, and the fourth generator is further provided with a refrigerant liquid pipeline via the third throttle valve
  • the second condenser is connected, and the fourth generator further has a refrigerant vapor passage communicating with the second condenser to form a three-effect-recovery type single-effect third-type absorption heat pump.
  • the third type of absorption heat pump is a fourth type of absorption heat pump according to item 22, wherein the fourth generator is added.
  • a fifth solution heat exchanger and a third throttle valve the second solution pump having a concentrated solution line connected to the second generator via the third solution heat exchanger, the second solution heat exchanger, and the fourth solution heat exchanger Adjusting to the second solution pump, the concentrated solution line is connected to the second generator via the third solution heat exchanger, the second solution heat exchanger, the fifth solution heat exchanger and the fourth solution heat exchanger, and the third generation occurs
  • the concentrated solution line is connected to the absorber through the second solution heat exchanger to be adjusted to be a third generator.
  • the concentrated solution line is connected to the fourth generator via the fifth solution heat exchanger, and the fourth generator has a concentrated solution.
  • the pipeline is connected to the absorber via the second solution heat exchanger, and the third generator has a refrigerant vapor passage connected to the second condenser to be adjusted to be a third generator having a refrigerant vapor passage connected to the fourth generator.
  • the generator further has a refrigerant liquid pipeline connected to the second condenser via the third throttle valve, and the fourth generator further has a refrigerant vapor passage communicating with the second condenser to form a three-effect-recovery type single effect third.
  • Absorption heat pump is connected to the absorber via the second solution heat exchanger
  • the third generator has a refrigerant vapor passage connected to the second condenser to be adjusted to be a third generator having a refrigerant vapor passage connected to the fourth generator.
  • a third type of absorption heat pump in the third type of absorption heat pump according to item 24, adding a fourth generator, a fifth solution heat exchanger, a third throttle valve, a fourth solution pump or a five-solution pump, the second solution pump has a concentrated solution pipeline connected to the third generator via the third solution heat exchanger and the second solution heat exchanger to adjust to a second solution pump having a concentrated solution pipeline through the third solution heat
  • the exchanger and the second solution heat exchanger are in communication with the fourth generator, and the fourth generator and the concentrated solution line are connected to the third generator via the fourth solution pump or the fifth solution pump, and the fifth solution heat exchanger
  • the second generator has a concentrated solution pipeline connected to the absorber through the fourth solution heat exchanger and the second solution heat exchanger to adjust the second generator to have a concentrated solution pipeline through the fourth solution heat exchanger, the fifth solution
  • the heat exchanger and the second solution heat exchanger are in communication with the absorber, and the third generator has a refrigerant vapor passage communicating with the second condenser to adjust the
  • the three throttle valve is in communication with the second condenser, and the fourth generator has a refrigerant vapor passage communicating with the second condenser to form a three-effect-recovery single-effect third-type absorption heat pump.
  • the third type of absorption heat pump is the third type of absorption heat pump according to item 4, wherein the third generator, the fourth solution heat exchanger and the second section are widened, and the second solution pump is passed through
  • the three-solution heat exchanger is further provided with a concentrated solution pipeline and is further connected to the third generator via the fourth solution heat exchanger, and the third generator and the concentrated solution pipeline are connected to the absorber via the fourth solution heat exchanger
  • the second generator has a refrigerant vapor passage communicating with the second condenser to adjust the second generator to have a refrigerant vapor passage communicating with the third generator, and the third generator is further provided with a refrigerant liquid pipeline via the second throttle valve
  • the second condenser is connected--the refrigerant vapor generated by the second generator is used as the driving heat medium of the third generator, and the third generator and the refrigerant vapor channel are connected with the second condenser to form a double-effect-recovery type Single-effect third-class absorption heat pump.
  • the third type of absorption heat pump is the third type of absorption heat pump according to item 4, wherein the third generator, the fourth solution heat exchanger and the second throttle valve are added, and the second solution pump is
  • the concentrated solution pipeline is connected to the second generator via the third solution heat exchanger and the second solution heat exchanger to be adjusted to a second solution pump having a concentrated solution pipeline through the third solution heat exchanger, the second solution heat exchanger, and
  • the fourth solution heat exchanger is in communication with the second generator, and the second generator has a concentrated solution line connected to the absorber via the second solution heat exchanger to adjust the second generator to have a concentrated solution line through the fourth solution heat
  • the exchanger is connected to the third generator, the third generator and the concentrated solution pipeline are connected to the absorber via the second solution heat exchanger, and the second generator has a refrigerant vapor passage connected to the second condenser to be adjusted to The second generator has a refrigerant vapor passage connected to the third generator, and the third generator and the refrigerant liquid pipeline are connected to the
  • the third type of absorption heat pump is a third type of absorption heat pump according to item 30, wherein the solution throttle valve is added, and the second solution pump has a concentrated solution line through the third solution heat exchanger, The two solution heat exchanger and the fourth solution heat exchanger are connected to the second generator to be adjusted to be the second solution pump.
  • the concentrated solution line is passed through the third solution heat exchanger and the second solution heat exchanger, and then the solution is throttled separately.
  • the valve is in communication with the third generator and is in communication with the second generator via the fourth solution heat exchanger to form a double effect-recovery single effect third type absorption heat pump.
  • the third type of absorption heat pump in the third type of absorption heat pump described in item 4, adds a third generator, a fourth solution heat exchanger, a third solution pump and a second throttle valve,
  • the second solution pump has a concentrated solution line connected to the second generator via the third solution heat exchanger and the second solution heat exchanger to adjust to a second solution pump having a concentrated solution line through the third solution heat exchanger and the second
  • the solution heat exchanger is in communication with the third generator, the third generator further has a concentrated solution line connected to the second generator via the third solution pump and the fourth solution heat exchanger, and the second generator has a concentrated solution line Passing through the second solution heat exchanger and the absorber to adjust to a second generator having a concentrated solution line communicating with the absorber via the fourth solution heat exchanger and the second solution heat exchanger, the second generator having a refrigerant vapor
  • the passage is connected to the second condenser to be adjusted so that the second generator has a refrigerant vapor passage communicating with the third generator, and then the
  • the third type of absorption heat pump is a third type of absorption heat pump according to item 32, wherein the solution throttle valve is added, and the second solution pump has a concentrated solution line through the third solution heat exchanger and The two solution heat exchanger is connected to the third generator to be adjusted to be the second solution pump.
  • the concentrated solution line is directly connected to the second generator and then passed through the solution section after passing through the third solution heat exchanger and the second solution heat exchanger.
  • the flow valve is in communication with the third generator to form a double-effect regenerative single-effect third-class absorption heat pump.
  • the third type of absorption heat pump is the third type of absorption heat pump according to item 29, wherein the fourth generator, the fifth solution heat exchanger and the third throttle valve are added, and the second solution pump is passed through
  • the three-solution heat exchanger is further provided with a concentrated solution pipeline and is further connected to the fourth generator via the fifth solution heat exchanger, and the fourth generator and the concentrated solution pipeline are connected to the absorber through the fifth solution heat exchanger, and the first
  • the third generator has a refrigerant vapor passage communicating with the second condenser to adjust the third generator to have a refrigerant vapor passage communicating with the fourth generator, and then the fourth generator has a refrigerant liquid pipeline flowing through the third section
  • the second condenser is connected, and the fourth generator further has a refrigerant vapor passage communicating with the second condenser to form a three-effect-recovery type single-effect third-type absorption heat pump.
  • the third type of absorption heat pump is the third type of absorption heat pump according to item 30, wherein the fourth generator, the fifth solution heat exchanger and the third throttle are added, and the second solution pump is
  • the concentrated solution pipeline is connected to the second generator via the third solution heat exchanger, the second solution heat exchanger and the fourth solution heat exchanger to be adjusted to be a second solution pump having a concentrated solution pipeline through the third solution heat exchanger,
  • the second solution heat exchanger, the fifth solution heat exchanger and the fourth solution heat exchanger are in communication with the second generator
  • the third generator has a concentrated solution line connected to the absorber via the second solution heat exchanger to be adjusted to
  • the third generator has a concentrated solution line communicating with the fourth generator via the fifth solution heat exchanger, and the fourth generator and the concentrated solution line are connected to the absorber via the second solution heat exchanger, and the third generator is
  • the refrigerant vapor passage is connected to the second condenser to be adjusted to be a third generator having a refrigerant vapor passage communicating with the fourth generator
  • the third type of absorption heat pump is a third type of absorption heat pump according to item 32, adding a fourth generator, a fifth solution heat exchanger, a third throttle valve and a fourth solution pump,
  • the second solution pump has a concentrated solution pipeline connected to the third generator via the third solution heat exchanger and the second solution heat exchanger to adjust the second solution pump to have a concentrated solution pipeline through the third solution heat exchanger and the second
  • the solution heat exchanger is in communication with the fourth generator, and the fourth generator further has a concentrated solution line connected to the third generator via the fourth solution pump and the fifth solution heat exchanger, and the second generator has a concentrated solution line
  • the fourth solution heat exchanger and the second solution heat exchanger are connected to the absorber to be adjusted to have a second solution having a concentrated solution line through the fourth solution heat exchanger, the fifth solution heat exchanger and the second solution heat exchanger
  • the third generator has a refrigerant vapor passage communicating with the second condenser to be adjusted to a third generator having a refrigerant vapor
  • the third type of absorption heat pump is the single-effect single-effect type III absorption heat pump mentioned in item 1 and the 5-12
  • a new generator, a new solution heat exchanger, a new throttle and a new solution pump are added, and a diluent solution is added to the absorber.
  • the solution heat exchanger is connected to the newly added generator, and the new generator and the concentrated solution pipeline are passed through the new solution pump and the newly added solution heat exchanger, and after the first generator is passed through the solution pump and the first solution heat exchanger.
  • the concentrated solution pipeline meets, and the first generator has a refrigerant vapor passage connected to the first condenser to be adjusted to be a first generator having a refrigerant vapor passage connected with the newly added generator, and then adding a new generator and then a refrigerant liquid.
  • the pipeline is connected to the first condenser via a new throttle valve, and a new generator and a refrigerant vapor passage are connected with the first condenser to form a third type of absorption heat pump with a double effect as a low temperature generation process.
  • the third type of absorption heat pump is the single-effect single-effect type III absorption heat pump mentioned in item 1 and the third type of absorption heat pump described in any of items 5-12. Adding a new generator, a new solution heat exchanger and a new throttle valve, and adjusting the first generator having a concentrated solution line through the solution pump and the first solution heat exchanger and the second solution heat exchanger to adjust A generator has a concentrated solution line connected to the newly added generator through the new solution heat exchanger, and the new generator has a concentrated solution line through the solution pump, the new solution heat exchanger and the first solution heat exchanger.
  • the second solution heat exchanger is connected, and the first generator has a refrigerant vapor channel connected to the first condenser to be adjusted to be a first generator having a refrigerant vapor channel connected with the newly added generator, and then adding a generator and then a refrigerant
  • the liquid pipeline is connected to the first condenser via a new throttle valve, and a new generator and a refrigerant vapor passage are connected with the first condenser to form a third type of absorption heat pump with a double effect as a low temperature generation process.
  • the third type of absorption heat pump is the single-effect single-effect type III absorption heat pump mentioned in item 1 and the third type absorption heat pump according to any of items 5-12.
  • the dilute solution pipeline is connected to the newly added generator through the first solution heat exchanger and the new solution heat exchanger, and the new generator and the concentrated solution pipeline are added to the new solution pump and the newly added solution heat exchanger and the first
  • the generator is connected, and the first generator has a refrigerant vapor passage connected to the first condenser to be adjusted to be a first generator having a refrigerant vapor passage connected with the newly added generator, and then adding a generator and then a refrigerant liquid pipeline
  • a new throttle valve is connected to the first condenser, and a new generator and a refrigerant
  • the third type of absorption heat pump in the third type of absorption heat pump described in item 37, adds a new second generator, adds a second solution heat exchanger, adds a second throttle valve, and Adding a second solution pump, adding a dilute solution pipeline to the absorber, and adding a second solution heat exchanger to connect with the newly added second generator, adding a second generator and a concentrated solution pipeline to add a second solution
  • the first first generator has a refrigerant vapor channel and the first condensation
  • the communication is adjusted to add a first generator with a refrigerant vapor channel and a new second generator is connected, a second generator is added, and a refrigerant liquid pipeline is added through the second throttle valve and the first condenser. Connected, a new second generator and a refrigerant vapor passage are connected to the first condenser to form a third type
  • the third type of absorption heat pump is a third type of absorption heat pump according to item 38, adding a new second generator, adding a second solution heat exchanger and adding a second section of the flow. Adding a first generator with a concentrated solution pipeline through a solution pump, adding a first solution heat exchanger, and a first solution heat exchanger to the second solution heat exchanger to adjust to a new first generator having a concentrated solution
  • the pipeline is connected with the newly added second generator through the newly added second solution heat exchanger, and the second generator and the concentrated solution pipeline are added through the solution pump, the second solution heat exchanger is added, and the first solution is added.
  • the heat exchanger and the first solution heat exchanger are in communication with the second solution heat exchanger, and the newly added first generator has a refrigerant vapor passage connected to the first condenser to be adjusted to add a first generator having a refrigerant vapor passage
  • the second generator is added, and the refrigerant liquid pipeline is connected with the first condenser through the addition of the second throttle valve, and the second generator and the refrigerant vapor passage are added.
  • the first condenser is connected to form a third type of absorption with a three-effect process Heat pump. 42.
  • the third type of absorption heat pump is a third type of absorption heat pump according to item 39, adding a new second generator, adding a second solution heat exchanger, adding a second throttle valve and A second solution pump is newly added, and the absorber has a dilute solution pipeline through the first solution heat exchanger and the newly added first solution heat exchanger is connected with the newly added first generator to adjust the absorber to a dilute solution pipeline.
  • a solution heat exchanger, a new first solution heat exchanger and a new second solution heat exchanger are connected to the newly added second generator, and a second generator and a concentrated solution line are added to the second solution.
  • the pump and the newly added second solution heat exchanger are connected with the newly added first generator, and the newly added first generator has a refrigerant vapor passage connected to the first condenser to adjust the newly added first generator to have a refrigerant vapor passage.
  • the second generator is connected, the second generator is added, and the refrigerant liquid pipeline is connected with the first condenser through the addition of the second throttle valve, and the second generator and the refrigerant vapor passage are added.
  • the first condenser is connected to form a third type of absorption heat pump with a three-effect low temperature generation process .
  • the third type of absorption heat pump is a third type of absorption heat pump according to any one of items 1, 13-20, adding a new generator, a new solution heat exchanger and an additional section.
  • the flow valve, the second solution pump is provided with a dilute solution pipeline, and the new solution heat exchanger is connected with the newly added generator, and the new generator and the concentrated solution pipeline are connected to the third generator via the new solution heat exchanger.
  • the first generator has a refrigerant vapor passage connected to the first condenser to be adjusted to be a first generator having a refrigerant vapor passage connected with the newly added generator, and then adding a new generator and then a refrigerant liquid pipeline is newly throttled
  • the valve is in communication with the first condenser, and the new generator and the refrigerant vapor passage are in communication with the first condenser to form a third type of absorption heat pump having a regenerative double effect as a low temperature generation process.
  • the third type of absorption heat pump is a third type of absorption heat pump according to any one of items 1, 13-20, adding a new generator, a new solution heat exchanger and an additional section. a flow valve, wherein the second solution pump has a dilute solution line connected to the first generator via the third solution heat exchanger to adjust to a second solution pump having a dilute solution line through the new solution heat exchanger and the third solution heat exchange
  • the device is connected to the first generator, and the first generator has a concentrated solution pipeline connected to the third generator via the third solution heat exchanger to adjust the first generator to have a concentrated solution pipeline through the third solution heat exchanger and
  • the new generator is connected, the new generator and the concentrated solution pipeline are connected to the third generator via the newly added solution heat exchanger, and the first generator has a refrigerant vapor passage connected to the first condenser to be adjusted to the first
  • the generator has a refrigerant vapor passage connected with the newly added generator, and then a new generator is added, and the refrigerant liquid pipeline
  • the third type of absorption heat pump is a third type of absorption heat pump according to any one of items 1, 13-20, adding a new generator, a new solution heat exchanger, and an additional section. a flow valve and a new solution pump, the second solution pump has a dilute solution line connected to the first generator via the third solution heat exchanger to adjust to a second solution pump having a dilute solution line through the third solution heat exchanger and New generator connection, new generator and concentrated solution pipeline are connected to the first generator via the new solution pump and the new solution heat exchanger, and the first generator has a concentrated solution pipeline through the third solution heat.
  • the exchanger is connected to the third generator and adjusted to be a first generator having a concentrated solution pipeline connected to the third generator via the new solution heat exchanger and the third solution heat exchanger, and the first generator has a refrigerant vapor passage
  • the first condenser is connected to the first condenser to adjust the first generator to have a refrigerant vapor channel connected with the newly added generator, and then the new generator is connected to the first condenser through the newly added throttle valve.
  • the generator also has a refrigerant vapor passage communicating with the first condenser, In double-effect heat recovery at a low temperature occurs in the third flow type absorption heat pump.
  • the third type of absorption heat pump is the third type of absorption heat pump according to any one of items 43 to 45, wherein the waste heat medium line connecting the third generator to the outside is canceled, and the additional number is added.
  • the second flow is wide, the first generator is connected with the refrigerant vapor passage and the third generator is connected, and the third generator is further connected with the first condenser through the addition of the second throttle valve through the second throttle valve, forming a back
  • the thermal double effect is the third type of absorption heat pump for the low temperature generation process.
  • the third type of absorption heat pump is a third type of absorption heat pump according to item 43, adding a new second generator, adding a second solution heat exchanger and adding a second throttle valve.
  • the second solution pump adds a dilute solution line through the addition of the second solution
  • the heat exchanger is connected to the newly added second generator, and the second generator and the concentrated solution pipeline are connected to the third generator via the newly added second solution heat exchanger, and the first generator is added with the refrigerant.
  • the steam passage is connected to the first condenser to be adjusted to add a first generator.
  • the refrigerant vapor passage is connected with the newly added second generator, and the second generator is added, and the refrigerant liquid pipeline is added with the second throttle.
  • the valve is in communication with the first condenser, and the second generator and the refrigerant vapor passage are connected to the first condenser to form a third type of absorption heat pump in which the regenerative three-effect is a low temperature generation process.
  • the third type of absorption heat pump is a third type of absorption heat pump according to item 44, adding a new second generator, adding a second solution heat exchanger and adding a second section of the flow.
  • the second solution pump has a dilute solution pipeline connected to the first generator via the newly added first solution heat exchanger and the third solution heat exchanger to adjust to a second solution pump having a dilute solution pipeline and adding a second solution heat
  • the exchanger, the first solution heat exchanger and the third solution heat exchanger are connected to the first generator, and the first generator has a concentrated solution pipeline added by the first solution heat exchanger and the third generation occurs
  • the device is connected to adjust the new first generator to have a concentrated solution pipeline.
  • the new first solution heat exchanger is connected with the newly added second generator, and the second generator and the concentrated solution pipeline are added by the second.
  • the solution heat exchanger is in communication with the third generator, and the newly added first generator has a refrigerant vapor passage connected to the first condenser to be adjusted to add a first generator having a refrigerant vapor passage and a new second generator.
  • After adding a second generator there is a refrigerant liquid pipeline added by the second section.
  • the third type of absorption heat pump in the third type of absorption heat pump described in item 45, adds a new second generator, adds a second solution heat exchanger, adds a second throttle valve, and A second solution pump is newly added, and the second solution pump has a dilute solution line connected to the newly added first generator through the third solution heat exchanger to be adjusted to a second solution pump having a dilute solution line through the third solution heat exchanger Connected with the newly added second generator, the second generator and the concentrated solution pipeline are connected to the newly added first generator via the newly added second solution pump and the newly added second solution heat exchanger, which will occur first.
  • the concentrated solution line is connected to the third generator through the addition of the first solution heat exchanger and the third solution heat exchanger to the second generator.
  • the second generator has a concentrated solution line through the addition of the first solution heat exchanger, new The second solution heat exchanger and the third solution heat exchanger are connected to the third generator, and the newly added first generator has a refrigerant vapor channel connected to the first condenser to adjust the newly added first generator to have a refrigerant Add a second generator after the steam channel is connected to the new second generator.
  • the refrigerant liquid pipeline is connected to the first condenser via a new second throttle valve, and a second generator and a refrigerant vapor passage are connected to the first condenser to form a regenerative three-effect low temperature generating process.
  • the third type of absorption heat pump is connected to the first condenser via a new second throttle valve, and a second generator and a refrigerant vapor passage are connected to the first condenser to form a regenerative three-effect low temperature generating process.
  • the third type of absorption heat pump is the third type of absorption heat pump according to any one of items 47-49, wherein the waste heat medium line connecting the third generator to the outside is canceled, and the additional number is added.
  • a three-way valve the first generator is connected with a refrigerant vapor passage and is connected with the third generator, and the third generator is further connected with the first condenser through a new third throttle valve, and is formed by three A regenerative third type absorption heat pump that functions as a low temperature generation process.
  • the third type of absorption heat pump is a third type of absorption heat pump according to any of the items 47-49, wherein the waste heat medium line connecting the third generator to the outside is canceled, and a third is added.
  • the throttle valve is newly added to the first generator to add a refrigerant vapor passage to communicate with the third generator, and the third generator and the refrigerant liquid pipeline are connected to the first condenser via a new third throttle valve to form
  • the regenerative three-effect is the third type of absorption heat pump for the low temperature generation process.
  • the third type of absorption heat pump is a third type of absorption heat pump according to any one of items 2-3, 21-28, adding a new generator, a new solution heat exchanger and a new one.
  • the throttle valve is added, and the first generator has a concentrated solution pipeline connected to the first solution pump, the first solution heat exchanger, and the absorption-generator and the steam distribution chamber to adjust the first generator to have a concentrated solution pipeline
  • a solution heat exchanger and an absorption-generator are connected to the steam distribution chamber, and the absorption-generator adds a dilute solution pipeline through the new solution heat exchanger to communicate with the newly added generator, and the new generator and the concentrated solution pipeline are
  • the first solution pump and the newly added solution heat exchanger are merged with the first generator through the concentrated solution line after the first solution heat exchanger, and the first generator has a refrigerant vapor channel and the first
  • the condenser is connected to adjust to the first generator, and the refrigerant vapor channel is connected with the newly added generator,
  • the third type of absorption heat pump is a third type of absorption heat pump according to any one of items 2-3, 21-28, adding a new generator, adding a new throttle valve and adding a solution throttle valve, the first generator has a concentrated solution pipeline connected to the first solution pump, the first solution heat exchanger, and the absorption-generator and the steam distribution chamber to adjust the first generator to have a concentrated solution pipeline through the solution
  • the throttle valve and the absorption-generator are connected to the steam distribution chamber, and the absorption-generator has a dilute solution pipeline connected to the first generator through the first solution heat exchanger to adjust to absorption-the generator has a dilute solution pipeline directly
  • the first generator is connected, the absorption-generator adds a dilute solution pipeline through the first solution heat exchanger to communicate with the newly added generator, and the new generator and the concentrated solution pipeline are exchanged with the first solution pump and the first solution.
  • the first generator After the first generator is merged with the concentrated solution pipeline after the solution throttle valve, the first generator has a refrigerant vapor passage connected to the first condenser, and the first generator has a refrigerant vapor passage and newly added After the generator is connected, the generator is added and the coolant line is new.
  • the throttle valve is in communication with the first condenser, and the new generator and the refrigerant vapor passage are in communication with the first condenser; canceling the refrigerant vapor passage of the first evaporator or the second evaporator and the absorption-generator,
  • a generator adds a refrigerant vapor channel to communicate with the absorption-generator, cancels the third solution pump, and the absorber has a dilute solution line connected to the absorption-generator via the third solution heat exchanger to form a regenerative double effect
  • the third type of absorption heat pump for the low temperature generation process is in communication with the first condenser, and the new generator and the refrigerant vapor passage are in communication with the first condenser; canceling the refrigerant vapor passage of the first evaporator or the second evaporator and the absorption-generator,
  • a generator adds a refrigerant vapor channel to communicate with the absorption-generator, cancels the third
  • the third type of absorption heat pump is a third type of absorption heat pump according to any one of items 2-3, 21-28, adding a new generator, a new solution heat exchanger and a new one.
  • the throttle valve is added, and the first generator has a concentrated solution pipeline connected to the first solution pump, the first solution heat exchanger, and the absorption-generator and the steam distribution chamber to adjust the first generator to have a concentrated solution pipeline through the new
  • the solution heat exchanger is connected to the newly added generator, and the new generator and the concentrated solution line are passed through the first solution pump, the new solution heat exchanger, the first solution heat exchanger, and the absorption-generator and the steam distribution chamber.
  • the first generator has a refrigerant vapor passage connected to the first condenser, and the first generator has a refrigerant vapor passage connected with the newly added generator, and the new generator is further added with a refrigerant liquid pipeline.
  • the throttle valve is in communication with the first condenser, and the new generator and the refrigerant vapor passage are in communication with the first condenser to form a third type of absorption heat pump having a regenerative double effect as a low temperature generation process.
  • the third type of absorption heat pump is a third type of absorption heat pump according to any one of items 2-3, 21-28, adding new generators and adding new throttle, which will absorb - the generator has a dilute solution line connected to the first generator via the first solution heat exchanger to adjust to absorption - the generator has a dilute solution line directly communicating with the first generator, the first generator having a concentrated solution line
  • the first solution pump, the first solution heat exchanger and the absorption-generator are connected to the steam separation chamber to be adjusted to be the first generator, and the concentrated solution pipeline is connected to the newly added generator through the first solution heat exchanger, and the addition occurs.
  • the concentrated solution pipeline is connected to the steam distribution chamber through the first solution pump, the first solution heat exchanger and the absorption-generator, and the first generator has a refrigerant vapor passage connected to the first condenser to be adjusted to the first
  • the generator has a refrigerant vapor passage connected with the newly added generator, and then a new generator is added, and the refrigerant liquid pipeline is connected to the first condenser via a new throttle valve, and the new generator has a refrigerant vapor passage and a first a condenser is connected; cancel the first evaporator or the second evaporator and absorb-transmit a refrigerant vapor passage connected to the refrigerant, the first generator adds a refrigerant vapor passage to communicate with the absorption-generator, cancels the third solution pump, and the absorber has a dilute solution pipeline connected to the absorption-generator via the third solution heat exchanger
  • the third type of absorption heat pump is a third type of absorption heat pump according to any one of items 2-3, 21-28, adding a new generator, a new solution heat exchanger, and a new one.
  • the throttle valve and the new solution pump are added, and the absorption-generator has a dilute solution line connected to the first generator through the first solution heat exchanger to be adjusted to absorb-the generator has a dilute solution line first solution heat exchanger
  • the new solution heat exchanger is connected with the newly added generator, the new generator and the concentrated solution pipeline are connected to the first generator through the new solution pump and the new solution heat exchanger, and the first generator is cooled.
  • the steam passage of the agent is connected to the first condenser to be adjusted so that the first generator has a refrigerant vapor passage connected with the newly added generator, and the new generator is further provided with a refrigerant liquid pipeline through the newly added throttle valve and the first A condenser is connected, and a new generator and a refrigerant vapor passage are connected to the first condenser to form a third type of absorption heat pump with a regenerative double effect as a low temperature generation process.
  • the third type of absorption heat pump is a third type of absorption heat pump according to any one of items 2-3, 21-28, adding a new generator, a new solution throttle valve and a new one.
  • the throttle valve is added, and the first generator has a concentrated solution pipeline connected to the first solution pump, the first solution heat exchanger, and the absorption-generator and the steam distribution chamber to adjust the first generator to have a concentrated solution pipeline through the new
  • the increasing solution throttle valve and the absorption-generator are connected to the steam distribution chamber, and the absorption-generator has a dilute solution pipeline connected to the first generator through the first solution heat exchanger to adjust to an absorption-generator with a dilute solution pipeline
  • the first solution heat exchanger is connected to the newly added generator, and the new generator and the concentrated solution pipeline are connected to the first generator via the first solution pump and the first solution heat exchanger, and the first generator has a refrigerant.
  • the steam passage is connected to the first condenser to be adjusted so that the first generator has a refrigerant vapor passage connected with the newly added generator, and then the new generator is connected, and the refrigerant liquid pipeline is connected to the first condenser via the newly added throttle valve.
  • the new generator also has a refrigerant vapor passage that communicates with the first condenser;
  • the evaporator or the second evaporator is connected to the refrigerant vapor passage of the absorption-generator, the first generator is connected with the refrigerant vapor passage and communicates with the absorption-generator, cancels the third solution pump, and the absorber has a dilute solution pipeline.
  • the three-solution heat exchanger is in communication with the absorption-generator to form a third type of absorption heat pump with a regenerative double effect as a low temperature generation process.
  • the third type of absorption heat pump is a third type of absorption heat pump according to item 52, adding a second generator, adding a second solution heat exchanger and adding a second throttle valve. Adding a new first generator with a concentrated solution line through the first solution pump and adding a first solution heat exchanger to merge with the first generator through the first solution heat exchanger after the concentrated solution line is adjusted to be newly added
  • the first generator has a concentrated solution pipeline which is merged with the concentrated solution pipeline after the first generator passes through the first solution heat exchanger after adding the first solution heat exchanger, and the absorption-generator adds a dilute solution pipeline through the new
  • the second solution heat exchanger is connected with the newly added second generator, and the second generator and the concentrated solution pipeline are added to the first generator through the first solution pump and the second solution heat exchanger.
  • the second generator is added and the refrigerant liquid pipeline is added.
  • a second throttle valve is connected to the first condenser, and a second generator and a refrigerant vapor passage are connected to the first condenser to form a third type of absorption with a regenerative three-effect process. Heat pump.
  • the third type of absorption heat pump in the third type of absorption heat pump described in item 53, adds a new second generator, a new solution heat exchanger and a new second section, which will be new.
  • Increasing the first generator has a concentrated solution pipeline through the first solution pump and the first solution heat exchanger and the first generator through the new solution throttle valve after the concentrated solution pipeline is adjusted to be added to the first generator
  • the concentrated solution pipeline passes through the first solution heat exchanger and merges with the concentrated solution pipeline of the first generator after adding the solution throttle valve, and the absorption-generator adds a dilute solution pipeline through the newly added solution heat exchanger and the new
  • the second generator is connected, and the second generator and the concentrated solution pipeline are added after the first solution pump and the new solution heat exchanger are connected to the first generator through the new solution throttle valve.
  • the first generator is added with a refrigerant vapor channel and the first condenser is connected to adjust to add a new generator.
  • the refrigerant vapor channel is connected with the newly added second generator, and the second generator is added.
  • the refrigerant liquid pipeline is added with the second throttle valve and the first condenser Pass, as well as the new refrigerant vapor passage in communication with the second generator of the first condenser, recuperative form a three-way flow of the third occurrence of low absorption heat pump.
  • the third type of absorption heat pump is a third type of absorption heat pump according to item 59, wherein the absorption-generator has a dilute solution line directly connected to the first generator to be adjusted to an absorption-generator
  • the solution pipeline is connected to the first generator via the first solution heat exchanger, and the first generator has a concentrated solution pipeline connected to the first generator via the new solution throttle valve and the absorption-generator and the steam distribution chamber.
  • the concentrated solution pipeline is connected to the steam distribution chamber through the first solution heat exchanger and the absorption-generator, and the absorption-generator has a dilute solution pipeline connected to the newly added first generator through the first solution heat exchanger to be adjusted to
  • the absorption-generator has a dilute solution line directly connected to the newly added first generator, and the newly added first generator has a concentrated solution line that is connected to the first solution heat exchanger and the absorption-generator and the steam distribution chamber to adjust Added first generator with concentrated solution pipeline via new solution throttle valve and absorption-occurrence
  • the device is connected to the steam distribution chamber, and the first generator has a refrigerant vapor passage and an absorption-generator connection, and is adjusted to be a new first generator having a refrigerant vapor passage and an absorption-generator connected to form a regenerative three-effect
  • the third type of absorption heat pump for low temperature generation processes is connected to the steam distribution chamber through the first solution heat exchanger and the absorption-generator, and
  • the third type of absorption heat pump is a third type of absorption heat pump according to item 54, adding a new second generator, adding a second solution heat exchanger and adding a second throttle valve. Adding a new first generator with a concentrated solution pipeline through the first solution pump and adding a first solution heat exchanger to the first solution heat exchanger to adjust to add a new first generator with a concentrated solution pipeline added
  • the second solution heat exchanger is connected with the newly added second generator, and the second generator and the concentrated solution line are added through the first solution pump, the second solution heat exchanger is added, and the first solution heat exchanger is added.
  • the second generator further has a refrigerant liquid pipeline connected to the first condenser via a new second throttle valve, and a second generator and a refrigerant vapor passage are connected to the first condenser to form a heat recovery.
  • the third type of absorption heat pump is a third type of low temperature generation process.
  • the third type of absorption heat pump is the third type of absorption heat pump described in item 55.
  • the addition of the second generator, the new solution heat exchanger and the addition of the second throttle valve will be new.
  • the first generator has a concentrated solution pipeline connected to the first solution heat exchanger via the first solution pump and is adjusted to be a new first generator having a concentrated solution pipeline via a new solution heat exchanger and a second addition generator Connected, the second generator and the concentrated solution pipeline are connected to the first solution heat exchanger via the first solution pump and the new solution heat exchanger, and the first generator has a refrigerant vapor passage and the first
  • the condenser is connected to adjust the new first generator to have a refrigerant vapor channel and the second generator is connected to add a second generator, and then the refrigerant liquid pipeline is added with the second throttle valve and the first condensation
  • the device is connected, and a second generator and a refrigerant vapor channel are connected to the first condenser to form a third type of absorption heat
  • the third type of absorption heat pump is the third type of absorption heat pump described in item 62.
  • the new solution pump is added, and the absorption-generator has a dilute solution line directly connected to the first generator.
  • the absorption-generator has a dilute solution pipeline connected to the first generator via the new solution pump and the first solution heat exchanger, and the second generator has a concentrated solution pipeline through the first solution pump and the new solution heat
  • the exchanger is connected to the first solution heat exchanger to be adjusted to add a second generator.
  • the concentrated solution pipeline is connected to the absorption generator via the first solution pump and the new solution heat exchanger, and the first generator has a refrigerant.
  • the steam passage and the absorption-generator connection are adjusted to add a first generator having a refrigerant vapor passage communicating with the absorption-generator to form a third type of absorption heat pump having a regenerative three-effect low temperature generation process.
  • the third type of absorption heat pump is a third type of absorption heat pump according to item 56, adding a new second generator, adding a second solution heat exchanger, adding a second throttle valve and Adding a second solution pump, adjusting the absorption-generator dilute solution line through the first solution heat exchanger and adding the first solution heat exchanger to the newly added first generator to adjust to the absorption-generator with dilute solution
  • the pipeline is connected to the newly added second generator via the first solution heat exchanger, the newly added first solution heat exchanger and the newly added second solution heat exchanger, and the second generator and the concentrated solution pipeline are newly added.
  • the second solution pump and the newly added second solution heat exchanger are connected with the newly added first generator, and the newly added first generator has a refrigerant vapor channel connected to the first condenser and is adjusted to be a new first generator.
  • the refrigerant vapor channel is connected with the newly added second generator, and the second generator is added, and the refrigerant liquid pipeline is connected with the first condenser through the addition of the second throttle valve, and the second generator is added with cold.
  • the vapor channel of the agent is in communication with the first condenser, and is formed in a regenerative three-effect manner to occur at a low temperature.
  • the third process type absorption heat pump is used to pump.
  • the third type of absorption heat pump is the addition of the second generator, the new solution heat exchanger, the addition of the second throttle valve and the addition of the third type of absorption heat pump described in item 57.
  • the solution pump, the absorption-generator has a dilute solution line
  • the first solution heat exchanger is connected with the newly added first generator, and is adjusted to absorb-the generator has a dilute solution line through the first solution heat exchanger and the new solution heat
  • the exchanger is connected to the newly added second generator, and the second generator and the concentrated solution pipeline are connected to the newly added first generator via the new solution pump and the new solution heat exchanger, and the first occurrence occurs.
  • a refrigerant vapor passage and a first condenser The connection is adjusted to add a first generator with a refrigerant vapor channel and a new second generator is connected, a second generator is added, and a refrigerant liquid pipeline is connected to the first condenser via a new second throttle valve.
  • a second generator and a refrigerant vapor passage are connected to the first condenser to form a third type of absorption heat pump with a regenerative three-effect process.
  • the third type of absorption heat pump is the third type of absorption heat pump described in item 65.
  • the new solution throttle valve is cancelled, and the first generator has a concentrated solution line through the newly added solution throttle valve.
  • the absorption-generator is connected to the steam separation chamber to adjust to the first generator, the concentrated solution pipeline is connected to the steam distribution chamber through the first solution heat exchanger and the absorption-generator, and the absorption-generator has a dilute solution pipeline
  • the first solution heat exchanger and the newly added solution heat exchanger are connected to the newly added second generator to be adjusted to be an absorption-generator having a dilute solution line connected to the newly added second generator via the newly added solution heat exchanger,
  • a generator has a refrigerant vapor channel and an absorption-generator connection adjusted to add a first generator to add a refrigerant vapor channel to communicate with the absorption-generator to form a third type of absorption with a regenerative three-effect process for low temperature generation. Heat pump.
  • the third type of absorption heat pump is a third type of absorption heat pump according to any one of items 4, 29-36, adding a new generator, a new solution heat exchanger, and an additional section. Flow valve and new solution pump, absorption-generator added dilute solution pipeline through new solution heat exchanger and new generator connected, new generator and concentrated solution pipeline through new solution pump and new solution
  • the heat exchanger is connected to the absorption-generator, and the first generator has a refrigerant vapor passage connected to the first condenser, and is adjusted to be a first generator having a refrigerant vapor passage connected with the newly added generator, and then adding a new generator.
  • the refrigerant liquid pipeline is connected to the first condenser via a new throttle valve, and the newly added generator and the refrigerant vapor passage are connected with the first condenser to form a third type in which the regenerative double effect is a low temperature generating process.
  • Absorption heat pump is used to pump the refrigerant liquid pipeline to form a third type in which the regenerative double effect is a low temperature generating process.
  • the third type of absorption heat pump is a third type of absorption heat pump according to any one of items 4, 29-36, adding a new generator, a new solution heat exchanger and an additional section.
  • a flow valve the first generator has a concentrated solution pipeline connected to the first solution pump and the first solution heat exchanger and the absorption-generator to adjust the first generator to have a concentrated solution pipeline through the new solution heat exchanger and New generator connection, new generator and concentrated solution pipeline are connected to the absorption-generator via the first solution pump, the new solution heat exchanger and the first solution heat exchanger, and the first generator has a refrigerant
  • the steam passage is connected to the first condenser to be adjusted so that the first generator has a refrigerant vapor passage connected with the newly added generator, and then the new generator is connected, and the refrigerant liquid pipeline is connected to the first condenser via the newly added throttle valve.
  • the new generator also has a refrigerant vapor passage that communicates with the first condenser to form
  • the third type of absorption heat pump is a third type of absorption heat pump according to any one of items 4, 29-36, adding a new generator, a new solution heat exchanger, and an additional section.
  • the absorption-generator has a dilute solution line connected to the first generator through the first solution heat exchanger to adjust to absorption-generator with dilute solution line first solution heat exchanger and new
  • the increasing solution heat exchanger is connected with the newly added generator, and the newly added generator and the concentrated solution pipeline are connected to the first generator via the new solution pump and the newly added solution heat exchanger, and the first generator has the refrigerant vapor.
  • the passage is connected to the first condenser to be adjusted so that the first generator has a refrigerant vapor passage connected with the newly added generator, and then the new generator is connected, and the refrigerant liquid pipeline is connected to the first condenser via the newly added throttle valve.
  • the generator and the refrigerant vapor passage are in communication with the first condenser to form a third type of absorption heat pump with a regenerative double effect as a low temperature generation process.
  • the third type of absorption heat pump is a third type of absorption heat pump according to item 67, adding a new second generator, adding a second solution heat exchanger, adding a second section of the flow and A second solution pump is added, and an absorption-generator is added to the dilute solution line.
  • the second solution heat exchanger is added to connect with the newly added second generator, and the second generator and the concentrated solution line are added.
  • the two solution pump and the newly added second solution heat exchanger are connected with the absorption-generator, and the newly added first generator has a refrigerant vapor passage connected with the first condenser to adjust the newly added first generator to have a refrigerant vapor passage.
  • the first condenser is connected to form a third type of absorption heat pump in which the regenerative three-effect is a low temperature generation process.
  • the third type of absorption heat pump is a third type of absorption heat pump according to item 68, adding a new second generator, adding a second solution heat exchanger and adding a second throttle valve.
  • the second solution heat exchanger is connected with the newly added second generator, and the second generator and the concentrated solution line are added through the first solution pump, the second solution heat exchanger is added, and the first solution heat exchanger is added.
  • the second generator further has a refrigerant liquid pipeline connected to the first condenser via a new second throttle valve, and a second generator and a refrigerant vapor passage are connected to the first condenser to form a heat recovery.
  • the third type of absorption heat pump is a third type of low temperature generation process.
  • the third type of absorption heat pump in the third type of absorption heat pump described in item 69, adds a new second generator, adds a second solution heat exchanger, adds a second throttle valve, and Adding a second solution pump, adjusting the absorption-generator dilute solution line through the first solution heat exchanger and adding the first solution heat exchanger to the newly added first generator to adjust to the absorption-generator with dilute solution
  • the pipeline is connected to the newly added second generator via the first solution heat exchanger, the newly added first solution heat exchanger and the newly added second solution heat exchanger, and the second generator and the concentrated solution pipeline are newly added.
  • the second solution pump and the newly added second solution heat exchanger are connected with the newly added first generator, and the newly added first generator has a refrigerant vapor channel connected to the first condenser and is adjusted to be a new first generator.
  • the refrigerant vapor channel is connected with the newly added second generator, and the second generator is added, and the refrigerant liquid pipeline is connected with the first condenser through the addition of the second throttle valve, and the second generator is added with cold.
  • the vapor channel of the agent is in communication with the first condenser, and is formed in a regenerative three-effect manner to occur at a low temperature.
  • the third process type absorption heat pump is used to pump.
  • the third type of absorption heat pump is the single-effect single-effect type III absorption heat pump mentioned in item 1 and the third type of absorption heat pump described in any of items 5-12.
  • a dilute solution line for the absorber is connected to the newly added absorption-evaporator via the new solution heat exchanger, and the new absorption-evaporator and the dilute solution line are connected to the first generator via the first solution heat exchanger.
  • the first generator has a concentrated solution pipeline connected to the first solution pump and the first solution heat exchanger and the second solution heat exchanger to adjust the first generator to have a concentrated solution pipeline through the first solution pump, the first solution
  • the heat exchanger and the newly added solution heat exchanger are connected to the second solution heat exchanger
  • the evaporator has a refrigerant vapor passage connected to the absorber to adjust the evaporator to have a refrigerant vapor passage and communicate with the newly added absorption-evaporator, and evaporate
  • the first condenser adds a refrigerant liquid pipeline through the newly added refrigerant
  • the absorption-evaporator is added, and then the refrigerant vapor channel is connected with the absorber, or the second condenser is added with the refrigerant liquid pipeline through the newly added throttle valve and newly absorbed-
  • a new absorption-evaporator is added, and then a refrigerant vapor channel is
  • the third type of absorption heat pump is the single-effect single-effect third-type absorption heat pump mentioned in item 1 and the third type absorption heat pump according to any one of items 5-12.
  • the solution provider has a concentrated solution line connected to the new absorption-evaporator via a new solution heat exchanger, a new absorption-evaporator and a dilute solution line via a new solution pump and a new solution heat exchanger and absorption
  • the device is connected, and the evaporator has a refrigerant vapor channel connected to the absorber to adjust the evaporator to have a refrigerant vapor channel connected with the new absorption-evaporator, and the evaporator or the first condenser adds a refrigerant liquid pipeline through the newly added cold.
  • the absorption-evaporator is added, and then the refrigerant vapor channel is connected with the absorber, or the second condenser is added with the refrigerant liquid pipeline through the newly added throttle valve and newly absorbed.
  • - Adding an absorption-evaporator and then a refrigerant vapor channel and absorber after the evaporator is connected Connected to form a third type of absorption heat pump with a stage of 0.5 low temperature generation.
  • the third type of absorption heat pump is the single-effect single-effect third-type absorption heat pump mentioned in item 1 and the third type absorption heat pump according to any one of items 5-12.
  • the refrigerant vapor passage is connected with the newly added absorption-evaporator, and the evaporator or the first condenser is added with a refrigerant liquid pipeline.
  • the new refrigerant liquid pump is connected with the new absorption-evaporator to add an absorption-evaporator.
  • the refrigerant vapor passage is connected to the absorber, or the second condenser is provided with a refrigerant liquid.
  • the pipeline is connected to the new absorption-evaporator via a new throttle valve, and then a new absorption-evaporator is connected to the refrigerant vapor passage to communicate with the absorber to form a third type of absorption type with a lower temperature generation process of 1.5. Heat pump.
  • the third type of absorption heat pump is a third type of absorption heat pump according to any one of items 1, 13-20, adding a new solution heat exchanger, adding an absorption-evaporator, a new a refrigerant liquid pump or a new throttle valve, and the dilute solution pipeline of the absorber is connected to the second absorber through the first solution heat exchanger to adjust the absorber to a dilute solution pipeline through the new solution heat exchanger and A new absorption-evaporator is connected, a new absorption-evaporator and a dilute solution line are connected to the second absorber via the first solution heat exchanger, and the third generator has a concentrated solution line through the first solution pump and The first solution heat exchanger is connected to the second solution heat exchanger to be adjusted to be a third generator having a concentrated solution line through the first solution pump, the first solution heat exchanger and the new solution heat exchanger and the second solution heat exchange The device is connected, and the evaporator has a refrigerant vapor channel connected to the absorber to adjust the e
  • the evaporator is further connected with the refrigerant vapor passage and the absorber, or the second condenser is provided with a refrigerant liquid pipeline.
  • the absorption-evaporator is added and the refrigerant is added.
  • the steam passage is connected to the absorber to form a third type of absorption heat pump in which the heat recovery type 1.5 is a low temperature generation process.
  • the third type of absorption heat pump is a third type of absorption heat pump according to any one of items 1, 13-20, adding a new solution heat exchanger, adding a new solution pump, and newly adding absorption.
  • - evaporator, new refrigerant liquid pump or new throttle valve connect the concentrated solution provider with concentrated solution line and absorber to adjust the concentrated solution to the thick solution line through the new solution heat exchanger and New absorption-evaporator connection, new absorption-evaporator and dilute solution line are connected to the absorber through the new solution pump and the new solution heat exchanger, and the evaporator has a refrigerant vapor channel connected to the absorber.
  • refrigerant vapor channel for the evaporator to communicate with the new absorption-evaporator, and the evaporator or the first condenser is provided with a refrigerant liquid pipeline.
  • the new refrigerant liquid pump is connected with the new absorption-evaporator to add absorption.
  • the evaporator is further connected with the refrigerant vapor passage and the absorber, or the second condenser is connected with the refrigerant liquid pipeline.
  • the new throttle valve is connected with the new absorption-evaporator, the absorption-evaporator is added and the refrigerant vapor is added. 5 ⁇
  • the channel is connected to the absorber, the formation is in the form of a regenerative type 1.
  • a third process occurs absorption heat pump.
  • the third type of absorption heat pump is the third type of absorption heat pump according to any one of items 1, 13-20, adding a new solution heat exchanger, adding a new solution pump, and newly adding absorption.
  • an evaporator, a new refrigerant liquid pump or a new throttle valve and the third generator has a concentrated solution line connected to the first solution pump and the first solution heat exchanger and the second solution heat exchanger to adjust to The three generators have a concentrated solution line connected to the new absorption-evaporator via the first solution pump, the first solution heat exchanger and the new solution heat exchanger, and a new absorption-evaporator and a dilute solution line are newly added.
  • the solution pump and the new solution heat exchanger are connected to the second solution heat exchanger, and the evaporator has a refrigerant vapor channel connected to the absorber to adjust the evaporator to have a refrigerant vapor channel and communicate with the newly added absorption-evaporator, and evaporate Adding a coolant liquid line to the first condenser or the new absorption liquid evaporator through the newly added refrigerant liquid pump, adding an absorption-evaporator and then having a refrigerant vapor passage communicating with the absorber, or the second condenser Additional coolant line is connected to the new absorption-evaporator via a new throttle valve After the addition of the absorption-evaporator and then the refrigerant vapor channel is connected to the absorber, forming a third type of absorption heat pump with a regenerative type 1.5 low temperature generation process.
  • the third type of absorption heat pump in the third type of absorption heat pump described in any of items 2-3, 21-28 and without the second evaporator, cancels the third solution pump 21, the absorber 3
  • the dilute solution pipeline is connected to the absorption-generator 16 via the third solution heat exchanger 15; the new refrigerant liquid pump or the new throttle valve is added to cancel the refrigerant vapor passage connecting the first evaporator and the absorber
  • the first condenser or the evaporator is provided with a refrigerant liquid pipeline connected to the absorption-generator through the newly added refrigerant liquid pump, the absorption-generator and the refrigerant vapor passage are connected to the absorber, or the second condenser is cooled.
  • the liquid-liquid pipeline is connected to the newly-added absorption-evaporator, and then the absorption-evaporator is connected to the refrigerant vapor channel and the absorber is connected to form a regenerative type 1.5.
  • the third type of absorption heat pump is a third type of absorption heat pump according to any one of items 2-3, 21-28, adding a new absorption-evaporator and a new refrigerant liquid pump. Or a new throttle valve, the absorption-generator has a dilute solution line connected to the first generator through the first solution heat exchanger to adjust to absorption - the generator has a dilute solution line directly connected to the new absorption-evaporator a new absorption-evaporator and a dilute solution line are connected to the first generator via the first solution heat exchanger, and the first evaporator has a refrigerant vapor passage connected to the absorber to adjust the first evaporator to have a refrigerant
  • the steam passage is connected to the newly added absorption-evaporator, and the first condenser or the first evaporator adds a refrigerant liquid pipeline through the newly added refrigerant liquid pump and the absorption-generator, and the absorption-generator and the refrigerant
  • the regenerative type 1. 5 is the third type of absorption heat pump for the low temperature generation process.
  • the third type of absorption heat pump is a third type of absorption heat pump according to any one of items 2-3, 21-28, adding a new solution heat exchanger, a new solution pump, a new one. Adding absorption-evaporator, adding refrigerant liquid pump or adding new throttle valve, connecting concentrated solution provider with concentrated solution line and absorber to adjust to concentrated solution provider with concentrated solution line through new solution heat exchange
  • the device is connected with the new absorption-evaporator, and the new absorption-evaporator and the dilute solution pipeline are connected to the absorber through the new solution pump and the new solution heat exchanger, and the first evaporator has a refrigerant vapor channel and
  • the absorber is adjusted to be connected to the first evaporator with a refrigerant vapor passage communicating with the newly added absorption-evaporator, and the first evaporator or the first condenser is provided with a refrigerant liquid pipeline via a newly added refrigerant liquid pump and newly absorbed - After the evaporator is
  • Class 5 is the third type of absorption heat pump for the low temperature generation process.
  • the third type of absorption heat pump is a third type of absorption heat pump according to any one of items 2-3, 21-28, adding a new solution heat exchanger, adding a new solution pump, new The absorption-evaporator, the newly added refrigerant liquid pump or the newly added throttle valve adjusts the concentrated solution line in the steam distribution chamber through the second solution pump and the third solution heat exchanger to the second solution heat exchanger to The steam distribution chamber has a concentrated solution pipeline connected to the new absorption-evaporator via the second solution pump, the third solution heat exchanger and the new solution heat exchanger, and the new absorption-evaporator and the dilute solution pipeline are newly added.
  • the increasing solution pump and the new solution heat exchanger are in communication with the second solution heat exchanger, and the first evaporator has a refrigerant vapor channel connected to the absorber to adjust the first evaporator to have a refrigerant vapor channel and a new absorption-evaporation Connected to the evaporator or the first condenser to add a refrigerant liquid pipeline.
  • the new refrigerant liquid pump is connected with the new absorption-evaporator, a new absorption-evaporator is connected, and then the refrigerant vapor passage is connected to the absorber, or
  • the second condenser adds a refrigerant liquid pipeline through a new throttle and a new absorption-steaming
  • the refrigerant vapor passage in communication with the absorbent to form a regenerative heat process occurring level 1.5 third category is the low temperature absorption heat pump.
  • the third type of absorption heat pump is a third type of absorption heat pump according to any one of items 4, 29-36, adding a new solution heat exchanger, adding an absorption-evaporator, a new The refrigerant liquid pump or the newly added throttle valve, the diluted solution pipeline of the absorber is connected to the steam distribution chamber through the third solution heat exchanger and the absorption-generator and the steam distribution chamber to adjust the absorber to have a dilute solution pipeline through the new solution
  • the heat exchanger is connected to the newly added absorption-evaporator, and the new absorption-evaporator and the dilute solution pipeline are connected to the steam distribution chamber through the third solution heat exchanger and the absorption-generator, and the second solution pump has a concentrated solution.
  • the pipeline passes through the third solution heat exchanger and the second solution heat
  • the exchanger is connected to the second solution pump
  • the concentrated solution pipeline is connected to the second solution heat exchanger via the third solution heat exchanger and the new solution heat exchanger
  • the second evaporator has a refrigerant vapor passage and an absorber.
  • connection adjustment is such that the second evaporator has a refrigerant vapor passage communicating with the newly added absorption-evaporator, and the third condenser or the second evaporator is provided with a refrigerant liquid pipeline via the newly added refrigerant liquid pump and the newly added absorption-evaporator
  • the absorption-evaporator is added, and then the refrigerant vapor channel is connected with the absorber, or the second condenser is added with the refrigerant liquid pipeline.
  • the new throttle valve is connected with the new absorption-evaporator, the absorption-evaporation is newly added.
  • the refrigerant flow channel is connected to the absorber, and the third type of absorption heat pump is a regenerative type 1.5 low temperature generating process.
  • the third type of absorption heat pump is a third type of absorption heat pump according to any one of items 4, 29-36, adding a new solution heat exchanger, adding a new solution pump, and newly adding absorption.
  • - evaporator, new refrigerant liquid pump or new throttle valve connect the concentrated solution provider with concentrated solution line and absorber to adjust the concentrated solution to the thick solution line through the new solution heat exchanger and A new absorption-evaporator connection is added, a new absorption-evaporator and a dilute solution line are connected to the absorber via a new solution pump and a new solution heat exchanger, and the second evaporator has a refrigerant vapor channel and an absorber.
  • connection adjustment is such that the second evaporator has a refrigerant vapor passage communicating with the newly added absorption-evaporator, and the third condenser or the second evaporator is provided with a refrigerant liquid pipeline via the newly added refrigerant liquid pump and the newly added absorption-evaporator
  • the absorption-evaporator is added, and then the refrigerant vapor channel is connected with the absorber, or the second condenser is added with the refrigerant liquid pipeline.
  • the new throttle valve is connected with the new absorption-evaporator, the absorption-evaporation is newly added.
  • the refrigerant vapor passage is connected to the absorber to form a back 1.5
  • the third type absorption heat pump using a low temperature process occurs.
  • the third type of absorption heat pump is a third type of absorption heat pump according to any one of items 4, 29-36, adding a new solution heat exchanger, adding a new solution pump, and newly adding absorption.
  • a new solution heat exchanger adding a new solution pump, and newly adding absorption.
  • an evaporator, a new refrigerant liquid pump or a new throttle valve, and the concentrated solution line in the steam distribution chamber is connected to the second solution heat exchanger and the second solution heat exchanger via the second solution pump and the second solution heat exchanger to adjust the steam separation
  • the concentrated solution line in the chamber is connected to the newly added absorption-evaporator via the second solution pump, the third solution heat exchanger and the new solution heat exchanger, and the new absorption-evaporator and the dilute solution line are added through the new solution.
  • the pump and the new solution heat exchanger are in communication with the second solution heat exchanger, and the second evaporator has a refrigerant vapor passage connected to the absorber to be adjusted to a second evaporator having a refrigerant vapor passage connected to the newly added absorption-evaporator , the third condenser or the second evaporator is added with a refrigerant liquid pipeline, and the new refrigerant liquid pump is connected with the new absorption-evaporator, and then the absorption-vaporizer is connected, and then the refrigerant vapor channel is connected with the absorber, or
  • the second condenser adds a refrigerant liquid pipeline through the addition of a new throttle valve and new absorption - After the evaporator is connected, a new absorption-evaporator is connected, and then a refrigerant vapor channel is connected with the absorber to form a third type of absorption heat pump with a regenerative type 1.5 as a low temperature generation process.
  • the third type of absorption heat pump is a third type of absorption heat pump according to any one of items 4, 29-36, adding a new solution heat exchanger, adding an absorption-evaporator and a new one.
  • a refrigerant pump the absorption-generator has a dilute solution line connected to the first generator through the first solution heat exchanger to adjust to absorption-the generator has a dilute solution line through the first solution heat exchanger and newly added
  • the absorption-evaporator is connected, the new absorption-evaporator and the dilute solution pipeline are connected to the first generator via the new solution heat exchanger, and the first generator has a concentrated solution pipeline through the first solution pump and the first
  • the solution heat exchanger is connected to the absorption-generator to adjust the first generator to have a concentrated solution line through the first solution pump, the new solution heat exchanger and the first solution heat exchanger to communicate with the absorption-generator, which will be first
  • the evaporator has a refrigerant vapor passage and an absorption
  • the third type of absorption heat pump is a third type of absorption heat pump according to any one of items 4, 29-36, adding a new solution heat exchanger, adding a new solution pump, and newly adding absorption.
  • the first generator has a concentrated solution line connected to the first solution pump and the first solution heat exchanger and the absorption-generator to adjust the first generator to have a concentrated solution line
  • the first solution pump and the first solution heat exchanger are connected to the newly added absorption-evaporator, and the new absorption-evaporator and the dilute solution pipeline are added to the new solution pump and the new solution heat exchanger and the absorption-generator.
  • the absorption-generator has a dilute solution line
  • the first solution heat exchanger is connected to the first generator to be adjusted to be an absorption-generator having a dilute solution line connected to the first generator via the new solution heat exchanger and the first solution heat exchanger, and the first evaporator is
  • the refrigerant vapor passage and the absorption-generator are connected to each other to adjust the first evaporator to have a refrigerant vapor passage communicating with the new absorption-evaporator, and the first condenser or the first evaporator to add a refrigerant liquid pipeline is newly absorbed.
  • a new absorption-evaporator and a refrigerant vapor channel are connected to the absorption-generator to form a third type of absorption heat pump in which the regenerative type 1.5 is a low temperature generation process.
  • Figure 1 is a single-effect single-effect third-class absorption heat pump structure and flow chart
  • FIG. 2 is a first configuration and flow diagram of a single-effect-recovery single-effect third-class absorption heat pump according to the present invention.
  • Figure 3 is a second construction and flow diagram of a single-effect-recovery single-effect third-class absorption heat pump according to the present invention.
  • Figure 4 is a third construction and flow diagram of a single-effect-recovery single-effect third-class absorption heat pump according to the present invention.
  • Figure 5 is a fourth configuration and flow diagram of a single-effect-recovery single-effect third-class absorption heat pump according to the present invention.
  • Figure 6 is a fifth configuration and flow diagram of a single-effect-recovery single-effect third-class absorption heat pump according to the present invention.
  • Figure 7 is a first construction and flow diagram of a double-effect-single-effect third-type absorption heat pump according to the present invention.
  • Figure 8 is a second construction and flow diagram of a double effect-single effect third type absorption heat pump provided in accordance with the present invention.
  • Figure 9 is a third construction and flow diagram of a double-effect-single-effect third-type absorption heat pump according to the present invention.
  • Figure 10 is a first construction and flow diagram of a three-effect-single-effect third-type absorption heat pump according to the present invention.
  • Figure 11 is a second construction and flow diagram of a three-effect-single-effect third-type absorption heat pump according to the present invention.
  • Figure 12 is a third construction and flow diagram of a three-effect-single-effect third-type absorption heat pump according to the present invention.
  • Figure 13 is a first construction and flow diagram of a single-effect, double-effect, third-class absorption heat pump in accordance with the present invention.
  • Figure 14 is a second construction and flow diagram of a single-effect, double-effect, third-class absorption heat pump in accordance with the present invention.
  • Figure 15 is a third construction and flow diagram of a single-effect, double-effect, third-class absorption heat pump in accordance with the present invention.
  • Figure 16 is a first construction and flow diagram of a single-effect - three-effect third type absorption heat pump according to the present invention.
  • Figure 17 is a second construction and flow diagram of a single-effect three-effect third type absorption heat pump according to the present invention.
  • Figure 18 is a third construction and flow diagram of a single-effect three-effect third type absorption heat pump according to the present invention.
  • Figure 19 is a first configuration and flow diagram of a single-effect-recovery double-effect third-class absorption heat pump according to the present invention.
  • Figure 20 is a second construction and flow diagram of a single-effect-recovery double-effect third-class absorption heat pump according to the present invention.
  • Figure 21 is a third configuration and flow diagram of a single-effect-recovery double-effect third-class absorption heat pump according to the present invention.
  • Figure 22 is a fourth configuration and flow diagram of a single-effect-recovery double-effect third-class absorption heat pump according to the present invention.
  • Figure 23 is a fifth configuration and flow diagram of a single-effect-recovery double-effect third-class absorption heat pump according to the present invention.
  • Figure 24 is a sixth configuration and flow diagram of a single-effect-recovery double-effect third-class absorption heat pump according to the present invention.
  • Figure 25 is a seventh configuration and flow diagram of a single-effect-recovery double-effect third-class absorption heat pump according to the present invention.
  • Figure 26 is a diagram showing the eighth structure and flow chart of a single-effect-recovery double-effect third-class absorption heat pump according to the present invention.
  • Figure 27 is a ninth configuration and flow diagram of a single-effect-recovery double-effect third-class absorption heat pump according to the present invention.
  • Figure 38 is a tenth configuration and flow diagram of a single-effect-recovery double-effect third-class absorption heat pump according to the present invention.
  • Figure 29 is a first configuration and flow diagram of a single-effect-recovery three-effect third-class absorption heat pump according to the present invention.
  • Figure 30 is a second construction and flow diagram of a single-effect-recovery three-effect third-class absorption heat pump according to the present invention.
  • Figure 31 is a third configuration and flow diagram of a single-effect-recovery three-effect third-class absorption heat pump according to the present invention.
  • Figure 32 is a fourth configuration and flow diagram of a single-effect-recovery three-effect third-class absorption heat pump according to the present invention.
  • Figure 33 is a fifth configuration and flow diagram of a single-effect-recovery three-effect third-class absorption heat pump according to the present invention.
  • Figure 34 is a sixth configuration and flow diagram of a single-effect-recovery three-effect third-class absorption heat pump according to the present invention.
  • Figure 35 is a seventh configuration and flow diagram of a single-effect-recovery three-effect third-class absorption heat pump according to the present invention.
  • Figure 36 is a diagram showing the eighth structure and flow chart of a single-effect-recovery three-effect third-class absorption heat pump according to the present invention.
  • Figure 37 is a ninth configuration and flow diagram of a single-effect-recovery three-effect third-class absorption heat pump according to the present invention.
  • Figure 38 is a tenth configuration and flow diagram of a single-effect-recovery three-effect third-class absorption heat pump according to the present invention.
  • Figure 39 is a diagram showing the eleventh structure and flow chart of a single-effect-recovery three-effect third-class absorption heat pump according to the present invention.
  • Figure 40 is a twelfth structure and flow chart of a single-effect-recovery three-effect third-class absorption heat pump according to the present invention.
  • Figure 41 is a first configuration and flow diagram of a single-acting-1. 5 third-class absorption heat pump according to the present invention.
  • Figure 42 is a second construction and flow diagram of a single-effect -1.5 class third type absorption heat pump provided in accordance with the present invention.
  • Figure 43 is a third construction and flow diagram of a single-effect -1.5 primary absorption heat pump according to the present invention.
  • Figure 44 is a first configuration and flow diagram of a single-effect-recovery type 1.5 third-class absorption heat pump according to the present invention.
  • Figure 45 is a second construction and flow diagram of a single-effect-recovery type 1.5 third-class absorption heat pump provided in accordance with the present invention.
  • Figure 46 is a third construction and flow diagram of a single-effect-recovery type 1.5 third-class absorption heat pump provided in accordance with the present invention.
  • Figure 47 is a fourth construction and flow diagram of a single-effect-recovery type 1.5 third-class absorption heat pump according to the present invention.
  • Figure 48 is a fifth configuration and flow diagram of a single-effect-recovery type 1.5 third-class absorption heat pump provided in accordance with the present invention.
  • Figure 49 is a sixth configuration and flow diagram of a single-effect-recovery type 1.5 third-class absorption heat pump according to the present invention.
  • Figure 50 is a seventh configuration and flow diagram of a single-effect-recovery type 1.5 third-class absorption heat pump according to the present invention.
  • Figure 51 is a diagram showing the eighth construction and flow chart of a single-effect-recovery type 1.5 third-class absorption heat pump according to the present invention.
  • Figure 52 is a diagram showing the ninth structure and flow chart of a single-effect-recovery type 1.5 third-class absorption heat pump according to the present invention.
  • Figure 53 is a diagram showing the tenth structure and flow chart of a single-effect-recovery type 1.5 third-class absorption heat pump according to the present invention.
  • Figure 54 is a diagram showing the eleventh structure and flow chart of a single-effect-recovery type 1.5 third-class absorption heat pump according to the present invention.
  • Figure 55 is a diagram showing the structure and flow chart of a single-effect-recovery type 1.5 third-class absorption heat pump according to the present invention.
  • a concentrated solution provider - means passing through the second solution heat exchanger 11, or passing through the second solution heat exchanger 11 and the third solution heat exchanger 15, respectively, and respectively passing through the second solution heat exchanger 11,
  • the three-solution heat exchanger 15 and the fourth solution heat exchanger 24 provide a component of the concentrated solution to the absorber 3; wherein, when the concentrated solution is two or three in parallel, it can be regarded as a branching into or into a single absorber into the absorber. 3.
  • the first solution pump 7 in FIG. 3 is used to adjust the pressure at which the solution flows through the absorption-generator 16 during the endothermic vaporization, and at this time, the refrigerant vapor pressure of the steam separation chamber 17 (ie, The refrigerant vapor pressure in the triple condenser 18 is higher than the refrigerant vapor pressure of the first condenser 4; when the refrigerant vapor pressure of the third condenser 18 is selected to be lower than the refrigerant vapor pressure of the first condenser 4, The first refrigerant liquid pump 7 is not provided.
  • the main function of the third solution pump 21 in Fig. 4 is to overcome the resistance of the solution flowing through the third solution heat exchanger 15 and the resistance of the line.
  • the generator is a rectification tower, and the first refinery tower 1 and the cooling medium pipeline are connected to the outside, and the second refinery tower 2 There is also a heated medium line that communicates with the outside.
  • the single-effect, single-effect, third-class absorption heat pump shown in Figure 1 is implemented as follows:
  • the first generator 1 structurally, it mainly consists of a first generator, a second generator, an absorber, a first condenser, a second condenser, an evaporator, a solution pump, a refrigerant liquid pump, a throttle valve, a first solution heat exchange And the second solution heat exchanger;
  • the first generator 1 has a concentrated solution line connected to the second generator 2 via the solution pump 7, the first solution heat exchanger 10 and the second solution heat exchanger 11
  • the second generator 2 and the concentrated solution line are connected to the absorber 3 via the second solution heat exchanger 11, and the absorber 3 and the dilute solution line are connected to the first generator 1 via the first solution heat exchanger 10,
  • a generator 1 and a refrigerant vapor passage are in communication with the first condenser 4, and the first condenser 4 and the refrigerant liquid line are connected to the evaporator 6 via the refrigerant liquid pump 8, and the second generator 2 is also cooled.
  • the refrigerant vapor passage is in communication with the second condenser 5, and the second condenser 5 and the refrigerant liquid pipeline are connected to the evaporator 6 via the throttle valve 9, and the evaporator 6 and the refrigerant vapor passage are connected to the absorber 3,
  • a generator 1 and an evaporator 6 respectively have a residual heat medium pipe connected to the outside
  • the second generator 2 also has a driving heat medium pipe connected to the outside, and the absorber 3 and the second condenser 5 are respectively connected to the outside by the heated medium pipe, and the first condenser 4 has a cooling medium pipe and the outside. Connected.
  • the dilute solution of the absorber 3 enters the first generator 1 through the first solution heat exchanger 10, and the residual heat medium flows through the first generator 1, and the solution heated therein is released and supplied to the first condenser 4.
  • the refrigerant vapor, the refrigerant vapor of the first condenser 4 is radiated to the cooling medium to form a refrigerant liquid, and the refrigerant liquid of the first condenser 4 is pressurized by the refrigerant liquid pump 8 into the evaporator 6; the first generator 1
  • the concentrated solution enters the second generator 2 via the solution pump 7, the first solution heat exchanger 10 and the second solution heat exchanger 11, drives the heat medium to flow through the second generator 2, and the solution heated into the solution is released and directed
  • the second condenser 5 supplies refrigerant vapor, and the refrigerant liquid of the second condenser 5 is throttled and depressurized by the throttle valve 9 to enter the evaporator 6; the waste heat medium flows through the evaporator 6,
  • the refrigerant vapor is supplied to the absorber 3, and the concentrated solution of the second generator 2 enters the absorber 3 through the second solution heat exchanger 11, absorbs the refrigerant vapor from the evaporator 6, and radiates heat to the heated medium, absorbing
  • the dilute solution of the device 3 enters the first solution through the first solution heat exchanger 10 a generator 1; the refrigerant vapor of the second condenser 5 is exothermic to the heated medium to form a refrigerant liquid; and a single-effect single-effect third type absorption heat pump is formed.
  • the regenerative third type absorption heat pump shown in Figure 2 is implemented as follows:
  • the third generator, the second absorber, the second solution pump and the third solution heat exchanger are added, and the absorber 3 has a dilute solution line.
  • the first solution heat exchanger 10 is connected to the first generator 1 to be adjusted so that the absorber 3 has a dilute solution line communicating with the second absorber 13 via the first solution heat exchanger 10, and the second absorber 13 has a dilute solution.
  • the pipeline is connected to the first generator 1 via the second solution pump 14 and the third solution heat exchanger 15, and the first generator 1 has a concentrated solution pipeline through the first solution pump 7, the first solution heat exchanger 10, and
  • the second solution heat exchanger 11 is connected to the second generator 2 to be adjusted so that the first generator 1 has a concentrated solution line connected to the third generator 12 via the third solution heat exchanger 15, and the third generator 12 is further rich.
  • the solution line is in communication with the second generator 2 via the first solution pump 7, the first solution heat exchanger 10 and the second solution heat exchanger 11, the third generator 12 further having a refrigerant vapor channel and a second absorber, respectively 13 connectivity
  • the residual heat medium pipeline communicates with the outside, and the second absorber 13 and the cooling medium pipeline communicate with the outside.
  • the dilute solution of the absorber 3 enters the second absorber 13 through the first solution heat exchanger 10, absorbs the refrigerant vapor from the third generator 12, and radiates heat to the cooling medium, and the second absorber 13 is diluted.
  • the solution enters the first generator 1 via the second solution pump 14 and the third solution heat exchanger 15; the concentrated solution of the first generator 1 enters the third generator 12 via the third solution heat exchanger 15, and the residual heat medium flows through the first a three generator 12, a solution heated therein to release and supply refrigerant vapor to the second absorber 13; a concentrated solution of the third generator 12 passes through the first solution pump 7, the first solution heat exchanger 10, and the second solution
  • the heat exchanger 11 enters the second generator 2 to form a recuperative third type absorption heat pump.
  • the regenerative third type absorption heat pump shown in Figure 3 is implemented as follows:
  • the absorber 3 has a dilute solution line connected to the first generator 1 through the first solution heat exchanger 10 to adjust the absorber 3 has a dilute solution line through the third solution heat exchanger 15 and
  • the absorption-generator 16 is connected, the absorption-generator 16 and the dilute solution line are connected to the first generator 1 via the first solution heat exchanger 10, and the first generator 1 has a concentrated solution line through the first solution pump.
  • the first solution heat exchanger 10 and the second solution heat exchanger 11 are connected to the second generator 2 to be adjusted so that the first generator 1 has a concentrated solution line through the first solution pump 7 and the first solution heat exchanger 10.
  • the absorption-generator 16 is in communication with the steam dividing chamber 17, and the steam dividing chamber 17 has a concentrated solution line passing through the second solution pump 14, the third solution heat exchanger 15 and the second solution heat exchanger 11 and the second generator 2 connected, the steam dividing chamber 17 and the refrigerant vapor passage are connected to the third condenser 18,
  • the third condenser 18 also has a refrigerant liquid line connected to the second evaporator 19 via the second refrigerant liquid pump 20, and the second evaporator 19 also has a refrigerant vapor passage communicating with the absorption-generator 16 for the third condensation.
  • the device 18 also has a cooling medium line communicating with the outside, and the second evaporator 19 and the residual heat medium line are in communication with the outside.
  • the dilute solution of the absorber 3 enters the absorption-generator 16 via the third solution heat exchanger 15, absorbs the refrigerant vapor from the second evaporator 19, and releases the solution flowing through the absorption-generator 16
  • the dilute solution of the absorption-generator 16 enters the first generator 1 via the first solution heat exchanger 10; the concentrated solution of the first generator 1 passes through the first solution pump 7 and the first solution heat exchanger 10 and then flows through
  • the absorption-generator 16 and the endothermic portion are vaporized into the steam dividing chamber 17, and the refrigerant vapor released from the steam dividing chamber 17 enters the third condenser 18, radiates heat to the cooling medium to form a refrigerant liquid, and the refrigerant of the third condenser 18
  • the liquid is pressurized into the second evaporator 19 via the second refrigerant liquid pump 20, absorbs the residual heat into the refrigerant vapor and is supplied to the absorption generator 16, and the concentrated solution of the steam
  • the pump and the third solution pump adjust the absorber 3 having a dilute solution line through the first solution heat exchanger 10 to the first generator 1 to adjust the absorber 3 to have a dilute solution line through the third solution pump 21 and the third
  • the solution heat exchanger 15 is in communication with the absorption-generator 16 and the absorption-generator 16 and the dilute solution line are in communication with the first generator 1 via the first solution heat exchanger 10, and the first generator 1 has a concentrated solution tube.
  • a solution heat exchanger 10 and an absorption-generator 16 are in communication with the steam dividing chamber 17, and the steam dividing chamber 17 has a concentrated solution line passing through the second solution pump 14, the third solution heat exchanger 15, and the second solution heat exchanger.
  • the absorption-generator 16 has a heated medium tube Communicating with the outside
  • the steam dividing chamber 17 also has a refrigerant vapor passage communicating with the third condenser 18, and the third condenser 18 and the refrigerant liquid pipeline are connected to the evaporator 6 via the second refrigerant liquid pump 20, the evaporator 6
  • the refrigerant vapor passage is connected to the absorption-generator 16 , and the third condenser 18 and the cooling medium conduit are in communication with the outside.
  • the dilute solution of the absorber 3 enters the absorption-generator via the third solution pump 21 and the third solution heat exchanger 15. 16.
  • the generator 1 ; the concentrated solution of the first generator 1 passes through the first solution pump 7 and the first solution heat exchanger 10 and then flows through the absorption-generator 16 , and the heat absorption portion is vaporized into the steam separation chamber 17 , and the steam separation chamber 17
  • the released refrigerant vapor enters the third condenser 18, radiates heat to the cooling medium to form a refrigerant liquid, and the refrigerant liquid of the third condenser 18 is pressurized into the evaporator 6 through the second refrigerant liquid pump 20, and the evaporator 6 generates The refrigerant vapor is
  • the regenerative third type absorption heat pump shown in Figure 5 is implemented as follows:
  • the heated medium line in which the absorption-generator 16 communicates with the outside is canceled, the second refrigerant liquid pump 20 is cancelled, the second throttle valve 22 is added, and the third
  • the condenser 18 has a refrigerant liquid line connected to the evaporator 6 via the second refrigerant liquid pump 20 to be adjusted to a third condenser 18, and a refrigerant liquid line is connected to the first condenser 4 via the second throttle valve 22.
  • the second throttle pump 22 is replaced by the second throttle valve 22 in order to reduce the amount of the refrigerant liquid pump; the price paid is a small increase in the energy consumption of the refrigerant liquid pump 8.
  • a generator 1 structurally, in the third type of absorption heat pump shown in FIG. 1, adding a second solution pump, a third solution heat exchanger, an absorption-generator, a steam separation chamber, a third condenser, a second evaporator, and
  • the second refrigerant liquid pump adjusts the first generator 1 concentrated solution line to the first solution pump 7, the first solution heat exchanger 10, and the second solution heat exchanger 11 and the second generator 2
  • a generator 1 has a concentrated solution line connected to the absorption-generator 16 via the first solution pump 7 and the first solution heat exchanger 10, and the absorption-generator 16 and the dilute solution line are passed through the first solution heat exchanger 10.
  • the dilute solution line of the absorber 3 is communicated with the first generator 1 via the first solution heat exchanger 10 to adjust the absorber 3 to have a dilute solution line through the third solution heat exchanger 15
  • the absorption-generator 16 is in communication with the steam dividing chamber 17, and the steam dividing chamber 17 has a concentrated solution line passing through the second solution pump 14, the third solution heat exchanger 15 and the second solution heat exchanger 11 and the second generator 2 connected
  • the first condenser 4 has a refrigerant liquid pipeline through the first refrigerant liquid pump 8 and
  • An evaporator 6 is connected to adjust the first condenser 4 to have a refrigerant liquid pipeline connected to the second evaporator 19 via the first refrigerant liquid pump 8, and the second evaporator 19 has a refrigerant vapor passage and an absorption-generator 16 communicating
  • the steam dividing chamber 17 and the refrigerant vapor passage are in communication with the third condenser 18, and the third condenser 18 and the ref
  • the diluted solution of the absorber 3 is cooled and depressurized by the third solution heat exchanger 15, and then flows through the absorption-generator 16, and the endothermic portion is vaporized and then enters the steam dividing chamber 17, and the refrigerant released from the steam dividing chamber 17
  • the steam enters the third condenser 18, exotherms in the cooling medium to form a refrigerant liquid, and the refrigerant liquid of the third condenser 18 is pressurized into the evaporator 6 through the second refrigerant liquid pump 20, and the concentrated solution of the steam separation chamber 17 passes through
  • the second solution pump 14, the third solution heat exchanger 15 and the second solution heat exchanger 11 enter the second generator 2; the refrigerant vapor generated by the first generator 1 enters the first condenser 4, the first condenser 4
  • the refrigerant liquid enters the second evaporator 19 via the first refrigerant liquid pump 8, absorbs the residual heat into the refrigerant vapor and supplies it to the absorption
  • the double-effect-single-effect third-type absorption heat pump shown in Figure 7 is implemented as follows:
  • the third generator, the third solution heat exchanger and the second throttle valve are added, and the first generator 1 passes through the first solution pump 7 and the first
  • the third generator 12 also has a concentrated solution line through the third solution heat
  • the exchanger 15 is in communication with the absorber 3
  • the second generator 2 has a refrigerant vapor passage communicating with the second condenser 5 to be adjusted to a second generator 2 having a refrigerant vapor passage communicating with the third generator 12 to occur third.
  • the refrigerant 12 is further connected to the second condenser 5 via the second throttle m 22, and the third generator 12 and the refrigerant vapor passage are in communication with the second condenser 5.
  • the refrigerant vapor generated by the second generator 2 is supplied to the third generator 12 to drive the heat medium, and the concentrated solution of the first generator 1 passes through the solution pump 7 and the first solution heat exchanger 10, respectively.
  • the second solution heat exchanger 11 enters the second generator 2 and then enters the third generator 12 via the third solution heat exchanger 15; the refrigerant vapor flows through the third generator 12, and the solution heated therein is released and directed
  • the second condenser 5 supplies refrigerant vapor, and the concentrated solution of the third generator 12 enters the absorber 3 through the third solution heat exchanger 15, and the refrigerant vapor flowing through the third generator 12 is released into a refrigerant liquid, and then
  • the second throttle valve 22 is throttled into the second condenser 5 to form a double-effect-single-effect third-type absorption heat pump.
  • the double-effect-single-effect third-type absorption heat pump shown in Figure 8 is implemented as follows:
  • the third generator, the third solution heat exchanger and the second throttle valve are added, and the first generator 1 has a concentrated solution pipeline.
  • a solution pump 7, a first solution heat exchanger 10 and a second solution heat exchanger 11 are connected to the second generator 2 to be adjusted so that the first generator 1 has a concentrated solution line through the first solution pump 7, the first solution heat The exchanger 10, the second solution heat exchanger 11 and the third solution heat exchanger 15 are in communication with the second generator 2, and the second generator 2 has a concentrated solution line through the second solution heat exchanger 11 and the absorber 3.
  • the communication is adjusted to be that the second generator 2 has a concentrated solution line that communicates with the third generator 12 via the third solution heat exchanger 15, and the third generator 12 also has a concentrated solution line that passes through the second solution heat exchanger 11 and absorbs
  • the third generator 12 is connected to the second generator 2 and has a refrigerant vapor passage communicating with the second condenser 5 to adjust the second generator 2 to have a refrigerant vapor passage communicating with the third generator 12.
  • the agent liquid pipeline communicates with the second condenser 5 via the second throttle valve 22, and the third There refrigerant vapor passage communicating with the second condenser 5 generator 12.
  • the concentrated solution of the first generator 1 enters the second generator 2 via the solution pump 7, the first solution heat exchanger 10, the second solution heat exchanger 11 and the third solution heat exchanger 15, the second occurrence
  • the refrigerant vapor generated by the device 2 is supplied to the third generator 12 to drive the heat medium, and the concentrated solution of the second generator 2 enters the absorber 3 through the third solution heat exchanger 15; the refrigerant vapor flows through the third generator 12
  • the solution heated into the solution is released and the refrigerant vapor is supplied to the second condenser 5, and the concentrated solution of the third generator 12 enters the absorber 3 through the second solution heat exchanger 11, and flows through the cold of the third generator 12.
  • the agent vapor is exothermic into a refrigerant liquid, and then throttled into the second condenser 5 through the second throttle valve 22 to form a double-effect-single-effect third type absorption heat pump.
  • the third generator, the third solution heat exchanger, the second solution pump and the second throttle valve are added, and the first generator 1 is thick
  • the solution line is connected to the second generator 2 via the first solution pump 7, the first solution heat exchanger 10, and the second solution heat exchanger 11 to be adjusted to be the first generator 1 having the concentrated solution line passing through the first solution pump 7
  • the first solution heat exchanger 10 and the second solution heat exchanger 11 are in communication with the third generator 12, and the third generator 12 has a concentrated solution line through the second solution pump 14 and the third solution heat exchanger 15 and
  • the second generator 2 is connected, and the second generator 2 has a concentrated solution pipeline connected to the absorber 3 via the second solution heat exchanger 11 to be adjusted to a second generator 2 having a concentrated solution pipeline through the third solution heat exchanger 15 and the second solution heat exchanger 11 is in communication with the absorber 3, and the second generator 2 has a refrigerant vapor passage communicating with the second condenser 5 to adjust the second generator 2 to have a ref
  • the concentrated solution of the first generator 1 enters the third generator 12 via the first solution pump 7, the first solution heat exchanger 10 and the second solution heat exchanger 11, and the refrigerant generated by the second generator 2
  • the steam is supplied to the third generator 12 as a driving heat medium
  • the refrigerant vapor flows through the third generator 12, the solution heated therein is released, and the refrigerant vapor is supplied to the second condenser 5, and the third generator 12 is concentrated.
  • the solution enters the second generator 2 through the second solution pump 14 and the third solution heat exchanger 15
  • the refrigerant vapor passing through the third generator 12 is exothermic into a refrigerant liquid, and then throttled into the second condenser 5 via the second throttle valve 22, and the concentrated solution of the second generator 1 passes through the third solution heat exchanger 15
  • the second solution heat exchanger 11 enters the absorber 3 to form a double-effect-single-effect third-type absorption heat pump.
  • the three-effect-single-effect third-class absorption heat pump shown in Figure 10 is implemented as follows:
  • the fourth generator, the fourth solution heat exchanger and the third throttle valve are added, and the first solution heat exchanger 10 is provided with a concentrated solution pipeline.
  • the fourth solution heat exchanger 24 is in communication with the fourth generator 23, and the fourth generator 23 and the concentrated solution line are in communication with the absorber 3 via the fourth solution heat exchanger 24, and the third generator 12 has refrigerant vapor.
  • the passage is connected to the second condenser 5 to be adjusted so that the third generator 12 has a refrigerant vapor passage communicating with the fourth generator 23, and then the fourth generator 23 has a refrigerant liquid pipeline passing through the third throttle valve 25 and the second
  • the condenser 5 is in communication, and the fourth generator 23 and the refrigerant vapor passage are in communication with the second condenser 5.
  • the refrigerant vapor generated by the third generator 12 is supplied to the fourth generator 23 as a driving heat medium, and a part of the concentrated solution of the first generator 1 passes through the solution pump 7, the first solution heat exchanger 10 and the fourth
  • the solution heat exchanger 24 enters the fourth generator 23, the refrigerant vapor flows through the fourth generator 23, the solution heated therein is released, and the refrigerant vapor is supplied to the second condenser 5, and the concentrated solution of the fourth generator 23
  • the refrigerant vapor flowing through the fourth generator 23 is released into a refrigerant liquid, and then throttled through the third throttle valve 25 into the second condenser 5 to form three Effect - single effect third type absorption heat pump.
  • the fourth generator, the fourth solution heat exchanger and the third throttle valve are added, and the second solution heat exchanger 11 has a concentrated solution pipeline.
  • the second solution heat exchanger 11 has a concentrated solution pipeline through the fourth solution heat exchanger 24 and the third solution heat exchanger 15 and the second generator.
  • the third generator 12 has a concentrated solution pipeline connected to the absorber 3 through the second solution heat exchanger 11 to be adjusted to a third generator 12 having a concentrated solution pipeline through the fourth solution heat exchanger 24 and
  • the fourth generator 23 is connected, the fourth generator 23 and the concentrated solution pipeline are connected to the absorber 3 via the second solution heat exchanger 11, and the third generator 12 has a refrigerant vapor passage connected to the second condenser 5.
  • the fourth generator 23 is further connected to the second condenser 5 via the third throttle valve 25, and the fourth generator 23 also has a refrigerant vapor passage communicating with the second condenser 5.
  • the concentrated solution of the first generator 1 enters the first through the solution pump 7, the first solution heat exchanger 10, the second solution heat exchanger 11, the fourth solution heat exchanger 24, and the third solution heat exchanger 15.
  • the second generator 2 the concentrated solution of the second generator 2 enters the third generator 12 via the third solution heat exchanger 15, and the concentrated solution of the third generator 12 enters the fourth generator 23 via the fourth solution heat exchanger 24.
  • the refrigerant vapor generated by the third generator 12 is supplied to the fourth generator 23 for driving the heat medium, and the refrigerant vapor flows through the fourth generator 23, and the solution heated therein is released and provides cold to the second condenser 5.
  • the vapor of the agent, the concentrated solution of the fourth generator 23 enters the absorber 3 via the second solution heat exchanger 11, and the refrigerant vapor flowing through the fourth generator 23 is released into a refrigerant liquid, and then passes through the third throttle valve 25 Entering the second condenser 5, a three-effect-single-effect third-type absorption heat pump is formed.
  • the fourth generator, the fourth solution heat exchanger, the third throttle valve, and the third solution pump are added, and the second solution heat exchanger 11 is added.
  • the concentrated solution line is connected to the third generator 12 to be adjusted to be the second solution heat exchanger 11 has a concentrated solution line connected to the fourth generator 23, and the fourth generator 23 has a concentrated solution line through the third solution pump
  • the 21 and fourth solution heat exchangers 24 are in communication with the third generator 12, and the second generator 2 has a concentrated solution line connected to the absorber 3 via the third solution heat exchanger 15 and the second solution heat exchanger 11 a second solution 2 having a concentrated solution line through the third solution heat exchanger 15, the fourth solution heat exchanger 24, and the second solution heat exchanger 11 and the absorber 3
  • the third generator 12 has a refrigerant vapor passage communicating with the second condenser 5 to be adjusted to a third generator 12 having a refrigerant vapor passage communicating with the fourth generator 23, and then the fourth generator 23 is
  • the concentrated solution of the first generator 1 enters the fourth generator 23 via the first solution pump 7, the first solution heat exchanger 10 and the second solution heat exchanger 11, and the refrigerant generated by the third generator 12
  • the steam is supplied to the fourth generator 23 for driving the heat medium
  • the refrigerant vapor flows through the fourth generator 23, the solution heated therein is released, and the refrigerant vapor is supplied to the second condenser 5, and the fourth generator 23 is concentrated.
  • the solution enters the third generator 12 through the third solution pump 21 and the fourth solution heat exchanger 24, and the refrigerant vapor flowing through the fourth generator 23 is released into a refrigerant liquid, and then enters the third section through the third section.
  • the second condenser 5, the concentrated solution of the second generator 2 enters the absorber 3 through the third solution heat exchanger 15, the fourth solution heat exchanger 24 and the second solution heat exchanger 11, forming a three-effect-single-effect third Absorption heat pump.
  • the single-effect, double-effect, third-class absorption heat pump shown in Figure 13 is implemented as follows:
  • a new generator, a new solution heat exchanger, a new throttle valve and a new solution pump are added, and the absorber 3 is provided with a dilute solution pipeline.
  • the new solution heat exchanger B is connected to the newly added generator A, and the new generator A and the concentrated solution pipeline are added to the first generator 1 through the new solution pump D and the new solution heat exchanger B.
  • the pump 7 and the concentrated solution pipeline after the first solution heat exchanger 10 meet, and the first generator 1 has a refrigerant vapor passage connected to the first condenser 4 to adjust the first generator 1 to have a refrigerant vapor passage and a new one.
  • the generator A After the generator A is connected, the generator A is newly added, and then the refrigerant liquid pipeline is connected to the first condenser 4 via the newly added throttle valve C, and the new generator A is also provided with the refrigerant vapor passage and the first condenser 4 Connected.
  • the dilute solution of the absorber 3 enters the newly added generator A through the newly added solution heat exchanger B, and the refrigerant vapor generated by the first generator 1 is supplied to the newly added generator A as the driving heat medium, the refrigerant vapor Flowing through the new generator A, heating the solution into it and releasing the refrigerant vapor to the first condenser 4, adding the concentrated solution of the generator A after adding the solution pump D and the new solution heat exchanger B Converging with the concentrated solution after the first generator 1 passes the solution pump 7 and the first solution heat exchanger 10, and then enters the second generator 2 via the second solution heat exchanger 11, flowing through the refrigerant of the newly added generator A
  • the steam is exothermic into a refrigerant liquid, and then throttled into the first condenser 4 by a new throttle valve C to form a single-effect-double-effect third-type absorption heat pump.
  • the single-effect, double-effect, third-class absorption heat pump shown in Figure 14 is implemented as follows:
  • the A and the concentrated solution line are connected to the second solution heat exchanger 11 via the solution pump 7, the new solution heat exchanger B and the first solution heat exchanger 10, and the first generator 1 has a refrigerant vapor channel and
  • the first condenser 4 is connected to be adjusted so that the first generator 1 has a refrigerant vapor passage connected with the newly added generator A, and then the generator A is newly added, and the refrigerant liquid pipeline is added through the newly added throttle valve C and the first condenser. 4 connected, the new generator A and the refrigerant vapor passage are in communication with the first condenser 4.
  • the concentrated solution of the first generator 1 is newly added to the generator A via the new solution heat exchanger B, and the refrigerant vapor generated by the first generator 1 is supplied to the newly added generator A for driving the heat medium, the refrigerant
  • the steam flows through the newly added generator A, the solution heated into it is released, and the refrigerant vapor is supplied to the first condenser 4, and the concentrated solution of the generator A is newly added to the solution pump 7, the new solution heat exchanger B, the first A solution heat exchanger 10 and a second solution heat exchanger 11 enter the second generator 2, and the refrigerant vapor flowing through the newly added generator A is released into a refrigerant liquid, and then enters the first through the new throttle valve C.
  • the condenser 4 forms a single-effect double-effect third type absorption heat pump.
  • the single-effect, double-effect, third-class absorption heat pump shown in Figure 15 is implemented as follows:
  • the exchanger 10 and the new solution heat exchanger B are connected to the newly added generator A, and the new generator A and the concentrated solution pipeline are added to the new solution pump D and the new solution heat exchanger B and the first generator 1 Connected, the first generator 1 has a refrigerant vapor passage connected to the first condenser 4 to be adjusted to be the first generator 1 has a refrigerant vapor passage connected with the newly added generator A, and then adds the generator A and then the refrigerant liquid
  • the pipeline is connected to the first condenser 4 via a new throttle valve C, and a new generator A and a refrigerant vapor passage are connected to the first condenser 4.
  • the dilute solution of the absorber 3 enters the newly added generator A through the first solution heat exchanger 10 and the newly added solution heat exchanger B, and the refrigerant vapor generated by the first generator 1 is supplied to the newly added generator A.
  • the refrigerant vapor flows through the newly added generator A, the solution heated into the solution is released, and the refrigerant vapor is supplied to the first condenser 4, and the concentrated solution of the generator A is newly added through the new solution pump D and
  • the new solution heat exchanger B enters the first generator 1, and the refrigerant vapor flowing through the newly added generator A is released into a refrigerant liquid, and then enters the first condenser 4 through the newly added throttle valve C to form a single effect.
  • Double-effect third-class absorption heat pump is
  • the single-effect, three-effect, third-class absorption heat pump shown in Figure 16 is implemented as follows:
  • the refrigerant vapor channel is connected with the newly added second generator E, and the second generator E is added, and then the refrigerant liquid pipeline is added by the second section.
  • the flow valve G is in communication with the first condenser 4, and the second generator E and the refrigerant vapor passage are connected to communicate with the first condenser 4.
  • the single-effect, three-effect, third-class absorption heat pump shown in Figure 17 is implemented as follows:
  • the first solution heat exchanger B and the first solution heat exchanger 10 are connected to the second solution heat exchanger 11 to adjust the newly added first generator A refrigerant vapor passage to the first condenser 4 to be newly added.
  • the first generator A has a refrigerant vapor passage connected with the newly added second generator E, and then adds a second generator E and then a refrigerant liquid pipeline is connected to the first condenser 4 via a new second throttle valve G.
  • the second generator E and the refrigerant vapor passage are connected to the first condenser 4.
  • the concentrated solution of the first generator A is newly added to the second solution E by adding the second solution heat exchanger F, and the refrigerant vapor generated by the first generator A is newly added to the new one.
  • the second generator E serves as a driving heat medium, and the refrigerant vapor flows through the newly added second generator E, the solution heated into the solution is released, and the refrigerant vapor is supplied to the first condenser 4, and the second generator E is added.
  • the solution is passed through the solution pump 7, and the second solution heat exchanger is added.
  • the single-effect, three-effect, third-class absorption heat pump shown in Figure 18 is implemented as follows:
  • a new second generator is added, a second solution heat exchanger is added, a second throttle valve is added, and a second solution pump is added.
  • the absorber 3 has a dilute solution line through the first solution heat exchanger 10 and the newly added first solution heat exchanger B and the newly added first generator A is connected to adjust the absorber 3 to have a dilute solution line through the first solution
  • the heat exchanger 10, the newly added first solution heat exchanger B and the newly added second solution heat exchanger F are connected with the newly added second generator E, and the second generator E and the concentrated solution pipeline are newly added.
  • the second solution pump H and the newly added second solution heat exchanger F are in communication with the newly added first generator A, and the newly added first generator A has a refrigerant vapor passage connected to the first condenser 4 to be newly added.
  • a generator A has a refrigerant vapor passage connected with the newly added second generator E, and then a second generator E is added, and then a refrigerant liquid pipeline is connected to the first condenser 4 via a new second throttle valve G.
  • a second generator E is added and a refrigerant vapor passage is connected to the first condenser 4.
  • the dilute solution of the absorber 3 enters the newly added second generator E through the first solution heat exchanger 10, the newly added first solution heat exchanger B, and the newly added second solution heat exchanger F, adding a new
  • the refrigerant vapor generated by a generator A is supplied to the newly added second generator E as a driving heat medium, and the refrigerant vapor flows through the newly added second generator E, and the solution heated into the same is released to the first condenser 4
  • the refrigerant vapor of E is exothermic into a refrigerant liquid, and then added to the second throttle valve G to enter the first condenser 4 to form a single-effect-three-effect third type absorption heat pump.
  • the single-effect-recovery double-effect third-class absorption heat pump shown in Figure 19 is implemented as follows:
  • the passage is connected to the first condenser 4 to be adjusted so that the first generator 1 has a refrigerant vapor passage connected with the newly added generator A, and then the new generator A is added and the refrigerant liquid pipeline is added with a new throttle C and the first The condenser 4 is connected, and the newly added generator A and the refrigerant vapor passage are in communication with the first condenser 4.
  • a part of the dilute solution of the second absorber 13 enters the newly added generator 8 through the second solution pump 14 and the newly added solution heat exchanger B, and the refrigerant vapor generated by the first generator 1 is supplied to the newly added generator.
  • A acts as a driving heat medium, and the refrigerant vapor flows through the newly added generator A, and the solution heated therein is released and supplies the refrigerant vapor to the first condenser 4, and the concentrated solution of the new generator A is heated by the added solution.
  • the device B enters the third generator 12, and the refrigerant vapor flowing through the newly added generator A is radiated into a refrigerant liquid, and then throttled into the first condenser 4 through the addition of a new throttle valve C to form a single-effect heat. Double-effect third-class absorption heat pump.
  • the single-effect-recovery double-effect third-class absorption heat pump shown in Figure 20 is implemented as follows:
  • the new generator, the new solution heat exchanger and the new throttle are added, and the second solution pump 14 has a dilute solution pipeline.
  • the three-solution heat exchanger 15 is connected to the first generator 1 to be adjusted to be a second solution pump 14 having a dilute solution line connected to the first generator 1 via the new solution heat exchanger B and the third solution heat exchanger 15
  • the first generator 1 has a concentrated solution line connected to the third generator 12 via the third solution heat exchanger 15 and is adjusted to be a first generator 1 having a concentrated solution line through the third solution heat exchanger 15 and a new generator A communication, the new generator A and the concentrated solution pipeline are connected to the third generator 12 via the new solution heat exchanger B, and the first generator 1 has a refrigerant vapor passage connected to the first condenser 4 to be adjusted to
  • the first generator 1 has a refrigerant vapor passage connected with the newly added generator A, and then adds a generator A and then a refrigerant
  • the dilute solution of the second absorber 13 enters the first generator 1 via the second solution pump 14, the new solution heat exchanger B and the third solution heat exchanger 15, and the concentrated solution of the first generator 1 is
  • the third solution heat exchanger 15 enters the newly added generator A, and the concentrated solution of the newly added generator A enters the third generator 12 via the newly added solution heat exchanger B; the refrigerant vapor generated by the first generator 1 is supplied to the new The generator A is driven to drive the heat medium, and the refrigerant vapor flows through the newly added generator A, and the solution heated therein is released and supplies the refrigerant vapor to the first condenser 4, and flows through the refrigerant vapor of the newly added generator A.
  • the exotherm is formed into a refrigerant liquid, and then added to the first condenser 4 by a new throttled C-throttle to form a single-effect-recovery double-effect third-class absorption heat pump.
  • the single-effect-recovery double-effect third-class absorption heat pump shown in Figure 21 is implemented as follows:
  • the residual heat medium line connecting the third generator 12 with the outside is canceled, and the second throttle valve is added, and the first generator 1 is provided with a refrigerant vapor passage and the first
  • the third generator 12 has a refrigerant liquid pipeline connected to the first condenser 4 via the addition of the second throttle valve G; the refrigerant vapor generated by the first generator 1 is separately supplied to the new generator
  • the generator A and the third generator 12 act as a driving heat medium, and the refrigerant vapor flowing through the third generator 12 is radiated into a refrigerant liquid, and then throttled into the first condenser 4 by adding a second throttle valve G.
  • a third type of absorption heat pump with a regenerative double effect as a low temperature generation process is formed.
  • the single-effect-recovery double-effect third-class absorption heat pump shown in Figure 22 is implemented as follows:
  • a new generator, a new solution heat exchanger, a new throttle valve and a new solution pump are added, and the second solution pump 14 is diluted.
  • the solution line is connected to the first generator 1 via the third solution heat exchanger 15 to be adjusted to be a second solution pump 14 having a dilute solution line connected to the newly added generator A via the third solution heat exchanger 15 to add a generator A also has a concentrated solution line connected to the first generator 1 via a new solution pump D and a new solution heat exchanger B, and the first generator 1 has a concentrated solution line through the third solution heat exchanger 15 and
  • the three generators 12 are connected to be adjusted so that the first generator 1 has a concentrated solution line connected to the third generator 12 via the new solution heat exchanger B and the third solution heat exchanger 15, and the first generator 1 has a refrigerant.
  • the steam passage is connected to the first condenser 4 to be adjusted so that the first generator 1 has a refrigerant vapor passage connected with the newly added generator A, and then the generator A is newly added, and the refrigerant liquid pipeline is added through the new throttle valve C and the first A condenser 4 is connected, and a new generator A and a refrigerant vapor passage are connected to the first condenser 4 through.
  • the refrigerant vapor generated by the first generator 1 is supplied to the newly added generator A as a driving heat medium, and the concentrated solution of the first generator 1 is passed through the newly added solution heat exchanger B and the third solution heat exchanger 15 Entering the third generator 12; the dilute solution of the second absorber 13 enters the new generator A through the second solution pump 14 and the third solution heat exchanger 15, and the refrigerant vapor flows through the newly added generator.
  • the solution inside releases and supplies the refrigerant vapor to the first condenser 4, and the concentrated solution of the newly added generator A enters the first generator 1 through the new solution pump D and the new solution heat exchanger B, and the flow occurs newly.
  • the refrigerant vapor of the device A is radiated into a refrigerant liquid, and then throttled into the first condenser 4 by a new throttle valve C to form a single-effect-recovery double-effect third-class absorption heat pump.
  • the single-effect-recovery double-effect third-class absorption heat pump shown in Figure 23 is implemented as follows:
  • the heated medium line connecting the absorption-generator 16 to the outside is eliminated, and the new generator, the new solution heat exchanger and the new section are added.
  • the first generator 1 has a concentrated solution pipeline connected to the first solution pump 7, the first solution heat exchanger 10, and the absorption-generator 16 and the steam distribution chamber 17 to be adjusted to have a concentrated solution of the first generator 1
  • the pipeline is connected to the steam distribution chamber 17 via the first solution heat exchanger 10 and the absorption-generator 16 , and the absorption-generator 16 is provided with a dilute solution pipeline connected to the newly added generator A via the new solution heat exchanger B.
  • the generator A and the concentrated solution line are merged with the concentrated solution line after the first solution 1 passes through the first solution heat exchanger 10 via the first solution pump and the new solution heat exchanger B, and will be first
  • the generator 1 has a refrigerant vapor passage communicating with the first condenser 4 to adjust the first generator 1 to have a refrigerant vapor passage and the new generator A is connected, and the new generator A is added and the refrigerant liquid pipeline is newly added.
  • Throttle valve C In communication with the first condenser 4, a new generator A and a refrigerant vapor passage are in communication with the first condenser 4.
  • the concentrated solution of the first generator 1 is heated and depressurized by the first solution heat exchanger 10, then flows through the absorption-generator 16, and the endothermic portion is vaporized into the steam dividing chamber 17; the refrigerant vapor flows through the newly added generator A, The solution heated into the solution is released and the refrigerant vapor is supplied to the first condenser 4, and the concentrated solution of the new generator A is added to the first generator 1 through the first solution pump 7 and the newly added solution heat exchanger B.
  • the concentrated solution line after the solution heat exchanger 10 merges, flows through the absorption-generator 16, and the heat absorption portion vaporizes into the steam separation chamber 17, and the refrigerant vapor flowing through the newly added generator A is released into a refrigerant liquid.
  • the new throttle valve C is throttled into the first condenser 4 to form a single-effect-recovery double-effect third-class absorption heat pump.
  • the single-effect-recovery double-effect third-class absorption heat pump shown in Figure 24 is implemented as follows:
  • the heated medium line in which the absorption-generator 16 communicates with the outside is canceled, the third solution pump 21 is eliminated, and the absorber 3 has a dilute solution line.
  • the third solution heat exchanger 15 is in communication with the absorption-generator 16; a new generator, a new throttle valve and a new solution throttle valve are added, and the first generator 1 has a concentrated solution line through the first solution pump 7.
  • the first solution heat exchanger 10 and the absorption-generator 16 are connected to the steam dividing chamber 17 to be adjusted so that the first generator 1 has a concentrated solution line through the solution throttle valve J and the absorption-generator 16 and the steam dividing chamber 17 Connected, the absorption-generator 16 has a dilute solution line connected to the first generator 1 through the first solution heat exchanger 10 to be adjusted to absorb-the generator 16 has a dilute solution line directly connected to the first generator 1 to absorb -
  • the generator 16 is provided with a dilute solution line connected to the newly added generator A via the first solution heat exchanger 10, and the new generator A and the concentrated solution line are passed through the first solution pump 7 and the first solution heat exchanger 10 After that, the concentrated solution after the first generator 1 passes through the solution throttle valve J
  • the first generator 1 has a refrigerant vapor passage connected to the first condenser 4 to be adjusted to be the first generator 1 has a refrigerant vapor passage connected with the newly added generator A, and then adds the generator A
  • the liquid pipeline is connected to the first condenser 4 via a new throttle valve C, and the new generator A and the refrigerant vapor passage are connected to the first condenser 4; the cold connection between the evaporator 6 and the absorption-generator 16 is cancelled.
  • the agent steam passage, the first generator 1 is provided with a refrigerant vapor passage communicating with the absorption-generator 16.
  • the diluted solution of the absorber 3 is cooled down by the third solution heat exchanger 15 to enter the absorption-generator 16, absorbs the refrigerant vapor from the first generator 1, and radiates heat through the absorption-generator.
  • the solution of 16; the dilute solution of the absorption-generator 16 is divided into two paths - the first path directly enters the first generator 1, and the second path passes through the first solution heat exchanger 10 to enter the new generator A; 1
  • the generated refrigerant vapor is supplied to the newly added generator A and the absorption-generator 16, respectively, and the concentrated solution of the first generator 1 is throttled by the added solution throttle valve J, and then flows through the absorption-generator 16, sucking
  • the hot portion is vaporized into the steam dividing chamber 17; the refrigerant vapor flows through the newly added generator A, the solution heated into it is released, and the refrigerant vapor is supplied to the first condenser 4, and the concentrated solution of the generator A is newly added.
  • the solution pump 7 and the first solution heat exchanger 10 are then passed through the absorption-generator 16, and the endothermic portion is vaporized into the steam dividing chamber 17, and the refrigerant vapor flowing through the newly added generator A is released into a refrigerant liquid, and then After the new throttle valve C is throttled into the first condenser 4, a single effect is formed - Regenerative double-effect third-class absorption heat pump.
  • the heated medium line connecting the absorption-generator 16 to the outside is eliminated, and the new generator, the new solution heat exchanger and the new section are added.
  • the first generator 1 has a concentrated solution pipeline connected to the first solution pump 7, the first solution heat exchanger 10, and the absorption-generator 16 and the steam distribution chamber 17 to be adjusted to have a concentrated solution of the first generator 1
  • the pipeline is connected to the newly added generator A via the new solution heat exchanger B, and the new generator A and the concentrated solution pipeline are passed through the first solution pump 7, the new solution heat exchanger B, and the first solution heat exchanger.
  • the first generator 1 has a refrigerant vapor passage communicating with the first condenser 4 to adjust the first generator 1 to have a refrigerant vapor passage and a new generator A.
  • the generator A is added and then the refrigerant liquid pipeline is added through the new throttle valve C and the first condensation.
  • the device 4 is connected, and the newly added generator A and the refrigerant vapor passage are in communication with the first condenser 4.
  • the concentrated solution of the first generator 1 enters the newly added generator A through the newly added solution heat exchanger B, and the refrigerant vapor generated by the first generator 1 is supplied to the newly added generator A as a driving heat medium, which is cold.
  • the agent vapor flows through the newly added generator A, the solution heated into the solution is released, and the refrigerant vapor is supplied to the first condenser 4, and the concentrated solution of the generator A is newly added to the first solution pump 7, and the new solution heat exchanger B and the first solution heat exchanger 10 are then passed through the absorption-generator 16, and the endothermic portion is vaporized into the steam dividing chamber 17, and the refrigerant vapor flowing through the newly added generator A is released into a refrigerant liquid, and then passed through a new
  • the throttle valve C is throttled into the first condenser 4 to form a single-effect-recovery double-effect third-class absorption heat pump.
  • the single-effect-recovery double-effect third-class absorption heat pump shown in Figure 26 is implemented as follows:
  • the heated medium line in which the absorption-generator 16 communicates with the outside is canceled, the third solution pump is canceled, and the absorber 3 has a dilute solution line through the first
  • the three-solution heat exchanger 15 is in communication with the absorption-generator 16; an additional generator is added and a new throttle valve is added, and the absorption-generator 16 has a dilute solution line through the first solution heat exchanger 10 and the first generator 1 connected to the absorption-generator 16 has a dilute solution line directly connected to the first generator 1, the first generator 1 has a concentrated solution line through the first solution pump 7, the first solution heat exchanger 10 and absorption -
  • the generator 16 is connected to the steam dividing chamber 17 to be adjusted so that the first generator 1 has a concentrated solution line connected to the newly added generator A via the first solution heat exchanger 10, and the newly added generator A and the concentrated solution line are The first solution pump 7, the first solution heat exchanger 10 and the absorption-gen
  • the refrigerant vapor channel is connected with the new generator A and newly added. Then, the refrigerant liquid pipeline is connected to the first condenser 4 via the newly added throttle valve C, and the new generator A and the refrigerant vapor passage are connected to the first condenser 4; the evaporator 6 and the absorption are cancelled.
  • the coolant 16 is connected to the refrigerant vapor passage, and the first generator 1 is provided with a refrigerant vapor passage communicating with the absorption-generator 16.
  • the dilute solution of the absorber 3 is cooled down by the third solution heat exchanger 15 to enter the absorption-generator 16, absorbs the refrigerant vapor from the first generator 1, and radiates heat through the absorption-generator
  • the solution of 16 the dilute solution of the absorption-generator 16 directly enters the first generator 1, and the refrigerant vapor generated by the first generator 1 is supplied to the new generator A and the absorption-generator 16, respectively, the first generator 1
  • the concentrated solution enters the new generator A through the first solution heat exchanger 10; the refrigerant vapor flows through the newly added generator 8.
  • the solution heated into the solution is released and supplies the refrigerant vapor to the first condenser 4, adding
  • the concentrated solution of the generator A passes through the first solution pump 7 and the first solution heat exchanger 10 and then flows through the absorption-generator 16 to vaporize the heat absorption portion into the steam separation chamber 17, and flows through the refrigerant of the newly added generator A.
  • the steam is exothermic into a refrigerant liquid, and then throttled into the first condenser 4 through a new throttle valve C to form a single-effect-recovery double-effect third-class absorption heat pump.
  • the single-effect-recovery double-effect third-class absorption heat pump shown in Figure 27 is implemented as follows:
  • the absorption-generator 16 has a dilute solution line connected to the first generator 1 through the first solution heat exchanger 10 to adjust to absorption - the generator 16 has a dilute solution line first solution heat
  • the exchanger 10 and the newly added solution heat exchanger B are in communication with the newly added generator A, and the new generator A and the concentrated solution pipeline are added to the new solution pump D and the new solution heat exchanger B and the first generator 1
  • the first generator 1 has a refrigerant vapor passage connected to the first condenser 4 to be adjusted to be the first generator 1 has a refrigerant vapor passage connected with the newly added generator A, and then adds the generator A and then the refrigerant liquid
  • the pipeline is connected to the first condenser 4 via
  • the dilute solution of the absorption-generator 16 enters the newly added generator A through the first solution heat exchanger 10 and the newly added solution heat exchanger B, and the refrigerant vapor generated by the first generator 1 is supplied to the newly generated one.
  • the device A acts as a driving heat medium, and the refrigerant vapor flows through the newly added generator. 8.
  • the solution heated into the solution is released and the refrigerant vapor is supplied to the first condenser 4, and the concentrated solution of the generator A is newly added through the new solution pump.
  • the single-effect-recovery double-effect third-class absorption heat pump shown in Figure 28 is implemented as follows:
  • the absorption-generator 16 has a dilute solution line connected to the first generator 1 through the first solution heat exchanger 10 to adjust to absorption - the generator 16 has a dilute solution line first solution heat exchanger 10 and new
  • the generator A is connected, the new generator A and the concentrated solution pipeline are connected to the first generator 1 via the first solution pump 7 and the first solution heat exchanger 10, and the first generator 1 has a refrigerant vapor passage.
  • the generator A is newly added, and then the refrigerant liquid pipeline is connected with the first condenser 4 through the newly added throttle valve C, and the new generator A is also provided with the refrigerant vapor passage and the first condensation.
  • the device 4 is connected; the refrigerant vapor passage of the evaporator 6 and the absorption-generator 16 is eliminated, and the first generator 1 is provided with a refrigerant vapor passage communicating with the absorption-generator 16.
  • the dilute solution of the absorber 3 is cooled down by the third solution heat exchanger 15 to enter the absorption-generator 16, absorbs the refrigerant vapor from the first generator 1, and radiates heat through the absorption-generator
  • the refrigerant vapor flows through the newly added generator A, the solution heated into the solution is released, and the refrigerant vapor is supplied to the first condenser 4, and the concentrated solution of the newly added generator A is exchanged with the first solution pump 7 and the first solution.
  • the device 10 enters the first generator 1, and the concentrated solution of the first generator 1 is throttled by the new throttle valve J, and then flows through the absorption-generator 16 and the heat absorption portion is vaporized into the steam distribution chamber 17, and flows through The refrigerant vapor of the generator A is radiated into a refrigerant liquid, and then throttled into the first condenser 4 through a new throttle valve C to form a single-effect-recovery double-effect third-class absorption heat pump.
  • the single-effect-recovery three-effect third-class absorption heat pump shown in Figure 29 is implemented as follows:
  • a new second generator is added, a second solution heat exchanger is added, and a second throttle valve is added, and the second solution pump 14 is added with a thinner
  • the solution line is connected to the newly added second generator E by adding the second solution heat exchanger F, and the second generator E and the concentrated solution line are newly added to the second solution heat exchanger F and the third generation occurs.
  • the device 12 is connected, and the newly added first generator A has a refrigerant vapor channel connected to the first condenser 4 to be adjusted to add a new first generator A.
  • the refrigerant vapor channel is connected with the newly added second generator E.
  • the second generator E further has a refrigerant liquid pipeline connected to the first condenser 4 via a new second throttle valve G, and a second generator E and a refrigerant vapor passage are connected to the first condenser 4.
  • the single-effect-recovery three-effect third-class absorption heat pump shown in Figure 30 is implemented as follows:
  • a new second generator is added, a second solution heat exchanger is added, and a second throttle valve is added, and the second solution pump 14 is provided.
  • the dilute solution pipeline is connected to the first generator 1 via the newly added first solution heat exchanger B and the third solution heat exchanger 15 to be adjusted to be the second solution pump 14 having a dilute solution pipeline by adding a second solution heat
  • the exchanger F, the newly added first solution heat exchanger B and the third solution heat exchanger 15 are in communication with the first generator 1, and the newly added first generator A has a concentrated solution pipeline through the newly added first solution heat exchange
  • the B is connected to the third generator 12 to be adjusted to add a first generator A.
  • the concentrated solution pipeline is connected to the newly added second generator E by adding the first solution heat exchanger B, and the second generator E is newly added. Further, the concentrated solution pipeline is connected to the third generator 12 via the newly added second solution heat exchanger F, and the newly added first generator A has a refrigerant vapor passage connected to the first condenser 4 to be newly added first.
  • the generator A has a refrigerant vapor passage connected with the newly added second generator E, and then a second generator E is added, and then the refrigerant liquid pipeline is connected to the first condenser 4 via the addition of the second throttle valve G,
  • the second generator E is further connected with the refrigerant vapor passage to communicate with the first condenser 4; the waste heat medium pipeline connecting the third generator 12 with the outside is cancelled, the third throttle valve is added, and the first generator is added.
  • a additional refrigerant vapor passage is connected with the third generator 12, and then the third generator 12 has a refrigerant liquid pipeline via a new third throttle valve and the first The condenser 4 is connected.
  • the newly added refrigerant vapor generated by the first generator A is separately supplied to the newly added second generator E and the third generator 12 as the driving heat medium, and the concentrated solution of the first generator A is newly added.
  • the first solution heat exchanger B enters a new second generator E, and the refrigerant vapor flows through the newly added second generator E, and the solution heated therein is released and supplies the refrigerant vapor to the first condenser 4, flowing through
  • the refrigerant vapor of the second generator E is newly added into a refrigerant liquid, and then the second throttle valve G is added to enter the first condenser 4; the concentrated solution of the second generator E is newly added by the second
  • the solution heat exchanger F enters the third generator 12, and the refrigerant vapor flows through the third generator 12, and the solution heated therein is released and supplies the refrigerant vapor to the second absorber 13 to flow through the third generator.
  • the refrigerant vapor of 12 is exothermed into a refrigerant liquid, and then added to the first condenser 4 by adding a third throttle valve I; the dilute solution of the second absorber 13 is passed through the second solution pump 14, and the second solution heat is added.
  • the first solution heat exchanger B and the third solution heat exchanger 15 are added to the first generator 1, and a single-effect-recovery three-effect type III absorption heat pump is formed.
  • the second solution pump 14 has a dilute solution line connected to the newly added first generator A via the third solution heat exchanger 15 to adjust the second solution pump 14 to have a dilute solution line through the third solution heat exchanger 15 and the new
  • the second generator E is connected, the second generator E and the concentrated solution pipeline are connected to the newly added first generator A by adding the second solution pump H and the newly added second solution heat exchanger F
  • the first generator 1 has a concentrated solution pipeline connected to the third generator 12 via the newly added first solution heat exchanger B and the third solution heat exchanger 15 to be adjusted to be the second generator 2
  • the first solution heat exchanger B, the newly added second solution heat exchanger F and the third solution heat exchanger 15 are in communication with the third generator 12, and the first generator A is added with the refrigerant vapor passage and the first condensation.
  • the refrigerant liquid pipeline is connected to the first condenser 4 via the addition of the second section flow G, and the second generator E is further provided with the refrigerant vapor passage and the first condenser. 4 communicating; canceling the residual heat medium pipeline of the third generator 12 and the outside, adding a new third section of the flow, the first generator 1 is connected with the third generator 12 after the refrigerant vapor passage is connected with the third generator 12 Further, the refrigerant liquid line is connected to the first condenser 4 via the addition of the third throttle valve I.
  • the dilute solution of the second absorber 13 enters the newly added second generator E through the second solution pump 14 and the third solution heat exchanger 15 to add the refrigerant vapor generated by the first generator A to the new
  • the second generator E is added to drive the heat medium, and the refrigerant vapor flows through the newly added second generator E, and the solution heated into the liquid is released and supplies the refrigerant vapor to the first condenser 4, and flows through the second generation.
  • the refrigerant vapor of the device E is radiated into a refrigerant liquid, and then the second throttle valve G is added to the first condenser 4, and the concentrated solution of the second generator E is newly added by adding the second solution pump H and the new
  • the second solution heat exchanger E is added to the newly added first generator A; the concentrated solution of the first generator 1 is added with the first solution heat exchanger B, the second solution heat exchanger F and the third solution heat are added.
  • the exchanger 15 enters the third generator 12, and the refrigerant vapor generated by the first generator 1 is supplied to the newly added first generator A and the third generator 12 as driving heat medium, and the refrigerant vapor flows through the third generator.
  • the single-effect-recovery three-effect third-class absorption heat pump shown in Figure 32 is implemented as follows:
  • the addition of the second generator in the third type of absorption heat pump shown in Fig. 23, the addition of the second generator, the addition of the second solution heat exchanger and the addition of the second throttle valve will be added, and the first generator will be added.
  • the concentrated solution line of A is merged with the concentrated solution line after the first solution heat exchanger 10 is passed through the first solution pump 7 and the first solution heat exchanger B, and is added to the first step.
  • the generator A has a concentrated solution line which is merged with the concentrated solution line after the first solution 1 passes through the first solution heat exchanger 10 after adding the first solution heat exchanger B, and the absorption-generator 16 adds a dilute solution tube.
  • the second solution heat exchanger F is newly connected with the newly added second generator E, and the second generator E and the concentrated solution pipeline are added through the first solution pump 7 and the second solution heat exchanger F. Thereafter, the first generator 1 is merged with the concentrated solution pipeline after the first solution heat exchanger 10, and the newly added first generator A has a refrigerant vapor passage connected to the first condenser 4 to be adjusted to be newly added.
  • A has a refrigerant vapor channel connected to the new second generator E to add a second occurrence E and then the refrigerant liquid pipe of the second throttle valve G communicates with the new first condenser 4, as well as new second generator E passage communicating with the first refrigerant vapor condenser 4.
  • the hot refrigerant liquid is added to the first condenser 4 by adding a second throttle valve G; the concentrated solution of the first generator A is added after the first solution heat exchanger B is added, and then flows through the absorption-occurrence The heat absorbing portion is vaporized into the steam dividing chamber 17 to form a single-effect-recovery three-effect third-class absorption heat pump.
  • the single-effect-recovery three-effect third-class absorption heat pump shown in Figure 33 is implemented as follows:
  • the B is connected to the newly added second generator E, and the second generator E and the concentrated solution pipeline are added to the first generator 1 through the first solution pump 7 and the new solution heat exchanger B.
  • the second generator E is connected, the second generator E is added, and then the refrigerant liquid pipeline is added with the second throttle.
  • G in communication with the first condenser 4, as well as new second generator E passage communicating with the first refrigerant vapor condenser 4.
  • the refrigerant coolant generated by the first generator A is newly supplied to the second generator E to drive the heat medium, and the concentrated solution of the first generator A is added after passing through the first solution heat exchanger 10.
  • the exchanger B flows through the absorption-generator 16
  • the heat absorption portion is vaporized into the steam separation chamber 17, and the refrigerant vapor flowing through the newly added second generator E is radiated into a refrigerant liquid, and then the second section is added.
  • the flow valve G enters the flow
  • the single-effect-recovery three-effect third-class absorption heat pump shown in Figure 34 is implemented as follows:
  • the absorption-generator 16 has a dilute solution line directly
  • the first generator 1 is connected and adjusted to be an absorption-generator 16 having a dilute solution line connected to the first generator 1 via the first solution heat exchanger 10, and the first generator 1 has a concentrated solution line through the newly added solution section.
  • the flow valve J and the absorption-generator 16 are connected to the steam distribution chamber 17 to be adjusted so that the first generator 1 has a concentrated solution line connected to the steam distribution chamber 17 via the first solution heat exchanger 10 and the absorption-generator 16 to absorb - the generator 16 has a dilute solution line connected to the newly added first generator A via the first solution heat exchanger 10 to be adjusted to absorb - the generator 16 has a dilute solution line directly connected to the newly added first generator A,
  • the first first generator A has a concentrated solution pipeline connected to the steam distribution chamber 17 through the first solution heat exchanger 10 and the absorption-generator 16 to be newly added to the first generator A.
  • the concentrated solution pipeline has a new solution.
  • the throttle valve J and the absorption-generator 16 are in communication with the steam dividing chamber 17, and the first generator 1 has a refrigerant vapor passage communicating with the absorption-generator 16 to adjust the newly added first generator A to have a refrigerant vapor passage and The absorption-generator 16 is in communication.
  • the dilute solution of the absorption-generator 16 is divided into three paths - the first path enters the first generator 1 via the first solution heat exchanger 10, and the second path directly enters the newly added first generator A, the third
  • the newly added solution heat exchanger B enters the newly added second generator E;
  • the newly added refrigerant vapor generated by the first generator A is separately supplied to the newly added second generator E and the absorption-generator 16, the refrigerant vapor Flowing through the newly added second generator E, releasing the solution into which it is heated and supplying the refrigerant vapor to the first condenser 4, and flowing the refrigerant vapor flowing through the second generator E to release the refrigerant liquid, and then
  • the second throttle valve G is added to enter the first condenser 4;
  • the concentrated solution of the first generator 1 passes through the first solution heat exchanger 10 and then flows through the absorption-generator 16 to vaporize the heat absorption portion and enter the steam separation portion.
  • the single-effect-recovery three-effect third-class absorption heat pump shown in Figure 35 is implemented as follows:
  • the addition of the second generator, the addition of the second solution heat exchanger and the addition of the second throttle valve will add a first generator.
  • a concentrated solution pipeline is connected to the first solution heat exchanger 10 via the first solution pump 7 and the newly added first solution heat exchanger B to be newly added, the first generator A has a concentrated solution pipeline, and the second is added.
  • the solution heat exchanger F is connected to the newly added second generator E, and the second generator E and the concentrated solution line are added through the first solution pump 7, the second solution heat exchanger F is added, and the first solution is added.
  • the heat exchanger B is in communication with the first solution heat exchanger 10, and the newly added first generator A has a refrigerant vapor passage communicating with the first condenser 4 to adjust the new first generator A to have a refrigerant vapor passage and a new one.
  • the second generator E is connected, the second generator E is newly added, and then the refrigerant liquid pipeline is connected with the first condenser 4 through the addition of the second throttle valve G, and the second generator E is added with the refrigerant.
  • the steam passage is in communication with the first condenser 4.
  • the concentrated solution of the first generator A is newly added to the second solution E by adding the second solution heat exchanger F, and the refrigerant vapor generated by the first generator A is newly added to the new one.
  • the second generator E serves as a driving heat medium, and the refrigerant vapor flows through the newly added second generator E, the solution heated into the solution is released, and the refrigerant vapor is supplied to the first condenser 4, and the second generator E is added.
  • the solution is passed through the first solution pump 7, and the second solution heat exchanger is added.
  • Adding the first solution heat exchanger B and the first solution heat exchanger 10 then flowing through the absorption-generator 16, vaporizing the heat absorption portion, and entering the steam separation chamber 17, flowing through the cold of the second generator E.
  • the agent steam exotherms into a refrigerant liquid, and then enters the first condenser 4 by adding a second throttle valve G to form a single-effect-recovery three-effect third-type absorption heat pump.
  • the single-effect-recovery three-effect third-class absorption heat pump shown in Figure 36 is implemented as follows:
  • the addition of the second generator, the new solution heat exchanger and the addition of the second throttle valve will be added, and the first generator A will be added.
  • the concentrated solution pipeline is connected to the first solution heat exchanger 10 via the first solution pump 7 to be newly added to the first generator A.
  • the concentrated solution pipeline is connected to the newly added second generator E via the new solution heat exchanger B.
  • the second generator E and the concentrated solution pipeline are connected to the first solution heat exchanger 10 via the first solution pump 7 and the new solution heat exchanger B, and the first generator A is added with refrigerant vapor.
  • the passage is connected with the first condenser 4 to adjust to add a new first generator A.
  • the refrigerant vapor passage is connected with the newly added second generator E, and then the second generator E is added and the refrigerant liquid pipeline is newly added.
  • the second throttle valve G is connected to the first condenser 4, and the second generator E and the refrigerant vapor passage are connected to the first condenser 4.
  • the concentrated solution of the first generator A is newly added to the newly added second heat exchanger B through the new solution heat exchanger B, and the new refrigerant generated by the first generator A is newly supplied to the second generation.
  • the device E serves as a driving heat medium, and the refrigerant vapor flows through the newly added second generator E, the solution heated into the solution is released, and the refrigerant vapor is supplied to the first condenser 4, and the concentrated solution of the second generator E is newly added.
  • the first solution pump 7, the new solution heat exchanger B and the first solution heat exchanger 10 are then passed through the absorption-generator 16, and the heat absorption portion is vaporized and then enters the steam separation chamber 17, and flows through the new second generator.
  • the refrigerant vapor of E is exothermic into a refrigerant liquid, and then added to the second throttle valve G to enter the first condenser 4 to form a single-effect-recovery three-effect third-type absorption heat pump.
  • the single-effect-recovery three-effect third-class absorption heat pump shown in Figure 37 is implemented as follows:
  • the absorption-generator 16 has a dilute solution line directly connected to the first generator 1 and adjusted to an absorption-generator 16
  • the dilute solution pipeline is connected to the first generator 1 via the new solution pump D and the first solution heat exchanger 10
  • the second generator E has a concentrated solution pipeline through the first solution pump 7 and the newly added solution.
  • the heat exchanger B is connected to the first solution heat exchanger 10 to be adjusted to add a second generator E.
  • the concentrated solution line is connected to the absorption-generator 16 via the first solution pump 7 and the new solution heat exchanger B.
  • the first generator 1 has a refrigerant vapor passage communicating with the absorption-generator 16 to adjust to add a first generator A having a refrigerant vapor passage in communication with the absorption-generator 16.
  • the dilute solution of the absorption-generator 16 enters the first generator 1 via the new solution pump D and the first solution heat exchanger 10, and the newly added refrigerant vapor generated by the first generator A is separately supplied to the new generator
  • the second generator E and the absorption-generator 16 add a concentrated solution of the second generator E through the first solution pump 7 and the newly added solution heat exchanger B, and then flow through the absorption-generator 16 to vaporize the endothermic portion.
  • a single-effect-recovery three-effect third-class absorption heat pump is formed.
  • the second new solution pump H and the newly added second solution heat exchanger F are connected to the newly added first generator A, and the newly added first generator A has a refrigerant vapor passage connected to the first condenser 4 to be adjusted.
  • the refrigerant vapor channel is connected with the newly added second generator E, and then the second generator E is added, and then the refrigerant liquid pipeline is added with the second throttle valve G and the first condensation.
  • the device 4 is connected, and a second generator E and a refrigerant vapor passage are connected to communicate with the first condenser 4.
  • the concentrated solution of the absorption-generator 16 enters the newly added second generator E through the first solution heat exchanger 10, the newly added first solution heat exchanger B, and the newly added second solution heat exchanger F, Increasing the refrigerant vapor generated by the first generator A is supplied to the newly added second generator E as a driving heat medium, and the refrigerant vapor flows through the newly added second generator E, and the solution heated into the liquid is released and discharged to the first condensation
  • the device 4 supplies the refrigerant vapor, and the refrigerant vapor flowing through the second generator E is dissipated into a refrigerant liquid, and then the second section G is added to the first condenser 4, and the second generator is added.
  • the concentrated solution of E is added to the first first generator A by adding a second solution pump H and a new second solution heat exchanger F to form a single-effect-recovery three-effect third-type absorption heat pump.
  • the first solution heat exchanger 10 has a dilute solution line and is connected to the newly added first generator A to adjust the absorption-generator 16 with a dilute solution line through the first solution heat exchanger 10 and the new solution heat exchanger.
  • B is connected with the newly added second generator E, and the second generator E and the concentrated solution pipeline are added through the new solution pump D.
  • the newly added solution heat exchanger B is connected with the newly added first generator A, and the newly added first generator A has a refrigerant vapor passage and communicates with the first condenser 4 to adjust the newly added first generator A to have a refrigerant.
  • the steam passage is connected with the newly added second generator E, the second generator E is newly added, and the refrigerant liquid pipeline is connected with the first condenser 4 through the addition of the second throttle valve G, and the second generator E is newly added.
  • the concentrated solution of the absorption-generator 16 enters the newly added second generator E through the first solution heat exchanger 10 and the newly added solution heat exchanger B, and the refrigerant vapor generated by the first generator A is newly supplied.
  • the second generator E is added to drive the heat medium, and the refrigerant vapor flows through the newly added second generator E, and the solution heated into the solution is released and supplies the refrigerant vapor to the first condenser 4, and flows through the new section.
  • the refrigerant vapor of the second generator E is radiated into a refrigerant liquid, and then the second throttle valve G is added to enter the first condenser 4, and the concentrated solution of the second generator E is newly added by the new solution pump D and new The solubilizing solution heat exchanger B enters the newly added first generator A to form a single-effect-recovery three-effect third-class absorption heat pump.
  • the single-effect-recovery three-effect third-class absorption heat pump shown in Figure 40 is implemented as follows:
  • the new solution throttle valve is cancelled, and the first generator 1 has a concentrated solution line through the newly added solution throttle valve J and the absorption-generator 16 is connected to the steam dividing chamber 17 to be adjusted so that the first generator 1 has a concentrated solution line connected to the steam dividing chamber 17 via the first solution heat exchanger 10 and the absorption-generator 16 , and the absorption-generator 16 has a dilute solution tube
  • the first solution heat exchanger 10 and the new solution heat exchanger B are connected to the newly added second generator E to be adjusted to absorb-the generator 16 has a dilute solution line through the new solution heat exchanger B and the new addition
  • the two generators E are connected, and the first generator 1 has a refrigerant vapor passage connected to the absorption-generator 16 to be adjusted to add a first generator A.
  • the additional refrigerant vapor passage is in communication with the absorption-generator 16.
  • the dilute solution of the absorption-generator 16 enters the newly added second generator E through the newly added solution heat exchanger B, and the newly added refrigerant vapor generated by the first generator A is separately supplied to the newly added second generator.
  • the concentrated solution of the first generator 1 passes through the first solution heat exchanger 10 and then flows through the absorption-generator 16, and the endothermic portion is vaporized and then enters the steam separation chamber 17, forming a single-effect-return Thermal three-effect third-class absorption heat pump.
  • the single-effect -1. 5 third-class absorption heat pump shown in Figure 41 is implemented as follows:
  • a new solution heat exchanger, a new absorption-evaporator and a new refrigerant liquid pump are added, and the absorber 3 has a dilute solution line.
  • the first solution heat exchanger 10 is connected to the first generator 1 to be adjusted so that the absorber 3 has a dilute solution line connected to the newly added absorption-evaporator K via the newly added solution heat exchanger B, and the new absorption-evaporator K is further added.
  • the dilute solution line is connected to the first generator 1 via the first solution heat exchanger 10, and the first generator 1 has a concentrated solution line through the first solution pump 7 and the first solution heat exchanger 10 and the second solution
  • the heat exchanger 11 is connected to be adjusted so that the first generator 1 has a concentrated solution line connected to the second solution heat exchanger 11 via the first solution pump 7, the first solution heat exchanger 10, and the new solution heat exchanger B
  • the evaporator 6 has a refrigerant vapor passage communicating with the absorber 3 to adjust the evaporator 6 to have a refrigerant vapor passage communicating with the newly added absorption-evaporator K
  • the first condenser 4 is provided with a refrigerant liquid pipeline through the newly added refrigerant liquid.
  • Pump L is connected to the new absorption-evaporator K and then added absorption-evaporator K and then cold Steam passage 3 communicating with the absorber.
  • the dilute solution of the absorber 3 enters the new absorption-evaporator K through the newly added solution heat exchanger B, absorbs the refrigerant vapor from the evaporator 6, and radiates heat through the new absorption-evaporator.
  • a refrigerant solution a dilute solution of the new absorption-evaporator ⁇ enters the first generator 1 through the first solution heat exchanger 10, and the concentrated solution of the first generator 1 passes through the solution pump 7, the first solution heat exchanger 10,
  • the new solution heat exchanger ⁇ and the second solution heat exchanger 11 enter the second generator 2; the refrigerant liquid of the first condenser 4 is divided into two paths - the first passage is pressurized by the refrigerant liquid pump 8 into the evaporator 6, the second way is added by the new refrigerant liquid pump L and then flows through the new absorption-evaporator, the heat is absorbed into the refrigerant vapor and is supplied to the absorber 3, forming a single effect - 1. 5 level third class Absorption heat pump.
  • the single-effect - 1. 5 third-class absorption heat pump shown in Figure 42 is implemented as follows: 1Structure, in the third type of absorption heat pump shown in Figure 1, adding a new solution heat exchanger, a new solution pump, a new absorption-evaporator and a new refrigerant liquid pump, the second generator 2
  • the concentrated solution pipeline is connected to the absorber 3 through the second solution heat exchanger 11 to be adjusted to be the second generator 2 having the concentrated solution pipeline passing through the second solution heat exchanger 11 and the newly added solution heat exchanger B and adding
  • the absorption-evaporator K is connected, the new absorption-evaporator K and the dilute solution line are connected to the absorber 3 via the new solution pump D and the new solution heat exchanger B, and the evaporator 6 has a refrigerant vapor channel and
  • the absorber 3 is connected to the evaporator 6 and has a refrigerant vapor passage communicating with the newly added absorption-evaporator K.
  • the evaporator 6 is provided with a refrigerant liquid pipeline connected to the newly added absorption liquid evaporator L through the newly added refrigerant liquid pump L. After that, the absorption-evaporator K is added and the refrigerant vapor passage is connected to the absorber 3.
  • the concentrated solution of the second generator 2 enters the new absorption-evaporator K through the second solution heat exchanger 11 and the new solution heat exchanger B, absorbs the refrigerant vapor from the evaporator 6, and radiates heat.
  • Flow through the new absorption-evaporator enthalpy solution add a new absorption-evaporator ⁇ dilute solution through the new solution pump D and the new solution heat exchanger ⁇ into the absorber 3, absorption from the new absorption-evaporation
  • the refrigerant vapor of the crucible is exothered in the heated medium; the refrigerant liquid of the evaporator 6 is divided into two paths - the first passage absorbs the residual heat into the refrigerant vapor and supplies it to the newly added absorption-evaporator, the second passage
  • the new refrigerant liquid pump L is pressurized and then flows through the new absorption-evaporator ⁇ , the heat is absorbed into the refrigerant vapor, and is supplied to the absorber 3 to form
  • the single-effect -1. 5 third-class absorption heat pump shown in Figure 43 is implemented as follows:
  • the liquid pipeline is connected to the absorber 3 by adding a new refrigerant liquid pump L and a new absorption-evaporator ⁇ , and then a refrigerant vapor channel is connected to the absorber 3.
  • the concentrated solution of the first generator 1 enters the new absorption-evaporator through the solution pump 7, the first solution heat exchanger 10 and the newly added solution heat exchanger: absorbs the refrigerant vapor from the evaporator 6. And exothermic to the refrigerant liquid flowing through the new absorption-evaporator , adding a dilute solution of the absorption-evaporator ⁇ to the new solution pump D, the new solution heat exchanger B and the second solution heat exchanger 11 Entering the second generator 2, the concentrated solution of the second generator 2 enters the absorber 3 through the second solution heat exchanger 11, absorbs the refrigerant vapor from the newly added absorption-evaporator K, and heats the heated medium; the evaporator 6
  • the refrigerant liquid is divided into two paths - the first path absorbs the waste heat into the refrigerant vapor and supplies it to the new absorption-evaporator K, and the second channel is pressurized by the newly added refrigerant liquid pump L and then flows through the newly absorbed
  • a new solution heat exchanger, a new absorption-evaporator and a new refrigerant liquid pump are added, and the absorber 3 has a dilute solution line.
  • the first solution heat exchanger 10 is connected to the second absorber 13 to be adjusted so that the absorber 3 has a dilute solution line through the new solution heat exchanger and is connected to the new absorption-evaporator, and the absorption-evaporator is added.
  • the dilute solution line is connected to the second absorber 13 via the first solution heat exchanger 10, and the third generator 12 has a concentrated solution line through the first solution pump 7 and the first solution heat exchanger 10 and the second solution.
  • the heat exchanger 11 is connected to be adjusted so that the third generator 12 has a concentrated solution line connected to the second solution heat exchanger 11 via the first solution pump 7, the first solution heat exchanger 10, and the new solution heat exchanger ,
  • the evaporator 6 has a refrigerant vapor passage connected to the absorber 3 to be adjusted so that the evaporator 6 has a refrigerant vapor passage connected to the newly added absorption-evaporator, and the evaporator 6 adds a refrigerant liquid pipeline through the newly added refrigerant liquid pump L.
  • an absorption-evaporator K is added and then a refrigerant vapor passage is connected to the absorber 3.
  • the dilute solution of the absorber 3 is introduced into the new absorption-evaporator via the newly added solution heat exchanger B, absorbs the refrigerant vapor from the evaporator 6, and radiates heat to the cold flowing through the new absorption-evaporator K.
  • the liquid solution, the dilute solution of the new absorption-evaporator K is introduced into the second absorber 13 through the first solution heat exchanger 10; the refrigerant liquid of the evaporator 6 is divided into two paths - the first path absorbs the residual heat into the refrigerant vapor and Provided to the newly added absorption-evaporator K, the second passage is pressurized by the newly added refrigerant liquid pump L, then flows through the new absorption-evaporator K, absorbs heat into the refrigerant vapor, and supplies it to the absorber 3;
  • the concentrated solution of the generator 12 enters the second generator 2 via the first solution pump 7, the first solution heat exchanger 10, the new solution heat exchanger ⁇ and the second solution heat exchanger 11 to form a single-effect-recovery type 1.
  • Class 5 third type absorption heat pump Class 5 third type absorption heat pump.
  • the fifth-stage type III absorption heat pump is realized as follows:
  • the concentrated solution of the second generator 2 passes through the second solution heat exchanger 11 and the newly added solution heat exchanger, enters the new absorption-evaporator, absorbs the refrigerant vapor from the evaporator 6, and radiates heat.
  • the fifth-stage type III absorption heat pump is realized as follows:
  • the third generator 12 has a concentrated solution pipeline through the first solution pump 7 and the first solution heat exchanger 10 and the second solution heat exchanger 11 communicated to adjust the third generator 12 has a concentrated solution pipeline through the first solution pump 7, first
  • the solution heat exchanger 10 and the new solution heat exchanger ⁇ are connected to the new absorption-evaporator, and the new absorption-evaporator and the dilute solution line are added to the new solution pump D and the new solution heat exchanger.
  • the liquid pipeline is connected to the absorber 3 by adding a new refrigerant liquid pump L to the new absorption-evaporator and then adding an absorption-evaporator and then a refrigerant vapor passage.
  • the concentrated solution of the third generator 12 passes through the solution pump 7, the first solution heat exchanger 10 and the newly added solution heat exchanger, enters the new absorption-evaporator, and absorbs the refrigerant vapor from the evaporator 6. And exothermic to the cold liquid flowing through the new absorption-evaporator, adding a dilute solution of the absorption-evaporator ⁇ through the new solution pump D, the new solution heat exchanger B and the second solution heat exchanger 11 Entering the second generator 2, the concentrated solution of the second generator 2 enters the absorber 3 through the second solution heat exchanger 11, absorbs the refrigerant vapor from the newly added absorption-evaporator K, and releases the heat to the heated medium;
  • the refrigerant liquid of the device 6 is divided into two paths - the first path absorbs the residual heat into the refrigerant vapor and is supplied to the newly added absorption-evaporator K, and the second path is pressurized by the newly added refrigerant liquid pump L, and then flows through the new The absorption
  • the third solution pump 21 is cancelled, and the diluted solution line of the absorber 3 is connected to the absorption-generator 16 via the third solution heat exchanger 15;
  • the refrigerant liquid pump is newly added, and the refrigerant vapor passage connecting the evaporator 6 and the absorber 3 is canceled, and the refrigerant line of the first condenser 4 is added by the newly added refrigerant liquid pump L and the absorption-generator 16 is connected and absorbed.
  • the generator 16 also has a refrigerant vapor passage in communication with the absorber 3.
  • the dilute solution of the absorber 3 enters the absorption-generator 16 through the third solution heat exchanger 15, absorbs the refrigerant vapor from the evaporator 6, and respectively releases the solution flowing through the absorption-generator 16 and is cooled.
  • the liquid of the first condenser 4 is divided into two paths - the first passage is pressurized by the refrigerant liquid pump 8 into the evaporator 6, and the second passage is pressurized by the newly added refrigerant liquid pump L and then flows through
  • the absorption-evaporator K and the heat-absorbing refrigerant vapor are added to the absorber 3 to form a single-effect-recovery type 1.5 third-class absorption heat pump.
  • the fifth-class type III absorption heat pump is realized as follows:
  • the third solution pump 21 is eliminated, and the absorber 3 has a dilute solution line connected to the absorption-generator 16 via the third solution heat exchanger 15;
  • a new absorption-evaporator and a new refrigerant liquid pump are added, and the absorption-generator 16 has a dilute solution line connected to the first generator 1 via the first solution heat exchanger 10 to be adjusted to absorb-the generator 16 has a dilute solution.
  • the pipeline is directly connected to the new absorption-evaporator, and the new absorption-evaporator and the dilute solution pipeline are connected to the first generator 1 via the first solution heat exchanger 10, and the first evaporator 6 is cooled.
  • the vapor passage of the agent is connected to the absorber 3 to be adjusted so that the first evaporator 6 has a refrigerant vapor passage connected to the newly added absorption-evaporator, and the first condenser 4 adds a refrigerant liquid pipeline through the newly added refrigerant liquid pump L and After the absorption-generator 16 is connected, the absorption-generator 16 and the refrigerant vapor passage are in communication with the absorber 3.
  • the dilute solution of the absorber 3 is cooled down by the third solution heat exchanger 15 into the absorption-generator 16, the dilute solution of the absorption-generator 16 enters the new absorption-evaporator, and the absorption is from the evaporator 6.
  • the refrigerant vapor is exothermic to the refrigerant liquid flowing through the absorption-generator 16, and the dilute solution of the new absorption-evaporator ⁇ is introduced into the first generator 1 through the first solution heat exchanger 10; the first condenser 4
  • the refrigerant liquid is divided into two paths - the first passage is pressurized into the evaporator 6 by the refrigerant liquid pump 8, and the second passage is pressurized by the newly added refrigerant liquid pump L, and then flows through the new absorption-evaporator,
  • the heat is cooled to a refrigerant vapor and supplied to the absorber 3 to form a single-effect-recovery type 1.5 third-stage absorption heat pump.
  • the fifth-stage type III absorption heat pump is implemented as follows:
  • the communication with the absorber 3 is adjusted so that the first evaporator 6 has a refrigerant vapor passage connected to the newly added absorption-evaporator, and the second condenser 5 adds a refrigerant liquid pipeline through the newly added throttle valve C and newly absorbed - After the evaporator is connected, an absorption-evaporator is added, and then a refrigerant vapor passage is connected to the absorber 3.
  • the concentrated solution of the second generator 2 passes through the second solution heat exchanger 11 and the newly added solution heat exchanger, enters the new absorption-evaporator, absorbs the refrigerant vapor from the first evaporator 6, and puts The hot liquid flows through the new absorption-evaporator ,, and the dilute solution of the new absorption-evaporator ⁇ is added to the absorber through the new solution pump D and the new solution heat exchanger, and the absorption is from the new absorption.
  • the refrigerant liquid of the second condenser 5 is divided into two paths - the first passage enters the first evaporator 6 via the throttle valve 9, the second passage is new After the throttle valve C is throttled, it flows through the new absorption-evaporator ⁇ , absorbs the refrigerant vapor, and supplies it to the absorber 3 to form a single-effect-recovery type 1.5 third-class absorption heat pump.
  • the refrigerant liquid of the second condenser 5 is all throttled by the newly added throttle valve C. Flow through the new absorption-evaporator K, at which time no refrigerant liquid is supplied to the first evaporator 6 via the throttle valve 9.
  • the fifth-stage type III absorption heat pump is realized as follows:
  • the concentrated solution line is connected to the second solution heat exchanger 11 via the second solution pump 14 and the third solution heat exchanger 15 to be adjusted to the steam dividing chamber 17 having the concentrated solution line passing through the second solution pump 14, the third solution heat
  • the exchanger 15 and the new solution heat exchanger B are connected to the newly added absorption-evaporator K, and the new absorption-evaporator K and the dilute solution pipeline are added to the new solution pump D and the new solution heat exchanger B and the first
  • the two solution heat exchanger 11 is connected to cancel the refrigerant vapor passage connecting the first evaporator 6 and the absorber 3, and the evaporator 6 is provided with a refrigerant liquid pipeline via the newly added refrigerant liquid pump L and the newly added absorption-evaporator K.
  • the absorption-evaporator K is added and the refrigerant vapor channel is connected to the absorber 3.
  • the concentrated solution of the steam separation chamber 17 enters the new absorption-evaporator K through the second solution pump 14, the third solution heat exchanger 15 and the new solution heat exchanger B, and absorbs the absorption from the first evaporator 6.
  • the refrigerant vapor is exothermic to the refrigerant liquid flowing through the new absorption-evaporator, and the dilute solution of the absorption-evaporator is added to the new solution pump D, the new solution heat exchanger B and the second solution heat.
  • the exchanger 11 enters the second generator 2, and the concentrated solution of the second generator 2 enters the absorber 3 via the second solution heat exchanger 11, absorbs the refrigerant vapor from the newly added absorption-evaporator K, and radiates heat to be heated.
  • the medium; the refrigerant liquid of the first evaporator 6 is divided into two paths - the first path absorbs the residual heat into the refrigerant vapor and is supplied to the newly added absorption-evaporator K, and the second path is pressurized by the newly added refrigerant liquid pump L. Then, a new type of absorption-evaporator K, an endothermic refrigerant vapor is supplied to the absorber 3 to form a single-effect-recovery type 1.
  • the fifth-class third-class absorption heat pump is realized as follows:
  • the new solution heat exchanger, the new absorption-evaporator and the newly added refrigerant liquid pump are added, and the absorber 3 has a dilute solution line.
  • the third solution heat exchanger 15 and the absorption-generator 16 are connected to the steam distribution chamber 17 to be adjusted so that the absorber 3 has a dilute solution line and is connected to the new absorption-evaporator via the new solution heat exchanger, and newly absorbed.
  • the second solution pump 14 has a concentrated solution line through the third solution heat exchanger 15 Connected with the second solution heat exchanger 11 to adjust the second solution pump 14 to have a concentrated solution line connected to the second solution heat exchanger 11 via the third solution heat exchanger 15 and the new solution heat exchanger
  • the second The evaporator 19 has a refrigerant vapor passage connected to the absorber 3 to be adjusted so that the second evaporator 19 has a refrigerant vapor passage connected to the newly added absorption-evaporator, and the second evaporator 19 adds a refrigerant liquid line through the newly added cold. Adding absorption-evaporation after the agent liquid pump L is connected to the new absorption-evaporator Further ⁇ refrigerant vapor passage 3 communicating with the absorber.
  • the dilute solution of the absorber 3 is passed through a new solution heat exchanger to enter a new absorption-evaporator ⁇ , absorbing the refrigerant vapor from the second evaporator 19 and radiating heat through the new absorption-evaporator
  • the cold refrigerant liquid of the crucible, the dilute solution of the absorption-evaporator ⁇ is added to the absorption-generator 16 through the third solution heat exchanger 15, and the endothermic portion is vaporized into the separation chamber 17, and the concentration of the separation chamber 17 is concentrated.
  • Class 5 absorption heat pump Provided to form a single-effect-recovery type 1. Class 5 absorption heat pump.
  • the fifth-class third-class absorption heat pump is realized as follows:
  • the new absorption-evaporator K and the dilute solution pipeline are connected to the absorber 3 via the new solution pump D and the new solution heat exchanger B, and the second evaporator 19 has a refrigerant vapor passage connected to the absorber 3 to adjust
  • the second evaporator 19 has a refrigerant vapor passage communicating with the newly added absorption-evaporator K
  • the third condenser 18 adds a refrigerant liquid pipeline through the newly added refrigerant liquid pump L to communicate with the newly added absorption-evaporator K.
  • a new absorption-evaporator K is added and a refrigerant vapor passage is connected to the absorber 3.
  • the concentrated solution of the second generator 2 enters the new absorption-evaporator K through the second solution heat exchanger 11 and the new solution heat exchanger B, absorbs the refrigerant vapor from the second evaporator 19, and discharges
  • the hot liquid flows through the new absorption-evaporator ,, and the dilute solution of the new absorption-evaporator ⁇ is added to the absorber through the new solution pump D and the new solution heat exchanger, and the absorption is from the new absorption.
  • the refrigerant liquid of the third condenser 18 is split into two paths - the first passage is pressurized by the second refrigerant liquid pump 20 into the second evaporator 19, The second pass is pressurized by a new refrigerant liquid pump L and then flows through a new absorption-evaporator ⁇ , which absorbs heat into a refrigerant vapor and supplies it to the absorber 3 to form a single-effect-recovery type 1.
  • Class 5 third-class absorption heat pump is realized like this -
  • the two solution heat exchanger 11 is in communication, and the second evaporator 19 has a refrigerant vapor passage connected to the absorber 3 to be adjusted to be a second evaporator 19 having a refrigerant vapor passage communicating with the newly added absorption-evaporator, the second evaporator 19 Adding a refrigerant liquid pipeline is connected with the new absorption-evaporator by adding a new refrigerant liquid pump L, and then adding an absorption-evaporator, and then a refrigerant vapor passage is connected to the absorber 3.
  • the concentrated solution of the steam separation chamber 17 passes through the second solution pump 14, the third solution heat exchanger 15 and the newly added solution heat exchanger ⁇ into the new absorption-evaporator! ⁇
  • the heat exchanger B and the second solution heat exchanger 11 enter the second generator 2, and the concentrated solution of the second generator 2 enters the absorber 3 through the second solution heat exchanger 11 to absorb the absorption from the new absorption-evaporator K.
  • the refrigerant vapor is exothermic to the heated medium; the refrigerant liquid of the second evaporator 19 is divided into two paths - the first passage absorbs the residual heat into the refrigerant vapor and supplies it to the newly added absorption-evaporator K, and the second passage is new
  • the fifth-stage absorption heat pump is a single-effect-recovery type 1. Class 5 third-stage absorption heat pump. The refrigerant is pumped through the new absorption-evaporator K and the heat-absorbing refrigerant vapor is supplied to the absorber 3. .
  • the fifth-class third-class absorption heat pump is realized as follows:
  • the first solution heat exchanger 10 is connected to the first generator 1 to be adjusted to be an absorption-generator 16 having a dilute solution line connected to the new absorption-evaporator via the first solution heat exchanger 10, and newly absorbed-
  • the evaporator ⁇ and the dilute solution line are connected to the first generator 1 via the new solution heat exchanger, and the first generator 1 has a concentrated solution line through the first solution pump 7 and the first solution heat exchanger 10 Connected to the absorption-generator 16 to adjust to the first generator 1 having a concentrated solution line connected to the absorption-generator 16 via the first solution pump 7, the new solution heat exchanger, and the first solution heat exchanger 10,
  • the first evaporator 6 has a refrigerant vapor passage connected to the absorption-generator 16 to be adjusted so that the first evaporator 6 has a refrigerant vapor passage communicating with the newly added absorption-evaporator, and the first condenser 4 is provided with a refrigerant liquid pipeline.
  • the concentrated solution of the first generator 1 is introduced into the absorption-generator 16 via the newly added solution heat exchanger ⁇ and the first solution heat exchanger 10, and the refrigerant vapor from the newly added absorption-evaporator is absorbed and discharged. Hot to the solution flowing through the absorption-generator 16
  • the dilute solution of the absorption-generator 16 enters the new absorption-evaporator K via the first solution heat exchanger 10, absorbs the refrigerant vapor from the first evaporator 6, and radiates heat through the new absorption-evaporator K.
  • the refrigerant liquid, the dilute solution of the new absorption-evaporator K is added to the first generator 1 through the new solution heat exchanger B; the refrigerant liquid of the first condenser 4 is divided into two paths - the first pass through the first cold
  • the liquid medium pump 8 is pressurized into the first evaporator 6, absorbs waste heat into refrigerant vapor and is supplied to the newly added absorption-evaporator K, and the second passage is pressurized by the newly added refrigerant liquid pump L, and then flows through the newly absorbed -
  • the third type of absorption heat pump of the fifth stage is formed by the evaporator K, the endothermic refrigerant vapor, and supplied to the absorption-generator 16.
  • the fifth-stage type III absorption heat pump is implemented as follows:
  • the concentrated solution of the first generator 1 enters the new absorption-evaporator ⁇ via the first solution pump 7 and the first solution heat exchanger 10, absorbs the refrigerant vapor from the first evaporator 6, and radiates heat.
  • Flow through the new absorption-evaporator ⁇ coolant solution add the absorption-evaporator ⁇ dilute solution through the new solution pump D and the new solution heat exchanger ⁇ into the absorption-generator 16 and absorb from the new absorption - the refrigerant vapor of the evaporator ⁇ and exothermic to the solution flowing through the absorption-generator 16, the dilute solution of the absorption-generator 16 is passed through the new solution heat exchanger ⁇ and the first solution heat exchanger 10 into the first occurrence
  • the refrigerant liquid of the first condenser 4 is divided into two paths - the first passage is pressurized by the first refrigerant liquid pump 8 into the first evaporator 6, and the residual heat is absorbed into the refrigerant vapor
  • the proposed third type of absorption heat pump enriches the third type of absorption heat pump which is used for the first stage of the solution and the high temperature drive heat for the second stage of the solution, which can better realize the heat pump supply. The match between heat and user needs.
  • the proposed third type of absorption heat pump when the temperature difference between the driving heat medium and the heated medium is large, is beneficial to play the role of high temperature driving heat or reduce the temperature requirement for high temperature driving heat.
  • the residual heat temperature can be further improved when the waste heat resources are abundant, especially when there is abundant waste heat resources mainly based on latent heat.

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Abstract

Disclosed in the present invention is a third-type absorption heat pump which pertains to the field of heat pump. A single-effect, double-effect, or multi-effect high-temperature generation process of solution is formed by adding other components comprising a generator, a throttle and a solution heat exchanger to a single-effect-single-effect third-type absorption heat pump with low-temperature waste heat being used during a first-phase generation process of solution and with high-temperature drive heat being used during a second-phase generation process of solution, in view of the temperature difference between high-temperature drive heat and heated medium; and a single-effect, double-effect, multi-effect, 1.5-stage and regenerative single-effect, regenerative double-effect, regenerative multi-effect, or regenerative 1.5-stage low-temperature generation process of solution is formed by adding other components including a new-added generator, a new-added throttle, and a new-added solution heat exchanger to the single-effect-single-effect third-type absorption heat pump, in view of the temperature difference between waste heat medium and cooling medium, thus a series of third-type absorption heat pumps are obtained.

Description

第三类吸收式热泵 技术领域：  The third type of absorption heat pump Technical field:
本发明属于低温余热利用热泵技术领域。  The invention belongs to the technical field of low temperature waste heat utilization heat pump.
背景技术： Background technique:
对于低温余热用于溶液第一阶段发生过程、 高温驱动热用于溶液第二阶段发生过程的第 三类吸收式热泵来说， 仅有单效 -单效第三类吸收式热泵是远远不够的， 不能有效满足或是无 法满足实际需求。 从热能高效利用的角度看， 高温驱动热与被加热介质之间的温差大小， 对 应着溶液高温发生过程的单效、 双效和多效； 考虑到余热资源参数与数量的多样性， 以及余 热与冷却介质之间的温差大小， 对应着溶液低温发生过程的单效、 双效、 多效、 1. 5 级和回 热式单效、 回热式双效、 回热式多效、 回热式 1. 5级； 再加上两方面的相结合， 得到系列第 三类吸收式热泵。  For the third type of absorption heat pump in which the low temperature waste heat is used in the first stage of the solution and the high temperature drive heat is used in the second stage of the solution, only the single effect-single effect third type absorption heat pump is not enough. , can not effectively meet or can not meet the actual needs. From the perspective of efficient use of thermal energy, the temperature difference between the high-temperature driving heat and the heated medium corresponds to the single-effect, double-effect and multi-effect of the solution high-temperature generation process; taking into account the diversity of parameters and quantities of waste heat resources, and waste heat The temperature difference between the cooling medium and the cooling medium corresponds to the single-effect, double-effect, multi-effect, 1.5-level and regenerative single-effect, regenerative double-effect, regenerative multi-effect and regenerative heat generation process. Equation 1. Level 5; combined with the combination of the two aspects, the series of the third type of absorption heat pump is obtained.
发明内容： Summary of the invention:
本发明的主要目的是提供第三类吸收式热泵， 具体发明内容分项阐述如下：  The main object of the present invention is to provide a third type of absorption heat pump, and the specific contents of the invention are as follows:
1. 第三类吸收式热泵， 是在由第一发生器、 第二发生器、 吸收器、 第一冷凝器、 第二 冷凝器、 蒸发器、 溶液泵、 冷剂液泵、 节流阀、 第一溶液热交换器和第二溶液热交换器组成 ——第一发生器有浓溶液管路经溶液泵、 第一溶液热交换器和第二溶液热交换器与第二发生 器连通， 第二发生器还有浓溶液管路经第二溶液热交换器与吸收器连通， 吸收器还有稀溶液 管路经第一溶液热交换器与第一发生器连通， 第一发生器还有冷剂蒸汽通道与第一冷凝器连 通， 第一冷凝器还有冷剂液管路经冷剂液泵与蒸发器连通， 第二发生器还有冷剂蒸汽通道与 第二冷凝器连通， 第二冷凝器还有冷剂液管路经节流阀与蒸发器连通， 蒸发器还有冷剂蒸汽 通道与吸收器连通， 第一发生器和蒸发器还分别有余热介质管路与外部连通， 第二发生器还 有驱动热介质管路与外部连通， 吸收器和第二冷凝器还分别有被加热介质管路与外部连通， 第一冷凝器还有冷却介质管路与外部连通——的单效-单效第三类吸收式热泵中，增加第三发 生器、 第二吸收器、 第二溶液泵和第三溶液热交换器， 将吸收器有稀溶液管路经第一溶液热 交换器与第一发生器连通调整为吸收器有稀溶液管路经第一溶液热交换器与第二吸收器连 通， 第二吸收器还有稀溶液管路经第二溶液泵和第三溶液热交换器与第一发生器连通， 将第 一发生器有浓溶液管路经第一溶液泵、 第一溶液热交换器和第二溶液热交换器与第二发生器 连通调整为第一发生器有浓溶液管路经第三溶液热交换器与第三发生器连通， 第三发生器还 有浓溶液管路经第一溶液泵、 第一溶液热交换器和第二溶液热交换器与第二发生器连通， 第 三发生器还分别有冷剂蒸汽通道与第二吸收器连通和有余热介质管路与外部连通， 第二吸收 器还有冷却介质管路与外部连通， 形成单效-回热式单效第三类吸收式热泵。  1. The third type of absorption heat pump is composed of a first generator, a second generator, an absorber, a first condenser, a second condenser, an evaporator, a solution pump, a refrigerant pump, a throttle valve, a first solution heat exchanger and a second solution heat exchanger - the first generator has a concentrated solution line connected to the second generator via the solution pump, the first solution heat exchanger and the second solution heat exchanger, The second generator further has a concentrated solution line connected to the absorber via the second solution heat exchanger, and the absorber and the dilute solution line are connected to the first generator via the first solution heat exchanger, and the first generator is also cold The refrigerant vapor passage is in communication with the first condenser, the first condenser and the refrigerant liquid pipeline are connected to the evaporator via the refrigerant liquid pump, and the second generator and the refrigerant vapor passage are connected to the second condenser, the second The condenser and the refrigerant liquid pipeline are connected to the evaporator via a throttle valve, and the evaporator and the refrigerant vapor passage are connected to the absorber, and the first generator and the evaporator respectively have a residual heat medium pipeline connected to the outside, The second generator also has a driving heat medium tube The road is connected to the outside, and the absorber and the second condenser are respectively connected to the outside by the heated medium pipeline, and the first condenser and the cooling medium pipeline are connected to the outside - single-effect-single-effect third-type absorption type In the heat pump, a third generator, a second absorber, a second solution pump and a third solution heat exchanger are added, and the absorber has a dilute solution line connected to the first generator via the first solution heat exchanger to be adjusted to absorb The dilute solution line is connected to the second absorber via the first solution heat exchanger, and the second absorber and the dilute solution line are connected to the first generator via the second solution pump and the third solution heat exchanger, The first generator has a concentrated solution pipeline connected to the second generator via the first solution pump, the first solution heat exchanger and the second solution heat exchanger to adjust the first generator to have a concentrated solution pipeline through the third solution heat The exchanger is in communication with the third generator, and the third generator further has a concentrated solution line connected to the second generator via the first solution pump, the first solution heat exchanger and the second solution heat exchanger, and the third generator further There are refrigerant vapor channels and The second absorber communicates with the residual heat medium line to communicate with the outside, and the second absorber and the cooling medium line communicate with the outside to form a single-effect-recovery single-effect third-type absorption heat pump.
2. 第三类吸收式热泵， 是在第 1项所提及的单效-单效第三类吸收式热泵中， 增加第二 溶液泵、 第三溶液热交换器、 吸收-发生器、 分汽室、 第三冷凝器、 第二蒸发器、 第二冷剂液 泵和第三冷剂液泵， 将吸收器有稀溶液管路经第一溶液热交换器与第一发生器连通调整为吸 收器有稀溶液管路经第三溶液热交换器与吸收-发生器连通， 吸收 -发生器还有稀溶液管路经 第一溶液热交换器与第一发生器连通， 将第一发生器有浓溶液管路经第一溶液泵、 第一溶液 热交换器和第二溶液热交换器与第二发生器连通调整为第一发生器有浓溶液管路经第一溶液 泵、 第一溶液热交换器和吸收-发生器与分汽室连通， 分汽室还有浓溶液管路经第二溶液泵、 第三溶液热交换器和第二溶液热交换器与第二发生器连通，吸收-发生器或还有被加热介质管 路与外部连通， 分汽室还有冷剂蒸汽通道与第三冷凝器连通， 第三冷凝器还有冷剂液管路经 第二冷剂液泵与第二蒸发器连通， 第一冷凝器增设冷剂液管路经第三冷剂液泵与第二蒸发器 连通， 第二蒸发器还有冷剂蒸汽通道与吸收-发生器连通， 第三冷凝器还有冷却介质管路与外 部连通，第二蒸发器还有余热介质管路与外部连通，形成单效 -回热式单效第三类吸收式热泵; 其中， 吸收-发生器无被加热介质管路与外部连通时， 可取消第一冷凝器经第三冷剂液泵与第 二蒸发器连通的冷剂液管路。 2. The third type of absorption heat pump is a single-effect-single-effect third-class absorption heat pump mentioned in item 1, adding a second solution pump, a third solution heat exchanger, an absorption-generator, and a minute a steam chamber, a third condenser, a second evaporator, a second refrigerant liquid pump and a third refrigerant liquid pump, wherein the absorber has a dilute solution line connected to the first generator via the first solution heat exchanger to be adjusted to The absorber has a dilute solution line connected to the absorption-generator via the third solution heat exchanger, and the absorption-generator and the dilute solution line are connected to the first generator via the first solution heat exchanger, and the first generator is The concentrated solution pipeline is connected to the second generator through the first solution pump, the first solution heat exchanger and the second solution heat exchanger to adjust the first generator to have a concentrated solution pipeline through the first solution pump, the first solution The heat exchanger and the absorption-generator are connected to the steam distribution chamber, and the steam distribution chamber and the concentrated solution pipeline are passed through the second solution pump, The third solution heat exchanger and the second solution heat exchanger are in communication with the second generator, the absorption-generator or the heated medium line is in communication with the outside, and the steam separation chamber has a refrigerant vapor passage and a third condenser Connected, the third condenser and the refrigerant liquid pipeline are connected to the second evaporator via the second refrigerant liquid pump, and the first condenser adds the refrigerant liquid pipeline to communicate with the second evaporator via the third refrigerant liquid pump The second evaporator has a refrigerant vapor passage communicating with the absorption-generator, the third condenser and the cooling medium conduit are in communication with the outside, and the second evaporator and the waste heat medium conduit are connected to the outside to form a single effect - A regenerative single-effect third-class absorption heat pump; wherein, when the absorption-generator is not connected to the outside by the heating medium pipeline, the cold connection between the first condenser and the second evaporator via the third refrigerant liquid pump may be cancelled Liquid line.
3. 第三类吸收式热泵， 是在第 1项所提及的单效-单效第三类吸收式热泵中， 增加第二 溶液泵、 第三溶液热交换器、 吸收-发生器、 分汽室、 第三冷凝器、 第二冷剂液泵和第三溶液 泵， 将吸收器有稀溶液管路经第一溶液热交换器与第一发生器连通调整为吸收器有稀溶液管 路经第三溶液泵和第三溶液热交换器与吸收-发生器连通， 吸收-发生器还有稀溶液管路经第 一溶液热交换器与第一发生器连通， 将第一发生器有浓溶液管路经第一溶液泵、 第一溶液热 交换器和第二溶液热交换器与第二发生器连通调整为第一发生器有浓溶液管路经第一溶液 泵、 第一溶液热交换器和吸收-发生器与分汽室连通， 分汽室还有浓溶液管路经第二溶液泵、 第三溶液热交换器和第二溶液热交换器与第二发生器连通，吸收-发生器或还有被加热介质管 路与外部连通， 分汽室还有冷剂蒸汽通道与第三冷凝器连通， 第三冷凝器还有冷剂液管路经 第二冷剂液泵与蒸发器连通， 蒸发器增设冷剂蒸汽通道与吸收-发生器连通， 第三冷凝器还有 冷却介质管路与外部连通， 形成单效 -回热式单效第三类吸收式热泵。  3. The third type of absorption heat pump is a single-effect-single-effect third-type absorption heat pump mentioned in the first item, adding a second solution pump, a third solution heat exchanger, an absorption-generator, and a minute a steam chamber, a third condenser, a second refrigerant liquid pump and a third solution pump, wherein the absorber has a dilute solution line connected to the first generator through the first solution heat exchanger to adjust the absorber to a dilute solution line The third solution pump and the third solution heat exchanger are in communication with the absorption-generator, and the absorption-generator and the dilute solution line are connected to the first generator via the first solution heat exchanger, and the first generator is rich The solution line is connected to the second generator via the first solution pump, the first solution heat exchanger and the second solution heat exchanger to adjust the first generator to have a concentrated solution line through the first solution pump, the first solution heat exchange And the absorption-generator is connected to the steam distribution chamber, and the steam distribution chamber and the concentrated solution pipeline are connected to the second generator via the second solution pump, the third solution heat exchanger and the second solution heat exchanger, and the absorption-occurrence occurs. Or a medium to be heated to communicate with the outside, The refrigerant vapor passage is connected to the third condenser, and the third condenser and the refrigerant liquid pipeline are connected to the evaporator via the second refrigerant liquid pump, and the evaporator adds a refrigerant vapor passage to communicate with the absorption-generator. The third condenser also has a cooling medium line communicating with the outside to form a single-effect-recovery single-effect third-type absorption heat pump.
4. 第三类吸收式热泵， 是在第 1项所提及的单效-单效第三类吸收式热泵中， 增加第二 溶液泵、 第三溶液热交换器、 吸收-发生器、 分汽室、 第三冷凝器、 第二蒸发器、 第二冷剂液 泵或第二节流阀， 将第一发生器有浓溶液管路经第一溶液泵、 第一溶液热交换器和第二溶液 热交换器与第二发生器连通调整为第一发生器有浓溶液管路经第一溶液泵和第一溶液热交换 器与吸收-发生器连通，吸收-发生器还有稀溶液管路经第一溶液热交换器与第一发生器连通， 将吸收器有稀溶液管路经第一溶液热交换器与第一发生器连通调整为吸收器有稀溶液管路经 第三溶液热交换器和吸收-发生器与分汽室连通， 分汽室还有浓溶液管路经第二溶液泵、第三 溶液热交换器和第二溶液热交换器与第二发生器连通， 将第一冷凝器有冷剂液管路经第一冷 剂液泵与第一蒸发器连通调整为第一冷凝器有冷剂液管路经第一冷剂液泵与第二蒸发器连 通， 第二蒸发器还有冷剂蒸汽通道与吸收-发生器连通， 分汽室还有冷剂蒸汽通道与第三冷凝 器连通， 第三冷凝器还有冷剂液管路经第二冷剂液泵与第一蒸发器连通、 或第三冷凝器还有 冷剂液管路经第二节流阀与第一冷凝器连通， 吸收 -发生器或还有被加热介质管路与外部连 通， 第三冷凝器还有冷却介质管路与外部连通， 第二蒸发器还有余热介质管路与外部连通， 形成单效 -回热式单效第三类吸收式热泵； 其中， ①无第二蒸发器时， 第一冷凝器有冷剂液管 路经第一冷剂液泵与第一蒸发器连通， 第一蒸发器增设冷剂蒸汽通道与吸收-发生器连通； ② 无第三冷凝器时， 分汽室有冷剂蒸汽通道与第一冷凝器连通， 第一冷凝器增设冷剂液管路经 第二冷剂液泵与第一蒸发器连通。  4. The third type of absorption heat pump is a single-effect-single-effect third-type absorption heat pump mentioned in the first item, adding a second solution pump, a third solution heat exchanger, an absorption-generator, and a minute a steam chamber, a third condenser, a second evaporator, a second refrigerant liquid pump or a second throttle valve, the first generator has a concentrated solution pipeline through the first solution pump, the first solution heat exchanger and the first The two solution heat exchanger is connected to the second generator to be adjusted to be a first generator having a concentrated solution line connected to the absorption-generator via the first solution pump and the first solution heat exchanger, and the absorption-generator and the dilute solution tube Passing through the first solution heat exchanger to communicate with the first generator, and connecting the absorber with the dilute solution line through the first solution heat exchanger to the first generator to adjust the absorber to have a dilute solution line through the third solution heat The exchanger and the absorption-generator are connected to the steam distribution chamber, and the steam distribution chamber and the concentrated solution pipeline are connected to the second generator via the second solution pump, the third solution heat exchanger and the second solution heat exchanger, a condenser has a refrigerant liquid pipeline through the first refrigerant liquid pump and the first evaporation The communication is adjusted to be that the first condenser has a refrigerant liquid pipeline connected to the second evaporator via the first refrigerant liquid pump, the second evaporator has a refrigerant vapor passage connected to the absorption-generator, and the steam separation chamber is also cooled. The vapor channel of the agent is in communication with the third condenser, the third condenser and the coolant liquid pipeline are connected to the first evaporator via the second refrigerant liquid pump, or the third condenser and the refrigerant liquid pipeline are passed through the second The throttle valve is in communication with the first condenser, the absorption-generator or the heated medium line is in communication with the outside, the third condenser and the cooling medium line are in communication with the outside, and the second evaporator has a residual heat medium conduit Connected with the outside to form a single-effect-recovery single-effect third-class absorption heat pump; wherein, 1 without the second evaporator, the first condenser has a refrigerant liquid pipeline through the first refrigerant liquid pump and the first The evaporator is connected, the first evaporator adds a refrigerant vapor channel to communicate with the absorption-generator; 2 when there is no third condenser, the steam distribution chamber has a refrigerant vapor passage communicating with the first condenser, and the first condenser is provided with a refrigerant The liquid pipeline is connected to the first evaporator via the second refrigerant liquid pump
5. 第三类吸收式热泵， 是在第 1项所提及的单效-单效第三类吸收式热泵中， 增加第三 发生器、 第三溶液热交换器和第二节流阀， 第一发生器经第一溶液泵和第一溶液热交换器之 后增设浓溶液管路并再经第三溶液热交换器与第三发生器连通， 第三发生器还有浓溶液管路 经第三溶液热交换器与吸收器连通， 将第二发生器有冷剂蒸汽通道与第二冷凝器连通调整为 第二发生器有冷剂蒸汽通道与第三发生器连通后第三发生器再有冷剂液管路经第二节流阔与 第二冷凝器连通——第二发生器产生的冷剂蒸汽作为第三发生器的驱动热介质， 第三发生器 还有冷剂蒸汽通道与第二冷凝器连通， 形成双效 -单效第三类吸收式热泵。 5. The third type of absorption heat pump is a single-effect-single-effect third-type absorption heat pump mentioned in item 1, adding a third generator, a third solution heat exchanger and a second throttle valve, The first generator is further provided with a concentrated solution pipeline after the first solution pump and the first solution heat exchanger, and is further connected to the third generator via the third solution heat exchanger, and the third generator further has a concentrated solution pipeline The three-solution heat exchanger is in communication with the absorber, and the second generator has a refrigerant vapor passage connected to the second condenser to be adjusted to be a second generator having a refrigerant vapor passage connected to the third generator, and then the third generator is further The refrigerant liquid pipeline is widened in the second section The second condenser is connected - the refrigerant vapor generated by the second generator is used as the driving heat medium of the third generator, and the third generator and the refrigerant vapor passage are connected with the second condenser to form a double effect-single effect Three types of absorption heat pumps.
6. 第三类吸收式热泵， 是在第 1项所提及的单效-单效第三类吸收式热泵中， 增加第三 发生器、 第三溶液热交换器和第二节流阀， 将第一发生器有浓溶液管路经溶液泵、 第一溶液 热交换器和第二溶液热交换器与第二发生器连通调整为第一发生器有浓溶液管路经溶液泵、 第一溶液热交换器、 第二溶液热交换器和第三溶液热交换器与第二发生器连通， 将第二发生 器有浓溶液管路经第二溶液热交换器与吸收器连通调整为第二发生器有浓溶液管路经第三溶 液热交换器与第三发生器连通， 第三发生器还有浓溶液管路经第二溶液热交换器与吸收器连 通， 将第二发生器有冷剂蒸汽通道与第二冷凝器连通调整为第二发生器有冷剂蒸汽通道与第 三发生器连通后第三发生器再有冷剂液管路经第二节流阀与第二冷凝器连通——第二发生器 产生的冷剂蒸汽作为第三发生器的驱动热介质， 第三发生器还有冷剂蒸汽通道与第二冷凝器 连通， 形成双效-单效第三类吸收式热泵。  6. The third type of absorption heat pump is a single-effect-single-effect third-type absorption heat pump mentioned in item 1, adding a third generator, a third solution heat exchanger and a second throttle valve, The first generator has a concentrated solution pipeline connected to the second generator via the solution pump, the first solution heat exchanger and the second solution heat exchanger to adjust the first generator to have a concentrated solution pipeline through the solution pump, first The solution heat exchanger, the second solution heat exchanger and the third solution heat exchanger are in communication with the second generator, and the second generator has a concentrated solution line connected to the absorber via the second solution heat exchanger to be adjusted to the second The generator has a concentrated solution pipeline connected to the third generator via the third solution heat exchanger, and the third generator and the concentrated solution pipeline communicate with the absorber via the second solution heat exchanger, and the second generator is cooled The refrigerant vapor passage is connected to the second condenser to be adjusted to be the second generator having the refrigerant vapor passage communicating with the third generator, and the third generator and the refrigerant liquid pipeline are connected to the second condenser via the second throttle valve - the refrigerant vapor produced by the second generator as the first Driving the heat medium generator, a third generator, the refrigerant vapor channel communicating with the second condenser to form a double effect - a third single effect absorption heat pump.
7. 第三类吸收式热泵， 是在第 6项所述的第三类吸收式热泵中， 增加溶液节流阀， 将 第一发生器有浓溶液管路经第一溶液泵、 第一溶液热交换器、 第二溶液热交换器和第三溶液 热交换器与第二发生器连通调整为第一发生器有浓溶液管路经第一溶液泵、 第一溶液热交换 器、 第二溶液热交换器之后分别再经溶液节流阀与第三发生器连通和再经第三溶液热交换器 与第二发生器连通， 形成双效 -单效第三类吸收式热泵。  7. The third type of absorption heat pump is a third type of absorption heat pump according to item 6, wherein the solution throttle valve is added, and the first generator has a concentrated solution line through the first solution pump and the first solution. The heat exchanger, the second solution heat exchanger and the third solution heat exchanger are connected to the second generator to be adjusted to have a first solution having a concentrated solution line through the first solution pump, the first solution heat exchanger, and the second solution The heat exchanger is then connected to the third generator via the solution throttle valve and then communicated with the second generator via the third solution heat exchanger to form a double-effect-single-effect third-type absorption heat pump.
8. 第三类吸收式热泵， 是在第 1项所提及的单效-单效第三类吸收式热泵中， 增加第三 发生器、 第三溶液热交换器、 第二溶液泵和第二节流阀， 将第一发生器有浓溶液管路经第一 溶液泵、 第一溶液热交换器和第二溶液热交换器与第二发生器连通调整为第一发生器有浓溶 液管路经第一溶液泵、 第一溶液热交换器和第二溶液热交换器与第三发生器连通， 第三发生 器还有浓溶液管路经第二溶液泵和第三溶液热交换器与第二发生器连通， 将第二发生器有浓 溶液管路经第二溶液热交换器与吸收器连通调整为第二发生器有浓溶液管路经第三溶液热交 换器和第二溶液热交换器与吸收器连通， 将第二发生器有冷剂蒸汽通道与第二冷凝器连通调 整为第二发生器有冷剂蒸汽通道与第三发生器连通后第三发生器再有冷剂液管路经第二节流 阀与第二冷凝器连通——第二发生器产生的冷剂蒸汽作为第三发生器的驱动热介质， 第三发 生器还有冷剂蒸汽通道与第二冷凝器连通， 形成双效 -单效第三类吸收式热泵。  8. The third type of absorption heat pump is a single-effect-single-effect third-type absorption heat pump mentioned in item 1, adding a third generator, a third solution heat exchanger, a second solution pump, and a a two-throttle valve, the first generator has a concentrated solution pipeline connected to the second generator through the first solution pump, the first solution heat exchanger and the second solution heat exchanger to adjust the first generator to have a concentrated solution tube The first solution pump, the first solution heat exchanger and the second solution heat exchanger are in communication with the third generator, and the third generator further has a concentrated solution line through the second solution pump and the third solution heat exchanger The second generator is connected, and the second generator has a concentrated solution pipeline connected to the absorber through the second solution heat exchanger to adjust the second generator to have a concentrated solution pipeline through the third solution heat exchanger and the second solution heat The exchanger is in communication with the absorber, the second generator has a refrigerant vapor passage connected to the second condenser, and the second generator has a refrigerant vapor passage connected to the third generator, and the third generator has a refrigerant liquid The pipeline is connected to the second condenser via the second throttle valve - A second refrigerant vapor generator as the driving medium of the third heat generator, a third generator, the refrigerant vapor channel communicating with the second condenser to form a double effect - a third single effect absorption heat pump.
9. 第三类吸收式热泵， 是在第 8项所述的第三类吸收式热泵中， 增加溶液节流阔， 将 第一发生器有浓溶液管路经第一溶液泵、 第一溶液热交换器和第二溶液热交换器与第三发生 器连通调整为第一发生器有浓溶液管路经第一溶液泵、 第一溶液热交换器和第二溶液热交换 器之后分别直接与第二发生器连通和再经溶液节流阀与第三发生器连通，形成双效-单效第三 类吸收式热泵。  9. The third type of absorption heat pump is a third type of absorption heat pump according to item 8, which increases the throttle section of the solution, and the first generator has a concentrated solution pipeline through the first solution pump and the first solution. The heat exchanger and the second solution heat exchanger are connected to the third generator to be adjusted so that the first generator has a concentrated solution line directly after passing through the first solution pump, the first solution heat exchanger and the second solution heat exchanger The second generator is in communication and is again in communication with the third generator via the solution throttle to form a double-effect single-effect third type absorption heat pump.
10. 第三类吸收式热泵， 是在第 5项所述的第三类吸收式热泵中， 增加第四发生器、 第 四溶液热交换器和第三节流阀， 第一溶液热交换器增设浓溶液管路经第四溶液热交换器与第 四发生器连通， 第四发生器还有浓溶液管路经第四溶液热交换器与吸收器连通， 将第三发生 器有冷剂蒸汽通道与第二冷凝器连通调整为第三发生器有冷剂蒸汽通道与第四发生器连通后 第四发生器再有冷剂液管路经第三节流阀与第二冷凝器连通， 第四发生器还有冷剂蒸汽通道 与第二冷凝器连通， 形成三效 -单效第三类吸收式热泵。  10. The third type of absorption heat pump, in the third type of absorption heat pump according to item 5, adding a fourth generator, a fourth solution heat exchanger and a third throttle valve, the first solution heat exchanger The concentrated solution line is connected to the fourth generator via the fourth solution heat exchanger, and the fourth generator and the concentrated solution line are connected to the absorber via the fourth solution heat exchanger, and the third generator has refrigerant vapor. The passage is connected to the second condenser to be adjusted to be a third generator having a refrigerant vapor passage communicating with the fourth generator, and then the fourth generator is further connected to the second condenser via the third throttle valve, The four generators also have a refrigerant vapor passage communicating with the second condenser to form a three-effect-single-effect third-type absorption heat pump.
11. 第三类吸收式热泵， 是在第 6项所述的第三类吸收式热泵中， 增加第四发生器、 第 四溶液热交换器和第三节流阀， 将第二溶液热交换器有浓溶液管路经第三溶液热交换器与第 二发生器连通调整为第二溶液热交换器有浓溶液管路经第四溶液热交换器和第三溶液热交换 器与第二发生器连通， 将第三发生器有浓溶液管路经第二溶液热交换器与吸收器连通调整为 第三发生器有浓溶液管路经第第四溶液热交换器与第四发生器连通， 第四发生器还有浓溶液 管路经第二溶液热交换器与吸收器连通， 将第三发生器有冷剂蒸汽通道与第二冷凝器连通调 整为第三发生器有冷剂蒸汽通道与第四发生器连通后第四发生器再有冷剂液管路经第三节流 阀与第二冷凝器连通， 第四发生器还有冷剂蒸汽通道与第二冷凝器连通， 形成三效-单效第三 类吸收式热泵。 11. The third type of absorption heat pump is a third type of absorption heat pump according to item 6, wherein the fourth generator, the fourth solution heat exchanger and the third throttle valve are added, and the second solution is heat exchanged. The machine has a concentrated solution pipeline through the third solution heat exchanger and the first The second generator is connected to the second solution heat exchanger, and the concentrated solution pipeline is connected to the second generator via the fourth solution heat exchanger and the third solution heat exchanger, and the third generator has a concentrated solution pipeline. The two solution heat exchanger is connected to the absorber to be adjusted so that the third generator has a concentrated solution line connected to the fourth generator via the fourth solution heat exchanger, and the fourth generator has a concentrated solution line through the second solution heat The exchanger is in communication with the absorber, and the third generator has a refrigerant vapor passage communicating with the second condenser to be adjusted to a third generator having a refrigerant vapor passage communicating with the fourth generator, the fourth generator having a refrigerant liquid The pipeline is connected to the second condenser via a third throttle valve, and the fourth generator has a refrigerant vapor passage communicating with the second condenser to form a three-effect-single-effect third-type absorption heat pump.
12. 第三类吸收式热泵， 是在第 8项所述的第三类吸收式热泵中， 增加第四发生器、 第 四溶液热交换器、 第三节流阀和第三溶液泵， 将第二溶液热交换器有浓溶液管路与第三发生 器连通调整为第二溶液热交换器有浓溶液管路与第四发生器连通， 第四发生器还有浓溶液管 路经第三溶液泵和第四溶液热交换器与第三发生器连通， 将第二发生器有浓溶液管路经第三 溶液热交换器和第二溶液热交换器与吸收器连通调整为第二发生器有浓溶液管路经第三溶液 热交换器、 第四溶液热交换器和第二溶液热交换器与吸收器连通， 将第三发生器有冷剂蒸汽 通道与第二冷凝器连通调整为第三发生器有冷剂蒸汽通道与第四发生器连通后第四发生器再 有冷剂液管路经第三节流阀与第二冷凝器连通， 第四发生器还有冷剂蒸汽通道与第二冷凝器 连通， 形成三效 -单效第三类吸收式热泵。  12. The third type of absorption heat pump is a third type of absorption heat pump according to item 8, adding a fourth generator, a fourth solution heat exchanger, a third throttle valve and a third solution pump, The second solution heat exchanger has a concentrated solution line connected to the third generator and is adjusted to be a second solution heat exchanger having a concentrated solution line connected to the fourth generator, and the fourth generator has a concentrated solution line through the third The solution pump and the fourth solution heat exchanger are in communication with the third generator, and the second generator has a concentrated solution line connected to the absorber via the third solution heat exchanger and the second solution heat exchanger to be adjusted to the second generator The concentrated solution pipeline communicates with the absorber through the third solution heat exchanger, the fourth solution heat exchanger and the second solution heat exchanger, and the third generator has a refrigerant vapor passage connected to the second condenser to be adjusted to The third generator has a refrigerant vapor passage connected to the fourth generator, and the fourth generator further has a refrigerant liquid pipeline connected to the second condenser via the third throttle valve, and the fourth generator further has a refrigerant vapor passage and The second condenser is connected to form a three-effect-single effect Three absorption heat pump.
13. 第三类吸收式热泵， 是在第 1项所述的第三类吸收式热泵中， 增加第四发生器、 第 四溶液热交换器和第二节流阀， 第一发生器经第一溶液泵和第一溶液热交换器之后增设浓溶 液管路并再经第四溶液热交换器与第四发生器连通， 第四发生器还有浓溶液管路经第四溶液 热交换器与吸收器连通， 将第二发生器有冷剂蒸汽通道与第二冷凝器连通调整为第二发生器 有冷剂蒸汽通道与第四发生器连通后第四发生器再有冷剂液管路经第二节流阀与第二冷凝器 连通——第二发生器产生的冷剂蒸汽作为第四发生器的驱动热介质， 第四发生器还有冷剂蒸 汽通道与第二冷凝器连通， 形成双效 -回热式单效第三类吸收式热泵。  13. The third type of absorption heat pump is the third type of absorption heat pump according to the first item, wherein the fourth generator, the fourth solution heat exchanger and the second throttle valve are added, the first generator a solution pump and a first solution heat exchanger are further provided with a concentrated solution line and then communicated with the fourth generator via the fourth solution heat exchanger, and the fourth generator further has a concentrated solution line through the fourth solution heat exchanger and The absorber is connected to communicate the second generator with the refrigerant vapor passage and the second condenser, and the second generator has a refrigerant vapor passage connected with the fourth generator, and then the fourth generator has a refrigerant liquid pipeline The second throttle valve is in communication with the second condenser - the refrigerant vapor generated by the second generator acts as a driving heat medium for the fourth generator, and the fourth generator and the refrigerant vapor passage communicate with the second condenser to form Double-effect-recovery single-effect third-class absorption heat pump.
14. 第三类吸收式热泵， 是在第 1项所述第三类吸收式热泵中， 增加第四发生器、 第四 溶液热交换器和第二节流阀， 将第一发生器有浓溶液管路经第一溶液泵、 第一溶液热交换器 和第二溶液热交换器与第二发生器连通调整为第一发生器有浓溶液管路经第一溶液泵、 第一 溶液热交换器、 第二溶液热交换器和第四溶液热交换器与第二发生器连通， 将第二发生器有 浓溶液管路经第二溶液热交换器与吸收器连通调整为第二发生器有浓溶液管路经第四溶液热 交换器与第四发生器连通， 第四发生器还有浓溶液管路经第二溶液热交换器与吸收器连通， 将第二发生器有冷剂蒸汽通道与第二冷凝器连通调整为第二发生器有冷剂蒸汽通道与第四发 生器连通后第四发生器再有冷剂液管路经第二节流阔与第二冷凝器连通——第二发生器产生 的冷剂蒸汽作为第四发生器的驱动热介质，第四发生器还有冷剂蒸汽通道与第二冷凝器连通， 形成双效 -回热式单效第三类吸收式热泵。  14. The third type of absorption heat pump, in the third type of absorption heat pump according to item 1, adds a fourth generator, a fourth solution heat exchanger and a second throttle valve, and the first generator has a rich The solution line is connected to the second generator via the first solution pump, the first solution heat exchanger and the second solution heat exchanger to adjust the first generator to have a concentrated solution line through the first solution pump, the first solution heat exchange The second solution heat exchanger and the fourth solution heat exchanger are in communication with the second generator, and the second generator has a concentrated solution line connected to the absorber via the second solution heat exchanger to be adjusted to have a second generator The concentrated solution pipeline is connected to the fourth generator via the fourth solution heat exchanger, and the fourth generator and the concentrated solution pipeline are connected to the absorber via the second solution heat exchanger, and the second generator has a refrigerant vapor passage The second condenser is connected to the second condenser, and the second generator has a refrigerant vapor passage communicating with the fourth generator, and then the fourth generator is further connected to the second condenser through the second throttle. The refrigerant vapor produced by the second generator is used as the fourth hair Driver's heat medium, a fourth generator, the refrigerant vapor channel communicating with the second condenser to form a double effect - a third heat recovery single effect absorption heat pump.
15. 第三类吸收式热泵， 是在第 14项所述的第三类吸收式热泵中， 增加溶液节流阀， 将第一发生器有浓溶液管路经第一溶液泵、 第一溶液热交换器、 第二溶液热交换器和第四溶 液热交换器与第二发生器连通调整为第一发生器有浓溶液管路经第一溶液泵、 第一溶液热交 换器、 第二溶液热交换器之后分别再经溶液节流阀与第四发生器连通和再经第四溶液热交换 器与第二发生器连通， 形成双效 -回热式单效第三类吸收式热泵。  15. The third type of absorption heat pump is the third type of absorption heat pump according to item 14, wherein the solution throttle valve is added, and the first generator has a concentrated solution line through the first solution pump and the first solution. The heat exchanger, the second solution heat exchanger and the fourth solution heat exchanger are connected to the second generator to be adjusted to have a first solution having a concentrated solution line through the first solution pump, the first solution heat exchanger, and the second solution The heat exchanger is then connected to the fourth generator via the solution throttle valve and then communicated with the second generator via the fourth solution heat exchanger to form a double-effect-recovery single-effect third-type absorption heat pump.
16. 第三类吸收式热泵， 是在第 1项所述的第三类吸收式热泵中， 增加第四发生器、 第 四溶液热交换器、 第二节流阔和第三溶液泵， 将第一发生器有浓溶液管路经第一溶液泵、 第 一溶液热交换器和第二溶液热交换器与第二发生器连通调整为第一发生器有浓溶液管路经第 一溶液泵、 第一溶液热交换器和第二溶液热交换器与第四发生器连通， 第四发生器还有浓溶 液管路经第三溶液泵和第四溶液热交换器与第二发生器连通， 将第二发生器有浓溶液管路经 第二溶液热交换器与吸收器连通调整为第二发生器有浓溶液管路经第四溶液热交换器和第二 溶液热交换器与吸收器连通， 将第二发生器有冷剂蒸汽通道与第二冷凝器连通调整为第二发 生器有冷剂蒸汽通道与第四发生器连通后第四发生器再有冷剂液管路经第二节流阀与第二冷 凝器连通——第二发生器产生的冷剂蒸汽作为第四发生器的驱动热介质， 第四发生器还有冷 剂蒸汽通道与第二冷凝器连通， 形成双效 -回热式单效第三类吸收式热泵。 16. The third type of absorption heat pump is a third type of absorption heat pump according to item 1, adding a fourth generator, a fourth solution heat exchanger, a second section flow and a third solution pump, The first generator has a concentrated solution line through the first solution pump, the first a solution heat exchanger and a second solution heat exchanger are connected to the second generator to be adjusted to have a first solution having a concentrated solution line through the first solution pump, the first solution heat exchanger and the second solution heat exchanger and The fourth generator is connected, the fourth generator has a concentrated solution pipeline connected to the second generator via the third solution pump and the fourth solution heat exchanger, and the second generator has a concentrated solution pipeline through the second solution for heat exchange The second generator has a concentrated solution line connected to the absorber through the fourth solution heat exchanger and the second solution heat exchanger, and the second generator has a refrigerant vapor channel and a second condenser The communication is adjusted so that the second generator has a refrigerant vapor passage communicating with the fourth generator, and the fourth generator is further connected to the second condenser via the second throttle valve - the second generator generates The refrigerant vapor is used as the driving heat medium of the fourth generator, and the fourth generator also has a refrigerant vapor passage communicating with the second condenser to form a double-effect-recovery single-effect third-type absorption heat pump.
17. 第三类吸收式热泵， 是在第 16项所述的第三类吸收式热泵中， 增加溶液节流阔， 将第一发生器有浓溶液管路经第一溶液泵、 第一溶液热交换器和第二溶液热交换器与第四发 生器连通调整为第一发生器有浓溶液管路经第一溶液泵、 第一溶液热交换器和第二溶液热交 换器之后分别直接与第二发生器连通和再经溶液节流阀与第四发生器连通，形成双效-单效第 三类吸收式热泵。  17. The third type of absorption heat pump is a third type of absorption heat pump according to item 16, which increases the throttle section of the solution, and the first generator has a concentrated solution pipeline through the first solution pump and the first solution. The heat exchanger and the second solution heat exchanger are connected to the fourth generator to be adjusted so that the first generator has a concentrated solution line directly after passing through the first solution pump, the first solution heat exchanger and the second solution heat exchanger The second generator is in communication and reconnected via the solution throttle valve to the fourth generator to form a double effect-single effect third type absorption heat pump.
18. 第三类吸收式热泵， 是在第 13项所述的第三类吸收式热泵中， 增加第五发生器、 第三节流阀和第五溶液热交换器， 第一溶液热交换器增设浓溶液管路经第五溶液热交换器与 第五发生器连通， 第五发生器还有浓溶液管路经第五溶液热交换器与吸收器连通， 将第四发 生器有冷剂蒸汽通道与第二冷凝器连通调整为第四发生器有冷剂蒸汽通道与第五发生器连通 后第五发生器再有冷剂液管路经第三节流阀与第二冷凝器连通， 第五发生器还有冷剂蒸汽通 道与第二冷凝器连通， 形成三效 -回热式单效第三类吸收式热泵。  18. The third type of absorption heat pump, in the third type of absorption heat pump according to item 13, adding a fifth generator, a third throttle valve and a fifth solution heat exchanger, the first solution heat exchanger The concentrated solution line is connected to the fifth generator via the fifth solution heat exchanger, and the fifth generator and the concentrated solution line are connected to the absorber via the fifth solution heat exchanger, and the fourth generator has refrigerant vapor. The passage is connected to the second condenser to be adjusted to be the fourth generator having the refrigerant vapor passage communicating with the fifth generator, and then the fifth generator is further connected to the second condenser via the third throttle valve, The five generators also have a refrigerant vapor passage communicating with the second condenser to form a three-effect-recovery single-effect third-type absorption heat pump.
19. 第三类吸收式热泵， 是在第 14项所述的第三类吸收式热泵中， 增加第五发生器、 第三节流阔和第五溶液热交换器， 将第二溶液热交换器有浓溶液管路经第四溶液热交换器与 第二发生器连通调整为第二溶液热交换器有浓溶液管路经第五溶液热交换器和第四溶液热交 换器与第二发生器连通， 将第四发生器有浓溶液管路经第二溶液热交换器与吸收器连通调整 为第四发生器有浓溶液管路经第第五溶液热交换器与第五发生器连通， 第五发生器还有浓溶 液管路经第二溶液热交换器与吸收器连通， 将第四发生器有冷剂蒸汽通道与第二冷凝器连通 调整为第四发生器有冷剂蒸汽通道与第五发生器连通后第五发生器再有冷剂液管路经第三节 流阀与第二冷凝器连通， 第五发生器还有冷剂蒸汽通道与第二冷凝器连通， 形成三效-回热式 单效第三类吸收式热泵。  19. The third type of absorption heat pump is a third type of absorption heat pump according to item 14, wherein the fifth generator, the third section of the flow and the fifth solution heat exchanger are added, and the second solution is heat exchanged. The concentrated solution line is connected to the second generator via the fourth solution heat exchanger to be adjusted to the second solution heat exchanger, and the concentrated solution line is passed through the fifth solution heat exchanger and the fourth solution heat exchanger and the second occurrence Connected to the fourth generator having a concentrated solution line connected to the absorber via the second solution heat exchanger to be adjusted to a fourth generator having a concentrated solution line connected to the fifth generator via the fifth solution heat exchanger, The fifth generator further has a concentrated solution pipeline connected to the absorber via the second solution heat exchanger, and the fourth generator has a refrigerant vapor passage communicating with the second condenser to adjust the fourth generator to have a refrigerant vapor passage and After the fifth generator is connected, the fifth generator further has a refrigerant liquid pipeline connected to the second condenser via the third throttle valve, and the fifth generator further has a refrigerant vapor passage communicating with the second condenser to form a three-effect - Regenerative single-effect third-class absorption heat pump.
20. 第三类吸收式热泵， 是在第 16项所述的第三类吸收式热泵中， 增加第五发生器、 第三节流阀、 第四溶液泵和第五溶液热交换器， 将第二溶液热交换器有浓溶液管路与第四发 生器连通调整为第二溶液热交换器有浓溶液管路与第五发生器连通， 第五发生器还有浓溶液 管路经第四溶液泵和第五溶液热交换器与第四发生器连通， 将第二发生器有浓溶液管路经第 四溶液热交换器和第二溶液热交换器与吸收器连通调整为第二发生器有浓溶液管路经第四溶 液热交换器、 第五溶液热交换器和第二溶液热交换器与吸收器连通， 将第四发生器有冷剂蒸 汽通道与第二冷凝器连通调整为第四发生器有冷剂蒸汽通道与第五发生器连通后第五发生器 再有冷剂液管路经第三节流阔与第二冷凝器连通， 第五发生器还有冷剂蒸汽通道与第二冷凝 器连通， 形成三效 -回热式单效第三类吸收式热泵。  20. The third type of absorption heat pump is a third type of absorption heat pump according to item 16, wherein the fifth generator, the third throttle valve, the fourth solution pump and the fifth solution heat exchanger are added, The second solution heat exchanger has a concentrated solution line connected to the fourth generator and is adjusted to be a second solution heat exchanger having a concentrated solution line connected to the fifth generator, and the fifth generator and the concentrated solution line are passed through a fourth The solution pump and the fifth solution heat exchanger are in communication with the fourth generator, and the second generator has a concentrated solution line connected to the absorber via the fourth solution heat exchanger and the second solution heat exchanger to be adjusted to the second generator The concentrated solution pipeline is connected to the absorber through the fourth solution heat exchanger, the fifth solution heat exchanger and the second solution heat exchanger, and the fourth generator has a refrigerant vapor passage connected to the second condenser to be adjusted to The fourth generator has a refrigerant vapor passage connected to the fifth generator, and the fifth generator has a refrigerant liquid pipeline connected to the second condenser through the third section, and the fifth generator has a refrigerant vapor passage and The second condenser is connected to form a three-effect heat The third single effect absorption heat pump.
21. 第三类吸收式热泵， 是在第 2-3项内任一一项所述的第三类吸收式热泵中， 增加第 三发生器、 第四溶液热交换器和第二节流阀， 第二溶液泵经第三溶液热交换器增设浓溶液管 路并再经第四溶液热交换器与第三发生器连通， 第三发生器还有浓溶液管路经第四溶液热交 换器与吸收器连通， 将第二发生器有冷剂蒸汽通道与第二冷凝器连通调整为第二发生器有冷 剂蒸汽通道与第三发生器连通后第三发生器再有冷剂液管路经第二节流阀与第二冷凝器连通 ——第二发生器产生的冷剂蒸汽作为第三发生器的驱动热介质， 第三发生器还有冷剂蒸汽通 道与第二冷凝器连通， 形成双效-回热式单效第三类吸收式热泵。 A third type of absorption heat pump, in the third type of absorption heat pump according to any one of items 2-3, wherein the third generator, the fourth solution heat exchanger and the second throttle valve are added The second solution pump is connected with the concentrated solution pipeline through the third solution heat exchanger and is further connected to the third generator via the fourth solution heat exchanger, and the third generator and the concentrated solution pipeline are further heated by the fourth solution. The converter is in communication with the absorber, and the second generator has a refrigerant vapor passage communicating with the second condenser to adjust the second generator to have a refrigerant vapor passage communicating with the third generator, and the third generator is further provided with a refrigerant liquid The pipeline is connected to the second condenser via the second throttle valve - the refrigerant vapor generated by the second generator acts as a driving heat medium for the third generator, and the third generator also has a refrigerant vapor passage and a second condenser Connected to form a double-effect-recovery single-effect third-class absorption heat pump.
22. 第三类吸收式热泵， 是在第 2-3项内任一一项所述的第三类吸收式热泵中， 增加第 三发生器、 第四溶液热交换器和第二节流阀， 将第二溶液泵有浓溶液管路经第三溶液热交换 器和第二溶液热交换器与第二发生器连通调整为第二溶液泵有浓溶液管路经第三溶液热交换 器、 第二溶液热交换器和第四溶液热交换器与第二发生器连通， 将第二发生器有浓溶液管路 经第二溶液热交换器与吸收器连通调整为第二发生器有浓溶液管路经第四溶液热交换器与第 三发生器连通， 第三发生器还有浓溶液管路经第二溶液热交换器与吸收器连通， 将第二发生 器有冷剂蒸汽通道与第二冷凝器连通调整为第二发生器有冷剂蒸汽通道与第三发生器连通后 第三发生器再有冷剂液管路经第二节流阀与第二冷凝器连通——第一发生器产生的冷剂蒸汽 作为第三发生器的驱动热介质， 第三发生器还有冷剂蒸汽通道与第二冷凝器连通， 形成双效- 回热式单效第三类吸收式热泵。  22. A third type of absorption heat pump, in the third type of absorption heat pump according to any one of items 2-3, wherein the third generator, the fourth solution heat exchanger and the second throttle valve are added And the second solution pump has a concentrated solution pipeline connected to the second generator through the third solution heat exchanger and the second solution heat exchanger to adjust to a second solution pump having a concentrated solution pipeline through the third solution heat exchanger, The second solution heat exchanger and the fourth solution heat exchanger are in communication with the second generator, and the second generator has a concentrated solution line connected to the absorber via the second solution heat exchanger to adjust the second generator to have a concentrated solution The pipeline is connected to the third generator via the fourth solution heat exchanger, and the third generator and the concentrated solution pipeline are connected to the absorber via the second solution heat exchanger, and the second generator has a refrigerant vapor passage and a second The second condenser is connected to adjust to the second generator having the refrigerant vapor passage communicating with the third generator, and then the third generator is further connected to the second condenser via the second throttle valve - the first occurrence The refrigerant vapor generated by the device acts as the driving heat of the third generator Quality, third generator, the refrigerant vapor passage communicates with the second condenser to form a double effect - a third heat recovery single effect absorption heat pump.
23. 第三类吸收式热泵， 是在第 22项所述的第三类吸收式热泵中， 增加溶液节流阀， 将第二溶液泵有浓溶液管路经第三溶液热交换器、 第二溶液热交换器和第四溶液热交换器与 第二发生器连通调整为第二溶液泵有浓溶液管路经第三溶液热交换器、 第二溶液热交换器之 后分别再经溶液节流阔与第三发生器连通和再经第四溶液热交换器与第二发生器连通， 形成 双效-回热式单效第三类吸收式热泵。  23. The third type of absorption heat pump is the third type of absorption heat pump according to item 22, wherein the solution throttle valve is added, and the second solution pump has a concentrated solution line through the third solution heat exchanger, The two solution heat exchanger and the fourth solution heat exchanger are connected to the second generator to be adjusted to be the second solution pump. The concentrated solution line is passed through the third solution heat exchanger and the second solution heat exchanger, and then the solution is throttled separately. The broadband is connected to the third generator and communicated with the second generator via the fourth solution heat exchanger to form a double-effect-recovery single-effect third-type absorption heat pump.
24. 第三类吸收式热泵， 是在第 2-3项内任一一项所述的第三类吸收式热泵中， 增加第 三发生器、 第四溶液热交换器、 第二节流阀、 第三溶液泵或第四溶液泵， 将第二溶液泵有浓 溶液管路经第三溶液热交换器和第二溶液热交换器与第二发生器连通调整为第二溶液泵有浓 溶液管路经第三溶液热交换器和第二溶液热交换器与第三发生器连通， 第三发生器还有浓溶 液管路经第三溶液泵或第四溶液泵、 第四溶液热交换器与第二发生器连通， 将第二发生器有 浓溶液管路经第二溶液热交换器与吸收器连通调整为第二发生器有浓溶液管路经第四溶液热 交换器和第二溶液热交换器与吸收器连通， 将第二发生器有冷剂蒸汽通道与第二冷凝器连通 调整为第二发生器有冷剂蒸汽通道与第三发生器连通后第三发生器再有冷剂液管路经第二节 流阀与第二冷凝器连通——第二发生器产生的冷剂蒸汽作为第三发生器的驱动热介质， 第三 发生器还有冷剂蒸汽通道与第二冷凝器连通， 形成双效 -回热式单效第三类吸收式热泵。  A third type of absorption heat pump, which is the third type of absorption heat pump according to any one of items 2-3, wherein the third generator, the fourth solution heat exchanger, and the second throttle valve are added a third solution pump or a fourth solution pump, wherein the second solution pump has a concentrated solution line connected to the second generator via the third solution heat exchanger and the second solution heat exchanger to adjust to a second solution pump having a concentrated solution The pipeline is connected to the third generator via the third solution heat exchanger and the second solution heat exchanger, and the third generator has a concentrated solution pipeline via the third solution pump or the fourth solution pump, the fourth solution heat exchanger Connected with the second generator, the second generator has a concentrated solution line connected to the absorber through the second solution heat exchanger, and the second generator has a concentrated solution line through the fourth solution heat exchanger and the second solution The heat exchanger is in communication with the absorber, and the second generator has a refrigerant vapor passage communicating with the second condenser to adjust the second generator to have a refrigerant vapor passage communicating with the third generator, and the third generator is further provided with a refrigerant The liquid pipeline is connected to the second condenser via the second throttle valve - the refrigerant vapor generated by the second generator acts as a driving heat medium for the third generator, and the third generator also has a refrigerant vapor passage communicating with the second condenser to form a double effect-recovery type single effect third type absorption Heat pump.
25. 第三类吸收式热泵， 是在第 24项所述的第三类吸收式热泵中， 增加溶液节流阀， 将第二溶液泵有浓溶液管路经第三溶液热交换器和第二溶液热交换器与第三发生器连通调整 为第二溶液泵有浓溶液管路经第三溶液热交换器和第二溶液热交换器之后分别直接与第二发 生器连通和再经溶液节流阀与第三发生器连通， 形成双效-回热式单效第三类吸收式热泵。  25. The third type of absorption heat pump is the third type of absorption heat pump according to item 24, wherein the solution throttle valve is added, and the second solution pump has a concentrated solution line through the third solution heat exchanger and the first The two solution heat exchanger is connected to the third generator to be adjusted to be the second solution pump. The concentrated solution line is directly connected to the second generator and then passed through the solution section after passing through the third solution heat exchanger and the second solution heat exchanger. The flow valve is in communication with the third generator to form a double-effect regenerative single-effect third-class absorption heat pump.
26. 第三类吸收式热泵， 是在第 21项所述的第三类吸收式热泵中， 增加第四发生器、 第五溶液热交换器和第三节流阀， 第二溶液泵经第三溶液热交换器增设浓溶液管路并再经第 五溶液热交换器与第四发生器连通， 第四发生器还有浓溶液管路经第五溶液热交换器与吸收 器连通， 将第三发生器有冷剂蒸汽通道与第二冷凝器连通调整为第三发生器有冷剂蒸汽通道 与第四发生器连通后第四发生器再有冷剂液管路经第三节流阀与第二冷凝器连通， 第四发生 器还有冷剂蒸汽通道与第二冷凝器连通， 形成三效-回热式单效第三类吸收式热泵。  26. The third type of absorption heat pump is the third type of absorption heat pump according to item 21, wherein the fourth generator, the fifth solution heat exchanger and the third throttle valve are added, and the second solution pump is passed through The three-solution heat exchanger is further provided with a concentrated solution pipeline and is further connected to the fourth generator via the fifth solution heat exchanger, and the fourth generator and the concentrated solution pipeline are connected to the absorber through the fifth solution heat exchanger, and the first The third generator has a refrigerant vapor passage connected to the second condenser and is adjusted to be a third generator having a refrigerant vapor passage connected to the fourth generator, and the fourth generator is further provided with a refrigerant liquid pipeline via the third throttle valve The second condenser is connected, and the fourth generator further has a refrigerant vapor passage communicating with the second condenser to form a three-effect-recovery type single-effect third-type absorption heat pump.
27. 第三类吸收式热泵， 是在第 22项所述的第三类吸收式热泵中， 增加第四发生器、 第五溶液热交换器和第三节流阀， 将第二溶液泵有浓溶液管路经第三溶液热交换器、 第二溶 液热交换器和第四溶液热交换器与第二发生器连通调整为第二溶液泵有浓溶液管路经第三溶 液热交换器、第二溶液热交换器、第五溶液热交换器和第四溶液热交换器与第二发生器连通， 将第三发生器有浓溶液管路经第二溶液热交换器与吸收器连通调整为第三发生器有浓溶液管 路经第五溶液热交换器与第四发生器连通， 第四发生器还有浓溶液管路经第二溶液热交换器 与吸收器连通， 将第三发生器有冷剂蒸汽通道与第二冷凝器连通调整为第三发生器有冷剂蒸 汽通道与第四发生器连通后第四发生器再有冷剂液管路经第三节流阀与第二冷凝器连通， 第 四发生器还有冷剂蒸汽通道与第二冷凝器连通， 形成三效 -回热式单效第三类吸收式热泵。 27. The third type of absorption heat pump is a fourth type of absorption heat pump according to item 22, wherein the fourth generator is added. a fifth solution heat exchanger and a third throttle valve, the second solution pump having a concentrated solution line connected to the second generator via the third solution heat exchanger, the second solution heat exchanger, and the fourth solution heat exchanger Adjusting to the second solution pump, the concentrated solution line is connected to the second generator via the third solution heat exchanger, the second solution heat exchanger, the fifth solution heat exchanger and the fourth solution heat exchanger, and the third generation occurs The concentrated solution line is connected to the absorber through the second solution heat exchanger to be adjusted to be a third generator. The concentrated solution line is connected to the fourth generator via the fifth solution heat exchanger, and the fourth generator has a concentrated solution. The pipeline is connected to the absorber via the second solution heat exchanger, and the third generator has a refrigerant vapor passage connected to the second condenser to be adjusted to be a third generator having a refrigerant vapor passage connected to the fourth generator. The generator further has a refrigerant liquid pipeline connected to the second condenser via the third throttle valve, and the fourth generator further has a refrigerant vapor passage communicating with the second condenser to form a three-effect-recovery type single effect third. Absorption heat pump.
28. 第三类吸收式热泵， 是在第 24项所述的第三类吸收式热泵中， 增加第四发生器、 第五溶液热交换器、 第三节流阀、 第四溶液泵或第五溶液泵， 将第二溶液泵有浓溶液管路经 第三溶液热交换器和第二溶液热交换器与第三发生器连通调整为第二溶液泵有浓溶液管路经 第三溶液热交换器和第二溶液热交换器与第四发生器连通， 第四发生器还有浓溶液管路经第 四溶液泵或第五溶液泵、 第五溶液热交换器与第三发生器连通， 将第二发生器有浓溶液管路 经第四溶液热交换器和第二溶液热交换器与吸收器连通调整为第二发生器有浓溶液管路经第 四溶液热交换器、 第五溶液热交换器和第二溶液热交换器与吸收器连通， 将第三发生器有冷 剂蒸汽通道与第二冷凝器连通调整为第三发生器有冷剂蒸汽通道与第四发生器连通后第四发 生器再有冷剂液管路经第三节流阀与第二冷凝器连通， 第四发生器还有冷剂蒸汽通道与第二 冷凝器连通， 形成三效-回热式单效第三类吸收式热泵。  28. A third type of absorption heat pump, in the third type of absorption heat pump according to item 24, adding a fourth generator, a fifth solution heat exchanger, a third throttle valve, a fourth solution pump or a five-solution pump, the second solution pump has a concentrated solution pipeline connected to the third generator via the third solution heat exchanger and the second solution heat exchanger to adjust to a second solution pump having a concentrated solution pipeline through the third solution heat The exchanger and the second solution heat exchanger are in communication with the fourth generator, and the fourth generator and the concentrated solution line are connected to the third generator via the fourth solution pump or the fifth solution pump, and the fifth solution heat exchanger, The second generator has a concentrated solution pipeline connected to the absorber through the fourth solution heat exchanger and the second solution heat exchanger to adjust the second generator to have a concentrated solution pipeline through the fourth solution heat exchanger, the fifth solution The heat exchanger and the second solution heat exchanger are in communication with the absorber, and the third generator has a refrigerant vapor passage communicating with the second condenser to adjust the third generator to have a refrigerant vapor passage connected to the fourth generator. Four generators have a coolant line through the first The three throttle valve is in communication with the second condenser, and the fourth generator has a refrigerant vapor passage communicating with the second condenser to form a three-effect-recovery single-effect third-type absorption heat pump.
29. 第三类吸收式热泵， 是在第 4项所述的第三类吸收式热泵中， 增加第三发生器、 第 四溶液热交换器和第二节流阔， 第二溶液泵经第三溶液热交换器增设浓溶液管路并再经第四 溶液热交换器与第三发生器连通， 第三发生器还有浓溶液管路经第四溶液热交换器与吸收器 连通， 将第二发生器有冷剂蒸汽通道与第二冷凝器连通调整为第二发生器有冷剂蒸汽通道与 第三发生器连通后第三发生器再有冷剂液管路经第二节流阀与第二冷凝器连通——第二发生 器产生的冷剂蒸汽作为第三发生器的驱动热介质， 第三发生器还有冷剂蒸汽通道与第二冷凝 器连通， 形成双效 -回热式单效第三类吸收式热泵。  29. The third type of absorption heat pump is the third type of absorption heat pump according to item 4, wherein the third generator, the fourth solution heat exchanger and the second section are widened, and the second solution pump is passed through The three-solution heat exchanger is further provided with a concentrated solution pipeline and is further connected to the third generator via the fourth solution heat exchanger, and the third generator and the concentrated solution pipeline are connected to the absorber via the fourth solution heat exchanger, The second generator has a refrigerant vapor passage communicating with the second condenser to adjust the second generator to have a refrigerant vapor passage communicating with the third generator, and the third generator is further provided with a refrigerant liquid pipeline via the second throttle valve The second condenser is connected--the refrigerant vapor generated by the second generator is used as the driving heat medium of the third generator, and the third generator and the refrigerant vapor channel are connected with the second condenser to form a double-effect-recovery type Single-effect third-class absorption heat pump.
30. 第三类吸收式热泵， 是在第 4项所述的第三类吸收式热泵中， 增加第三发生器、 第 四溶液热交换器和第二节流阀， 将第二溶液泵有浓溶液管路经第三溶液热交换器和第二溶液 热交换器与第二发生器连通调整为第二溶液泵有浓溶液管路经第三溶液热交换器、 第二溶液 热交换器和第四溶液热交换器与第二发生器连通， 将第二发生器有浓溶液管路经第二溶液热 交换器与吸收器连通调整为第二发生器有浓溶液管路经第四溶液热交换器与第三发生器连 通， 第三发生器还有浓溶液管路经第二溶液热交换器与吸收器连通， 将第二发生器有冷剂蒸 汽通道与第二冷凝器连通调整为第二发生器有冷剂蒸汽通道与第三发生器连通后第三发生器 再有冷剂液管路经第二节流阔与第二冷凝器连通——第一发生器产生的冷剂蒸汽作为第三发 生器的驱动热介质， 第三发生器还有冷剂蒸汽通道与第二冷凝器连通， 形成双效-回热式单效 第三类吸收式热泵。  30. The third type of absorption heat pump is the third type of absorption heat pump according to item 4, wherein the third generator, the fourth solution heat exchanger and the second throttle valve are added, and the second solution pump is The concentrated solution pipeline is connected to the second generator via the third solution heat exchanger and the second solution heat exchanger to be adjusted to a second solution pump having a concentrated solution pipeline through the third solution heat exchanger, the second solution heat exchanger, and The fourth solution heat exchanger is in communication with the second generator, and the second generator has a concentrated solution line connected to the absorber via the second solution heat exchanger to adjust the second generator to have a concentrated solution line through the fourth solution heat The exchanger is connected to the third generator, the third generator and the concentrated solution pipeline are connected to the absorber via the second solution heat exchanger, and the second generator has a refrigerant vapor passage connected to the second condenser to be adjusted to The second generator has a refrigerant vapor passage connected to the third generator, and the third generator and the refrigerant liquid pipeline are connected to the second condenser via the second throttle flow - the refrigerant vapor generated by the first generator is used as Third generator driving heat medium, third A steam generator, the refrigerant passage communicates with the second condenser to form a double effect - a third heat recovery single effect absorption heat pump.
31. 第三类吸收式热泵， 是在第 30项所述的第三类吸收式热泵中， 增加溶液节流阀， 将第二溶液泵有浓溶液管路经第三溶液热交换器、 第二溶液热交换器和第四溶液热交换器与 第二发生器连通调整为第二溶液泵有浓溶液管路经第三溶液热交换器、 第二溶液热交换器之 后分别再经溶液节流阀与第三发生器连通和再经第四溶液热交换器与第二发生器连通， 形成 双效 -回热式单效第三类吸收式热泵。 32. 第三类吸收式热泵， 是在第 4项所述的第三类吸收式热泵中， 增加第三发生器、 第 四溶液热交换器、 第三溶液泵和第二节流阀， 将第二溶液泵有浓溶液管路经第三溶液热交换 器和第二溶液热交换器与第二发生器连通调整为第二溶液泵有浓溶液管路经第三溶液热交换 器和第二溶液热交换器与第三发生器连通， 第三发生器还有浓溶液管路经第三溶液泵和第四 溶液热交换器与第二发生器连通， 将第二发生器有浓溶液管路经第二溶液热交换器与吸收器 连通调整为第二发生器有浓溶液管路经第四溶液热交换器和第二溶液热交换器与吸收器连 通， 将第二发生器有冷剂蒸汽通道与第二冷凝器连通调整为第二发生器有冷剂蒸汽通道与第 三发生器连通后第三发生器再有冷剂液管路经第二节流阔与第二冷凝器连通——第二发生器 产生的冷剂蒸汽作为第三发生器的驱动热介质， 第三发生器还有冷剂蒸汽通道与第二冷凝器 连通， 形成双效 -回热式单效第三类吸收式热泵。 31. The third type of absorption heat pump is a third type of absorption heat pump according to item 30, wherein the solution throttle valve is added, and the second solution pump has a concentrated solution line through the third solution heat exchanger, The two solution heat exchanger and the fourth solution heat exchanger are connected to the second generator to be adjusted to be the second solution pump. The concentrated solution line is passed through the third solution heat exchanger and the second solution heat exchanger, and then the solution is throttled separately. The valve is in communication with the third generator and is in communication with the second generator via the fourth solution heat exchanger to form a double effect-recovery single effect third type absorption heat pump. 32. The third type of absorption heat pump, in the third type of absorption heat pump described in item 4, adds a third generator, a fourth solution heat exchanger, a third solution pump and a second throttle valve, The second solution pump has a concentrated solution line connected to the second generator via the third solution heat exchanger and the second solution heat exchanger to adjust to a second solution pump having a concentrated solution line through the third solution heat exchanger and the second The solution heat exchanger is in communication with the third generator, the third generator further has a concentrated solution line connected to the second generator via the third solution pump and the fourth solution heat exchanger, and the second generator has a concentrated solution line Passing through the second solution heat exchanger and the absorber to adjust to a second generator having a concentrated solution line communicating with the absorber via the fourth solution heat exchanger and the second solution heat exchanger, the second generator having a refrigerant vapor The passage is connected to the second condenser to be adjusted so that the second generator has a refrigerant vapor passage communicating with the third generator, and then the third generator and the refrigerant liquid pipeline are connected to the second condenser via the second throttle flow- The refrigerant vapor generated by the second generator is used as the third generator The heat medium is driven, and the third generator and the refrigerant vapor passage are connected with the second condenser to form a double-effect-recovery single-effect third-type absorption heat pump.
33. 第三类吸收式热泵， 是在第 32项所述的第三类吸收式热泵中， 增加溶液节流阀， 将第二溶液泵有浓溶液管路经第三溶液热交换器和第二溶液热交换器与第三发生器连通调整 为第二溶液泵有浓溶液管路经第三溶液热交换器和第二溶液热交换器之后分别直接与第二发 生器连通和再经溶液节流阀与第三发生器连通， 形成双效 -回热式单效第三类吸收式热泵。  33. The third type of absorption heat pump is a third type of absorption heat pump according to item 32, wherein the solution throttle valve is added, and the second solution pump has a concentrated solution line through the third solution heat exchanger and The two solution heat exchanger is connected to the third generator to be adjusted to be the second solution pump. The concentrated solution line is directly connected to the second generator and then passed through the solution section after passing through the third solution heat exchanger and the second solution heat exchanger. The flow valve is in communication with the third generator to form a double-effect regenerative single-effect third-class absorption heat pump.
34. 第三类吸收式热泵， 是在第 29项所述的第三类吸收式热泵中， 增加第四发生器、 第五溶液热交换器和第三节流阀， 第二溶液泵经第三溶液热交换器增设浓溶液管路并再经第 五溶液热交换器与第四发生器连通， 第四发生器还有浓溶液管路经第五溶液热交换器与吸收 器连通， 将第三发生器有冷剂蒸汽通道与第二冷凝器连通调整为第三发生器有冷剂蒸汽通道 与第四发生器连通后第四发生器再有冷剂液管路经第三节流阔与第二冷凝器连通， 第四发生 器还有冷剂蒸汽通道与第二冷凝器连通， 形成三效 -回热式单效第三类吸收式热泵。  34. The third type of absorption heat pump is the third type of absorption heat pump according to item 29, wherein the fourth generator, the fifth solution heat exchanger and the third throttle valve are added, and the second solution pump is passed through The three-solution heat exchanger is further provided with a concentrated solution pipeline and is further connected to the fourth generator via the fifth solution heat exchanger, and the fourth generator and the concentrated solution pipeline are connected to the absorber through the fifth solution heat exchanger, and the first The third generator has a refrigerant vapor passage communicating with the second condenser to adjust the third generator to have a refrigerant vapor passage communicating with the fourth generator, and then the fourth generator has a refrigerant liquid pipeline flowing through the third section The second condenser is connected, and the fourth generator further has a refrigerant vapor passage communicating with the second condenser to form a three-effect-recovery type single-effect third-type absorption heat pump.
35. 第三类吸收式热泵， 是在第 30项所述的第三类吸收式热泵中， 增加第四发生器、 第五溶液热交换器和第三节流闽， 将第二溶液泵有浓溶液管路经第三溶液热交换器、 第二溶 液热交换器和第四溶液热交换器与第二发生器连通调整为第二溶液泵有浓溶液管路经第三溶 液热交换器、第二溶液热交换器、第五溶液热交换器和第四溶液热交换器与第二发生器连通， 将第三发生器有浓溶液管路经第二溶液热交换器与吸收器连通调整为第三发生器有浓溶液管 路经第五溶液热交换器与第四发生器连通， 第四发生器还有浓溶液管路经第二溶液热交换器 与吸收器连通， 将第三发生器有冷剂蒸汽通道与第二冷凝器连通调整为第三发生器有冷剂蒸 汽通道与第四发生器连通后第四发生器再有冷剂液管路经第三节流阀与第二冷凝器连通， 第 四发生器还有冷剂蒸汽通道与第二冷凝器连通， 形成三效 -回热式单效第三类吸收式热泵。  35. The third type of absorption heat pump is the third type of absorption heat pump according to item 30, wherein the fourth generator, the fifth solution heat exchanger and the third throttle are added, and the second solution pump is The concentrated solution pipeline is connected to the second generator via the third solution heat exchanger, the second solution heat exchanger and the fourth solution heat exchanger to be adjusted to be a second solution pump having a concentrated solution pipeline through the third solution heat exchanger, The second solution heat exchanger, the fifth solution heat exchanger and the fourth solution heat exchanger are in communication with the second generator, and the third generator has a concentrated solution line connected to the absorber via the second solution heat exchanger to be adjusted to The third generator has a concentrated solution line communicating with the fourth generator via the fifth solution heat exchanger, and the fourth generator and the concentrated solution line are connected to the absorber via the second solution heat exchanger, and the third generator is The refrigerant vapor passage is connected to the second condenser to be adjusted to be a third generator having a refrigerant vapor passage communicating with the fourth generator, and then the fourth generator is further provided with a refrigerant liquid pipeline through the third throttle valve and the second condensation Connected, the fourth generator also has a refrigerant vapor pass The channel is connected to the second condenser to form a three-effect-recovery type single-effect third-type absorption heat pump.
36. 第三类吸收式热泵， 是在第 32项所述的第三类吸收式热泵中， 增加第四发生器、 第五溶液热交换器、 第三节流阀和第四溶液泵， 将第二溶液泵有浓溶液管路经第三溶液热交 换器和第二溶液热交换器与第三发生器连通调整为第二溶液泵有浓溶液管路经第三溶液热交 换器和第二溶液热交换器与第四发生器连通， 第四发生器还有浓溶液管路经第四溶液泵和第 五溶液热交换器与第三发生器连通， 将第二发生器有浓溶液管路经第四溶液热交换器和第二 溶液热交换器与吸收器连通调整为第二发生器有浓溶液管路经第四溶液热交换器、 第五溶液 热交换器和第二溶液热交换器与吸收器连通， 将第三发生器有冷剂蒸汽通道与第二冷凝器连 通调整为第三发生器有冷剂蒸汽通道与第四发生器连通后第四发生器再有冷剂液管路经第三 节流阀与第二冷凝器连通， 第四发生器还有冷剂蒸汽通道与第二冷凝器连通， 形成三效-回热 式单效第三类吸收式热泵。  36. The third type of absorption heat pump is a third type of absorption heat pump according to item 32, adding a fourth generator, a fifth solution heat exchanger, a third throttle valve and a fourth solution pump, The second solution pump has a concentrated solution pipeline connected to the third generator via the third solution heat exchanger and the second solution heat exchanger to adjust the second solution pump to have a concentrated solution pipeline through the third solution heat exchanger and the second The solution heat exchanger is in communication with the fourth generator, and the fourth generator further has a concentrated solution line connected to the third generator via the fourth solution pump and the fifth solution heat exchanger, and the second generator has a concentrated solution line The fourth solution heat exchanger and the second solution heat exchanger are connected to the absorber to be adjusted to have a second solution having a concentrated solution line through the fourth solution heat exchanger, the fifth solution heat exchanger and the second solution heat exchanger In communication with the absorber, the third generator has a refrigerant vapor passage communicating with the second condenser to be adjusted to a third generator having a refrigerant vapor passage communicating with the fourth generator, the fourth generator having a refrigerant liquid conduit Connected to the second condenser via the third throttle valve The fourth steam generator, the refrigerant passage communicates with the second condenser to form a three-way - a third heat recovery single effect absorption heat pump.
37. 第三类吸收式热泵， 是在第 1项所提及的单效-单效第三类吸收式热泵以及第 5-12 内任一第项所述的第三类吸收式热泵中， 增加新增发生器、 新增溶液热交换器、 新增节流阔 和新增溶液泵， 吸收器增设稀溶液管路经新增溶液热交换器与新增发生器连通， 新增发生器 还有浓溶液管路经新增溶液泵和新增溶液热交换器之后与第一发生器经溶液泵和第一溶液热 交换器之后的浓溶液管路汇合， 将第一发生器有冷剂蒸汽通道与第一冷凝器连通调整为第一 发生器有冷剂蒸汽通道与新增发生器连通后新增发生器再有冷剂液管路经新增节流阀与第一 冷凝器连通， 新增发生器还有冷剂蒸汽通道与第一冷凝器连通， 形成以双效为低温发生流程 的第三类吸收式热泵。 37. The third type of absorption heat pump is the single-effect single-effect type III absorption heat pump mentioned in item 1 and the 5-12 In the third type of absorption heat pump described in any of the above items, a new generator, a new solution heat exchanger, a new throttle and a new solution pump are added, and a diluent solution is added to the absorber. The solution heat exchanger is connected to the newly added generator, and the new generator and the concentrated solution pipeline are passed through the new solution pump and the newly added solution heat exchanger, and after the first generator is passed through the solution pump and the first solution heat exchanger. The concentrated solution pipeline meets, and the first generator has a refrigerant vapor passage connected to the first condenser to be adjusted to be a first generator having a refrigerant vapor passage connected with the newly added generator, and then adding a new generator and then a refrigerant liquid. The pipeline is connected to the first condenser via a new throttle valve, and a new generator and a refrigerant vapor passage are connected with the first condenser to form a third type of absorption heat pump with a double effect as a low temperature generation process.
38. 第三类吸收式热泵， 是在第 1项所提及的单效-单效第三类吸收式热泵以及第 5-12 内任一第项所述的第三类吸收式热泵中， 增加新增发生器、新增溶液热交换器和新增节流阀， 将第一发生器有浓溶液管路经溶液泵和第一溶液热交换器与第二溶液热交换器连通调整为第 一发生器有浓溶液管路经新增溶液热交换器与新增发生器连通， 新增发生器还有浓溶液管路 经溶液泵、 新增溶液热交换器和第一溶液热交换器与第二溶液热交换器连通， 将第一发生器 有冷剂蒸汽通道与第一冷凝器连通调整为第一发生器有冷剂蒸汽通道与新增发生器连通后新 增发生器再有冷剂液管路经新增节流阀与第一冷凝器连通， 新增发生器还有冷剂蒸汽通道与 第一冷凝器连通， 形成以双效为低温发生流程的第三类吸收式热泵。  38. The third type of absorption heat pump is the single-effect single-effect type III absorption heat pump mentioned in item 1 and the third type of absorption heat pump described in any of items 5-12. Adding a new generator, a new solution heat exchanger and a new throttle valve, and adjusting the first generator having a concentrated solution line through the solution pump and the first solution heat exchanger and the second solution heat exchanger to adjust A generator has a concentrated solution line connected to the newly added generator through the new solution heat exchanger, and the new generator has a concentrated solution line through the solution pump, the new solution heat exchanger and the first solution heat exchanger. The second solution heat exchanger is connected, and the first generator has a refrigerant vapor channel connected to the first condenser to be adjusted to be a first generator having a refrigerant vapor channel connected with the newly added generator, and then adding a generator and then a refrigerant The liquid pipeline is connected to the first condenser via a new throttle valve, and a new generator and a refrigerant vapor passage are connected with the first condenser to form a third type of absorption heat pump with a double effect as a low temperature generation process.
39. 第三类吸收式热泵， 是在第 1项所提及的单效-单效第三类吸收式热泵以及第 5-12 内任一第项所述的第三类吸收式热泵中， 增加新增发生器、 新增溶液热交换器、 新增节流阀 和新增溶液泵， 将吸收器有稀溶液管路经第一溶液热交换器与第一发生器连通调整为吸收器 有稀溶液管路经第一溶液热交换器和新增溶液热交换器与新增发生器连通， 新增发生器还有 浓溶液管路经新增溶液泵和新增溶液热交换器与第一发生器连通， 将第一发生器有冷剂蒸汽 通道与第一冷凝器连通调整为第一发生器有冷剂蒸汽通道与新增发生器连通后新增发生器再 有冷剂液管路经新增节流阀与第一冷凝器连通， 新增发生器还有冷剂蒸汽通道与第一冷凝器 连通， 形成以双效为低温发生流程的第三类吸收式热泵。  39. The third type of absorption heat pump is the single-effect single-effect type III absorption heat pump mentioned in item 1 and the third type absorption heat pump according to any of items 5-12. Add a new generator, a new solution heat exchanger, a new throttle valve and a new solution pump, and connect the absorber with a dilute solution line through the first solution heat exchanger to the first generator to adjust the absorber to have The dilute solution pipeline is connected to the newly added generator through the first solution heat exchanger and the new solution heat exchanger, and the new generator and the concentrated solution pipeline are added to the new solution pump and the newly added solution heat exchanger and the first The generator is connected, and the first generator has a refrigerant vapor passage connected to the first condenser to be adjusted to be a first generator having a refrigerant vapor passage connected with the newly added generator, and then adding a generator and then a refrigerant liquid pipeline A new throttle valve is connected to the first condenser, and a new generator and a refrigerant vapor passage are connected to the first condenser to form a third type of absorption heat pump with a double effect as a low temperature generation process.
40. 第三类吸收式热泵， 是在第 37项所述的第三类吸收式热泵中， 增加新增第二发生 器、 新增第二溶液热交换器、 新增第二节流阀和新增第二溶液泵， 吸收器增设稀溶液管路经 新增第二溶液热交换器与新增第二发生器连通， 新增第二发生器还有浓溶液管路经新增第二 溶液泵和新增第二溶液热交换器之后与第一发生器经溶液泵和第一溶液热交换器之后的浓溶 液管路汇合， 将新增第一发生器有冷剂蒸汽通道与第一冷凝器连通调整为新增第一发生器有 冷剂蒸汽通道与新增第二发生器连通后新增第二发生器再有冷剂液管路经新增第二节流阀与 第一冷凝器连通， 新增第二发生器还有冷剂蒸汽通道与第一冷凝器连通， 形成以三效为低温 发生流程的第三类吸收式热泵。  40. The third type of absorption heat pump, in the third type of absorption heat pump described in item 37, adds a new second generator, adds a second solution heat exchanger, adds a second throttle valve, and Adding a second solution pump, adding a dilute solution pipeline to the absorber, and adding a second solution heat exchanger to connect with the newly added second generator, adding a second generator and a concentrated solution pipeline to add a second solution After the pump and the newly added second solution heat exchanger are merged with the first generator through the solution pump and the concentrated solution line after the first solution heat exchanger, the first first generator has a refrigerant vapor channel and the first condensation The communication is adjusted to add a first generator with a refrigerant vapor channel and a new second generator is connected, a second generator is added, and a refrigerant liquid pipeline is added through the second throttle valve and the first condenser. Connected, a new second generator and a refrigerant vapor passage are connected to the first condenser to form a third type of absorption heat pump with a three-effect low temperature generation process.
41. 第三类吸收式热泵， 是在第 38项所述的第三类吸收式热泵中， 增加新增第二发生 器、 新增第二溶液热交换器和新增第二节流阔， 将新增第一发生器有浓溶液管路经溶液泵、 新增第一溶液热交换器和第一溶液热交换器与第二溶液热交换器连通调整为新增第一发生器 有浓溶液管路经新增第二溶液热交换器与新增第二发生器连通， 新增第二发生器还有浓溶液 管路经溶液泵、 新增第二溶液热交换器、 新增第一溶液热交换器和第一溶液热交换器与第二 溶液热交换器连通， 将新增第一发生器有冷剂蒸汽通道与第一冷凝器连通调整为新增第一发 生器有冷剂蒸汽通道与新增第二发生器连通后新增第二发生器再有冷剂液管路经新增第二节 流阀与第一冷凝器连通， 新增第二发生器还有冷剂蒸汽通道与第一冷凝器连通， 形成以三效 为低温发生流程的第三类吸收式热泵。 42. 第三类吸收式热泵， 是在第 39项所述的第三类吸收式热泵中， 增加新增第二发生 器、 新增第二溶液热交换器、 新增第二节流阀和新增第二溶液泵， 将吸收器有稀溶液管路经 第一溶液热交换器和新增第一溶液热交换器与新增第一发生器连通调整为吸收器有稀溶液管 路经第一溶液热交换器、 新增第一溶液热交换器和新增第二溶液热交换器与新增第二发生器 连通， 新增第二发生器还有浓溶液管路经新增第二溶液泵和新增第二溶液热交换器与新增第 一发生器连通， 将新增第一发生器有冷剂蒸汽通道与第一冷凝器连通调整为新增第一发生器 有冷剂蒸汽通道与新增第二发生器连通后新增第二发生器再有冷剂液管路经新增第二节流阀 与第一冷凝器连通， 新增第二发生器还有冷剂蒸汽通道与第一冷凝器连通， 形成以三效为低 温发生流程的第三类吸收式热泵。 41. The third type of absorption heat pump is a third type of absorption heat pump according to item 38, adding a new second generator, adding a second solution heat exchanger and adding a second section of the flow. Adding a first generator with a concentrated solution pipeline through a solution pump, adding a first solution heat exchanger, and a first solution heat exchanger to the second solution heat exchanger to adjust to a new first generator having a concentrated solution The pipeline is connected with the newly added second generator through the newly added second solution heat exchanger, and the second generator and the concentrated solution pipeline are added through the solution pump, the second solution heat exchanger is added, and the first solution is added. The heat exchanger and the first solution heat exchanger are in communication with the second solution heat exchanger, and the newly added first generator has a refrigerant vapor passage connected to the first condenser to be adjusted to add a first generator having a refrigerant vapor passage After the second generator is connected, the second generator is added, and the refrigerant liquid pipeline is connected with the first condenser through the addition of the second throttle valve, and the second generator and the refrigerant vapor passage are added. The first condenser is connected to form a third type of absorption with a three-effect process Heat pump. 42. The third type of absorption heat pump is a third type of absorption heat pump according to item 39, adding a new second generator, adding a second solution heat exchanger, adding a second throttle valve and A second solution pump is newly added, and the absorber has a dilute solution pipeline through the first solution heat exchanger and the newly added first solution heat exchanger is connected with the newly added first generator to adjust the absorber to a dilute solution pipeline. a solution heat exchanger, a new first solution heat exchanger and a new second solution heat exchanger are connected to the newly added second generator, and a second generator and a concentrated solution line are added to the second solution. The pump and the newly added second solution heat exchanger are connected with the newly added first generator, and the newly added first generator has a refrigerant vapor passage connected to the first condenser to adjust the newly added first generator to have a refrigerant vapor passage. After the second generator is connected, the second generator is added, and the refrigerant liquid pipeline is connected with the first condenser through the addition of the second throttle valve, and the second generator and the refrigerant vapor passage are added. The first condenser is connected to form a third type of absorption heat pump with a three-effect low temperature generation process .
43. 第三类吸收式热泵， 是在第 1、 13-20项内任一一项所述的第三类吸收式热泵中， 增加新增发生器、 新增溶液热交换器和新增节流阀， 第二溶液泵增设稀溶液管路经新增溶液 热交换器与新增发生器连通， 新增发生器还有浓溶液管路经新增溶液热交换器与第三发生器 连通， 将第一发生器有冷剂蒸汽通道与第一冷凝器连通调整为第一发生器有冷剂蒸汽通道与 新增发生器连通后新增发生器再有冷剂液管路经新增节流阀与第一冷凝器连通， 新增发生器 还有冷剂蒸汽通道与第一冷凝器连通， 形成以回热式双效为低温发生流程的第三类吸收式热 泵。  43. The third type of absorption heat pump is a third type of absorption heat pump according to any one of items 1, 13-20, adding a new generator, a new solution heat exchanger and an additional section. The flow valve, the second solution pump is provided with a dilute solution pipeline, and the new solution heat exchanger is connected with the newly added generator, and the new generator and the concentrated solution pipeline are connected to the third generator via the new solution heat exchanger. The first generator has a refrigerant vapor passage connected to the first condenser to be adjusted to be a first generator having a refrigerant vapor passage connected with the newly added generator, and then adding a new generator and then a refrigerant liquid pipeline is newly throttled The valve is in communication with the first condenser, and the new generator and the refrigerant vapor passage are in communication with the first condenser to form a third type of absorption heat pump having a regenerative double effect as a low temperature generation process.
44. 第三类吸收式热泵， 是在第 1、 13-20项内任一一项所述的第三类吸收式热泵中， 增加新增发生器、 新增溶液热交换器和新增节流阀， 将第二溶液泵有稀溶液管路经第三溶液 热交换器与第一发生器连通调整为第二溶液泵有稀溶液管路经新增溶液热交换器和第三溶液 热交换器与第一发生器连通， 将第一发生器有浓溶液管路经第三溶液热交换器与第三发生器 连通调整为第一发生器有浓溶液管路经第三溶液热交换器与新增发生器连通， 新增发生器还 有浓溶液管路经新增溶液热交换器与第三发生器连通， 将第一发生器有冷剂蒸汽通道与第一 冷凝器连通调整为第一发生器有冷剂蒸汽通道与新增发生器连通后新增发生器再有冷剂液管 路经新增节流阀与第一冷凝器连通， 新增发生器还有冷剂蒸汽通道与第一冷凝器连通， 形成 以回热式双效为低温发生流程的第三类吸收式热泵。  44. The third type of absorption heat pump is a third type of absorption heat pump according to any one of items 1, 13-20, adding a new generator, a new solution heat exchanger and an additional section. a flow valve, wherein the second solution pump has a dilute solution line connected to the first generator via the third solution heat exchanger to adjust to a second solution pump having a dilute solution line through the new solution heat exchanger and the third solution heat exchange The device is connected to the first generator, and the first generator has a concentrated solution pipeline connected to the third generator via the third solution heat exchanger to adjust the first generator to have a concentrated solution pipeline through the third solution heat exchanger and The new generator is connected, the new generator and the concentrated solution pipeline are connected to the third generator via the newly added solution heat exchanger, and the first generator has a refrigerant vapor passage connected to the first condenser to be adjusted to the first The generator has a refrigerant vapor passage connected with the newly added generator, and then a new generator is added, and the refrigerant liquid pipeline is connected to the first condenser via a new throttle valve, and the new generator has a refrigerant vapor passage and a first A condenser is connected to form a regenerative double effect as a low temperature flow The third type of absorption heat pump.
45. 第三类吸收式热泵， 是在第 1、 13- 20项内任一一项所述的第三类吸收式热泵中， 增加新增发生器、 新增溶液热交换器、 新增节流阀和新增溶液泵， 将第二溶液泵有稀溶液管 路经第三溶液热交换器与第一发生器连通调整为第二溶液泵有稀溶液管路经第三溶液热交换 器与新增发生器连通， 新增发生器还有浓溶液管路经新增溶液泵和新增溶液热交换器与第一 发生器连通， 将第一发生器有浓溶液管路经第三溶液热交换器与第三发生器连通调整为第一 发生器有浓溶液管路经新增溶液热交换器和第三溶液热交换器与第三发生器连通， 将第一发 生器有冷剂蒸汽通道与第一冷凝器连通调整为第一发生器有冷剂蒸汽通道与新增发生器连通 后新增发生器再有冷剂液管路经新增节流阀与第一冷凝器连通， 新增发生器还有冷剂蒸汽通 道与第一冷凝器连通， 形成以回热式双效为低温发生流程的第三类吸收式热泵。  45. The third type of absorption heat pump is a third type of absorption heat pump according to any one of items 1, 13-20, adding a new generator, a new solution heat exchanger, and an additional section. a flow valve and a new solution pump, the second solution pump has a dilute solution line connected to the first generator via the third solution heat exchanger to adjust to a second solution pump having a dilute solution line through the third solution heat exchanger and New generator connection, new generator and concentrated solution pipeline are connected to the first generator via the new solution pump and the new solution heat exchanger, and the first generator has a concentrated solution pipeline through the third solution heat. The exchanger is connected to the third generator and adjusted to be a first generator having a concentrated solution pipeline connected to the third generator via the new solution heat exchanger and the third solution heat exchanger, and the first generator has a refrigerant vapor passage The first condenser is connected to the first condenser to adjust the first generator to have a refrigerant vapor channel connected with the newly added generator, and then the new generator is connected to the first condenser through the newly added throttle valve. The generator also has a refrigerant vapor passage communicating with the first condenser, In double-effect heat recovery at a low temperature occurs in the third flow type absorption heat pump.
46. 第三类吸收式热泵， 是在第 43- 45项内任一一项所述的第三类吸收式热泵中， 取消 第三发生器与外部连通的余热介质管路， 增加新增第二节流阔， 第一发生器增设冷剂蒸汽通 道与第三发生器连通后第三发生器再有冷剂液管路经新增第二节流阀与第一冷凝器连通， 形 成以回热式双效为低温发生流程的第三类吸收式热泵。  The third type of absorption heat pump is the third type of absorption heat pump according to any one of items 43 to 45, wherein the waste heat medium line connecting the third generator to the outside is canceled, and the additional number is added. The second flow is wide, the first generator is connected with the refrigerant vapor passage and the third generator is connected, and the third generator is further connected with the first condenser through the addition of the second throttle valve through the second throttle valve, forming a back The thermal double effect is the third type of absorption heat pump for the low temperature generation process.
47. 第三类吸收式热泵， 是在第 43项所述的第三类吸收式热泵中， 增加新增第二发生 器、 新增第二溶液热交换器和新增第二节流阀， 第二溶液泵增设稀溶液管路经新增第二溶液 热交换器与新增第二发生器连通， 新增第二发生器还有浓溶液管路经新增第二溶液热交换器 与第三发生器连通， 将新增第一发生器有冷剂蒸汽通道与第一冷凝器连通调整为新增第一发 生器有冷剂蒸汽通道与新增第二发生器连通后新增第二发生器再有冷剂液管路经新增第二节 流阀与第一冷凝器连通， 新增第二发生器还有冷剂蒸汽通道与第一冷凝器连通， 形成以回热 式三效为低温发生流程的第三类吸收式热泵。 47. The third type of absorption heat pump is a third type of absorption heat pump according to item 43, adding a new second generator, adding a second solution heat exchanger and adding a second throttle valve. The second solution pump adds a dilute solution line through the addition of the second solution The heat exchanger is connected to the newly added second generator, and the second generator and the concentrated solution pipeline are connected to the third generator via the newly added second solution heat exchanger, and the first generator is added with the refrigerant. The steam passage is connected to the first condenser to be adjusted to add a first generator. The refrigerant vapor passage is connected with the newly added second generator, and the second generator is added, and the refrigerant liquid pipeline is added with the second throttle. The valve is in communication with the first condenser, and the second generator and the refrigerant vapor passage are connected to the first condenser to form a third type of absorption heat pump in which the regenerative three-effect is a low temperature generation process.
48. 第三类吸收式热泵， 是在第 44项所述的第三类吸收式热泵中， 增加新增第二发生 器、 新增第二溶液热交换器和新增第二节流阔， 将第二溶液泵有稀溶液管路经新增第一溶液 热交换器和第三溶液热交换器与第一发生器连通调整为第二溶液泵有稀溶液管路经新增第二 溶液热交换器、 新增第一溶液热交换器和第三溶液热交换器与第一发生器连通， 将新增第一 发生器有浓溶液管路经新增第一溶液热交换器与第三发生器连通调整为新增第一发生器有浓 溶液管路经新增第一溶液热交换器与新增第二发生器连通， 新增第二发生器还有浓溶液管路 经新增第二溶液热交换器与第三发生器连通， 将新增第一发生器有冷剂蒸汽通道与第一冷凝 器连通调整为新增第一发生器有冷剂蒸汽通道与新增第二发生器连通后新增第二发生器再有 冷剂液管路经新增第二节流阀与第一冷凝器连通， 新增第二发生器还有冷剂蒸汽通道与第一 冷凝器连通， 形成以回热式三效为低温发生流程的第三类吸收式热泵。  48. The third type of absorption heat pump is a third type of absorption heat pump according to item 44, adding a new second generator, adding a second solution heat exchanger and adding a second section of the flow. The second solution pump has a dilute solution pipeline connected to the first generator via the newly added first solution heat exchanger and the third solution heat exchanger to adjust to a second solution pump having a dilute solution pipeline and adding a second solution heat The exchanger, the first solution heat exchanger and the third solution heat exchanger are connected to the first generator, and the first generator has a concentrated solution pipeline added by the first solution heat exchanger and the third generation occurs The device is connected to adjust the new first generator to have a concentrated solution pipeline. The new first solution heat exchanger is connected with the newly added second generator, and the second generator and the concentrated solution pipeline are added by the second. The solution heat exchanger is in communication with the third generator, and the newly added first generator has a refrigerant vapor passage connected to the first condenser to be adjusted to add a first generator having a refrigerant vapor passage and a new second generator. After adding a second generator, there is a refrigerant liquid pipeline added by the second section. A condenser in communication with the first valve, as well as the new refrigerant vapor passage in communication with the second generator of the first condenser, recuperative form a three-way flow of the third occurrence of low absorption heat pump.
49. 第三类吸收式热泵， 是在第 45项所述的第三类吸收式热泵中， 增加新增第二发生 器、 新增第二溶液热交换器、 新增第二节流阀和新增第二溶液泵， 将第二溶液泵有稀溶液管 路经第三溶液热交换器与新增第一发生器连通调整为第二溶液泵有稀溶液管路经第三溶液热 交换器与新增第二发生器连通， 新增第二发生器还有浓溶液管路经新增第二溶液泵和新增第 二溶液热交换器与新增第一发生器连通， 将第一发生器有浓溶液管路经新增第一溶液热交换 器和第三溶液热交换器与第三发生器连通调整为第二发生器有浓溶液管路经新增第一溶液热 交换器、 新增第二溶液热交换器和第三溶液热交换器与第三发生器连通， 将新增第一发生器 有冷剂蒸汽通道与第一冷凝器连通调整为新增第一发生器有冷剂蒸汽通道与新增第二发生器 连通后新增第二发生器再有冷剂液管路经新增第二节流阀与第一冷凝器连通， 新增第二发生 器还有冷剂蒸汽通道与第一冷凝器连通， 形成以回热式三效为低温发生流程的第三类吸收式 热泵。  49. The third type of absorption heat pump, in the third type of absorption heat pump described in item 45, adds a new second generator, adds a second solution heat exchanger, adds a second throttle valve, and A second solution pump is newly added, and the second solution pump has a dilute solution line connected to the newly added first generator through the third solution heat exchanger to be adjusted to a second solution pump having a dilute solution line through the third solution heat exchanger Connected with the newly added second generator, the second generator and the concentrated solution pipeline are connected to the newly added first generator via the newly added second solution pump and the newly added second solution heat exchanger, which will occur first. The concentrated solution line is connected to the third generator through the addition of the first solution heat exchanger and the third solution heat exchanger to the second generator. The second generator has a concentrated solution line through the addition of the first solution heat exchanger, new The second solution heat exchanger and the third solution heat exchanger are connected to the third generator, and the newly added first generator has a refrigerant vapor channel connected to the first condenser to adjust the newly added first generator to have a refrigerant Add a second generator after the steam channel is connected to the new second generator. The refrigerant liquid pipeline is connected to the first condenser via a new second throttle valve, and a second generator and a refrigerant vapor passage are connected to the first condenser to form a regenerative three-effect low temperature generating process. The third type of absorption heat pump.
50. 第三类吸收式热泵， 是在第 47-49项内任一一项所述的第三类吸收式热泵中， 取消 第三发生器与外部连通的余热介质管路， 增加新增第三节流阀， 第一发生器增设冷剂蒸汽通 道与第三发生器连通后第三发生器再有冷剂液管路经新增第三节流阀与第一冷凝器连通， 形 成以三效为低温发生流程的回热式第三类吸收式热泵。  The third type of absorption heat pump is the third type of absorption heat pump according to any one of items 47-49, wherein the waste heat medium line connecting the third generator to the outside is canceled, and the additional number is added. a three-way valve, the first generator is connected with a refrigerant vapor passage and is connected with the third generator, and the third generator is further connected with the first condenser through a new third throttle valve, and is formed by three A regenerative third type absorption heat pump that functions as a low temperature generation process.
51. 第三类吸收式热泵， 是在第 47-49内任一第项所述的第三类吸收式热泵中， 取消第 三发生器与外部连通的余热介质管路， 增加新增第三节流阀， 新增第一发生器增设冷剂蒸汽 通道与第三发生器连通后第三发生器再有冷剂液管路经新增第三节流阀与第一冷凝器连通， 形成以回热式三效为低温发生流程的第三类吸收式热泵。  The third type of absorption heat pump is a third type of absorption heat pump according to any of the items 47-49, wherein the waste heat medium line connecting the third generator to the outside is canceled, and a third is added. The throttle valve is newly added to the first generator to add a refrigerant vapor passage to communicate with the third generator, and the third generator and the refrigerant liquid pipeline are connected to the first condenser via a new third throttle valve to form The regenerative three-effect is the third type of absorption heat pump for the low temperature generation process.
52. 第三类吸收式热泵， 是在第 2-3、 21-28项内任一一项所述的第三类吸收式热泵中， 增加新增发生器、 新增溶液热交换器和新增节流阀， 将第一发生器有浓溶液管路经第一溶液 泵、第一溶液热交换器和吸收-发生器与分汽室连通调整为第一发生器有浓溶液管路经第一溶 液热交换器和吸收-发生器与分汽室连通， 吸收-发生器增设稀溶液管路经新增溶液热交换器 与新增发生器连通， 新增发生器还有浓溶液管路经第一溶液泵和新增溶液热交换器之后与第 一发生器经第一溶液热交换器之后的浓溶液管路汇合， 将第一发生器有冷剂蒸汽通道与第一 冷凝器连通调整为第一发生器有冷剂蒸汽通道与新增发生器连通后新增发生器再有冷剂液管 路经新增节流阀与第一冷凝器连通， 新增发生器还有冷剂蒸汽通道与第一冷凝器连通， 形成 以回热式双效为低温发生流程的第三类吸收式热泵。 52. The third type of absorption heat pump is a third type of absorption heat pump according to any one of items 2-3, 21-28, adding a new generator, a new solution heat exchanger and a new one. The throttle valve is added, and the first generator has a concentrated solution pipeline connected to the first solution pump, the first solution heat exchanger, and the absorption-generator and the steam distribution chamber to adjust the first generator to have a concentrated solution pipeline A solution heat exchanger and an absorption-generator are connected to the steam distribution chamber, and the absorption-generator adds a dilute solution pipeline through the new solution heat exchanger to communicate with the newly added generator, and the new generator and the concentrated solution pipeline are The first solution pump and the newly added solution heat exchanger are merged with the first generator through the concentrated solution line after the first solution heat exchanger, and the first generator has a refrigerant vapor channel and the first The condenser is connected to adjust to the first generator, and the refrigerant vapor channel is connected with the newly added generator, and then the new generator is connected, and the refrigerant liquid pipeline is connected with the first condenser through the newly added throttle valve, and the new generator is further connected. A refrigerant vapor passage is connected to the first condenser to form a third type of absorption heat pump having a regenerative double effect as a low temperature generation process.
53. 第三类吸收式热泵， 是在第 2-3、 21- 28项内任一一项所述的第三类吸收式热泵中， 增加新增发生器、新增节流阀和新增溶液节流阀， 将第一发生器有浓溶液管路经第一溶液泵、 第一溶液热交换器和吸收-发生器与分汽室连通调整为第一发生器有浓溶液管路经溶液节流 阀和吸收-发生器与分汽室连通， 将吸收-发生器有稀溶液管路经第一溶液热交换器与第一发 生器连通调整为吸收 -发生器有稀溶液管路直接与第一发生器连通， 吸收 -发生器增设稀溶液 管路经第一溶液热交换器与新增发生器连通， 新增发生器还有浓溶液管路经第一溶液泵和第 一溶液热交换器之后与第一发生器经溶液节流阀之后的浓溶液管路汇合， 将第一发生器有冷 剂蒸汽通道与第一冷凝器连通调整为第一发生器有冷剂蒸汽通道与新增发生器连通后新增发 生器再有冷剂液管路经新增节流阀与第一冷凝器连通， 新增发生器还有冷剂蒸汽通道与第一 冷凝器连通； 取消第一蒸发器或第二蒸发器与吸收-发生器连通的冷剂蒸汽通道， 第一发生器 增设冷剂蒸汽通道与吸收-发生器连通， 取消第三溶液泵， 吸收器有稀溶液管路经第三溶液热 交换器与吸收-发生器连通， 形成以回热式双效为低温发生流程的第三类吸收式热泵。  53. The third type of absorption heat pump is a third type of absorption heat pump according to any one of items 2-3, 21-28, adding a new generator, adding a new throttle valve and adding a solution throttle valve, the first generator has a concentrated solution pipeline connected to the first solution pump, the first solution heat exchanger, and the absorption-generator and the steam distribution chamber to adjust the first generator to have a concentrated solution pipeline through the solution The throttle valve and the absorption-generator are connected to the steam distribution chamber, and the absorption-generator has a dilute solution pipeline connected to the first generator through the first solution heat exchanger to adjust to absorption-the generator has a dilute solution pipeline directly The first generator is connected, the absorption-generator adds a dilute solution pipeline through the first solution heat exchanger to communicate with the newly added generator, and the new generator and the concentrated solution pipeline are exchanged with the first solution pump and the first solution. After the first generator is merged with the concentrated solution pipeline after the solution throttle valve, the first generator has a refrigerant vapor passage connected to the first condenser, and the first generator has a refrigerant vapor passage and newly added After the generator is connected, the generator is added and the coolant line is new. The throttle valve is in communication with the first condenser, and the new generator and the refrigerant vapor passage are in communication with the first condenser; canceling the refrigerant vapor passage of the first evaporator or the second evaporator and the absorption-generator, A generator adds a refrigerant vapor channel to communicate with the absorption-generator, cancels the third solution pump, and the absorber has a dilute solution line connected to the absorption-generator via the third solution heat exchanger to form a regenerative double effect The third type of absorption heat pump for the low temperature generation process.
54. 第三类吸收式热泵， 是在第 2-3、 21-28项内任一一项所述的第三类吸收式热泵中， 增加新增发生器、 新增溶液热交换器和新增节流阀， 将第一发生器有浓溶液管路经第一溶液 泵、第一溶液热交换器和吸收-发生器与分汽室连通调整为第一发生器有浓溶液管路经新增溶 液热交换器与新增发生器连通， 新增发生器还有浓溶液管路经第一溶液泵、 新增溶液热交换 器、第一溶液热交换器和吸收-发生器与分汽室连通， 将第一发生器有冷剂蒸汽通道与第一冷 凝器连通调整为第一发生器有冷剂蒸汽通道与新增发生器连通后新增发生器再有冷剂液管路 经新增节流阀与第一冷凝器连通， 新增发生器还有冷剂蒸汽通道与第一冷凝器连通， 形成以 回热式双效为低温发生流程的第三类吸收式热泵。  54. The third type of absorption heat pump is a third type of absorption heat pump according to any one of items 2-3, 21-28, adding a new generator, a new solution heat exchanger and a new one. The throttle valve is added, and the first generator has a concentrated solution pipeline connected to the first solution pump, the first solution heat exchanger, and the absorption-generator and the steam distribution chamber to adjust the first generator to have a concentrated solution pipeline through the new The solution heat exchanger is connected to the newly added generator, and the new generator and the concentrated solution line are passed through the first solution pump, the new solution heat exchanger, the first solution heat exchanger, and the absorption-generator and the steam distribution chamber. Connected, the first generator has a refrigerant vapor passage connected to the first condenser, and the first generator has a refrigerant vapor passage connected with the newly added generator, and the new generator is further added with a refrigerant liquid pipeline. The throttle valve is in communication with the first condenser, and the new generator and the refrigerant vapor passage are in communication with the first condenser to form a third type of absorption heat pump having a regenerative double effect as a low temperature generation process.
55. 第三类吸收式热泵， 是在第 2-3、 21-28项内任一一项所述的第三类吸收式热泵中， 增加新增发生器和新增节流阔，将吸收 -发生器有稀溶液管路经第一溶液热交换器与第一发生 器连通调整为吸收-发生器有稀溶液管路直接与第一发生器连通，将第一发生器有浓溶液管路 经第一溶液泵、第一溶液热交换器和吸收-发生器与分汽室连通调整为第一发生器有浓溶液管 路经第一溶液热交换器与新增发生器连通， 新增发生器还有浓溶液管路经第一溶液泵、 第一 溶液热交换器和吸收-发生器与分汽室连通，将第一发生器有冷剂蒸汽通道与第一冷凝器连通 调整为第一发生器有冷剂蒸汽通道与新增发生器连通后新增发生器再有冷剂液管路经新增节 流阀与第一冷凝器连通， 新增发生器还有冷剂蒸汽通道与第一冷凝器连通； 取消第一蒸发器 或第二蒸发器与吸收-发生器连通的冷剂蒸汽通道， 第一发生器增设冷剂蒸汽通道与吸收-发 生器连通， 取消第三溶液泵， 吸收器有稀溶液管路经第三溶液热交换器与吸收-发生器连通， 形成以回热式双效为低温发生流程的第三类吸收式热泵。  55. The third type of absorption heat pump is a third type of absorption heat pump according to any one of items 2-3, 21-28, adding new generators and adding new throttle, which will absorb - the generator has a dilute solution line connected to the first generator via the first solution heat exchanger to adjust to absorption - the generator has a dilute solution line directly communicating with the first generator, the first generator having a concentrated solution line The first solution pump, the first solution heat exchanger and the absorption-generator are connected to the steam separation chamber to be adjusted to be the first generator, and the concentrated solution pipeline is connected to the newly added generator through the first solution heat exchanger, and the addition occurs. The concentrated solution pipeline is connected to the steam distribution chamber through the first solution pump, the first solution heat exchanger and the absorption-generator, and the first generator has a refrigerant vapor passage connected to the first condenser to be adjusted to the first The generator has a refrigerant vapor passage connected with the newly added generator, and then a new generator is added, and the refrigerant liquid pipeline is connected to the first condenser via a new throttle valve, and the new generator has a refrigerant vapor passage and a first a condenser is connected; cancel the first evaporator or the second evaporator and absorb-transmit a refrigerant vapor passage connected to the refrigerant, the first generator adds a refrigerant vapor passage to communicate with the absorption-generator, cancels the third solution pump, and the absorber has a dilute solution pipeline connected to the absorption-generator via the third solution heat exchanger A third type of absorption heat pump with a regenerative double effect as a low temperature generation process is formed.
56. 第三类吸收式热泵， 是在第 2-3、 21- 28项内任一一项所述的第三类吸收式热泵中， 增加新增发生器、 新增溶液热交换器、 新增节流阀和新增溶液泵， 将吸收 -发生器有稀溶液管 路经第一溶液热交换器与第一发生器连通调整为吸收-发生器有稀溶液管路第一溶液热交换 器和新增溶液热交换器与新增发生器连通， 新增发生器还有浓溶液管路经新增溶液泵和新增 溶液热交换器与第一发生器连通， 将第一发生器有冷剂蒸汽通道与第一冷凝器连通调整为第 一发生器有冷剂蒸汽通道与新增发生器连通后新增发生器再有冷剂液管路经新增节流阀与第 一冷凝器连通， 新增发生器还有冷剂蒸汽通道与第一冷凝器连通， 形成以回热式双效为低温 发生流程的第三类吸收式热泵。 56. The third type of absorption heat pump is a third type of absorption heat pump according to any one of items 2-3, 21-28, adding a new generator, a new solution heat exchanger, and a new one. The throttle valve and the new solution pump are added, and the absorption-generator has a dilute solution line connected to the first generator through the first solution heat exchanger to be adjusted to absorb-the generator has a dilute solution line first solution heat exchanger And the new solution heat exchanger is connected with the newly added generator, the new generator and the concentrated solution pipeline are connected to the first generator through the new solution pump and the new solution heat exchanger, and the first generator is cooled. The steam passage of the agent is connected to the first condenser to be adjusted so that the first generator has a refrigerant vapor passage connected with the newly added generator, and the new generator is further provided with a refrigerant liquid pipeline through the newly added throttle valve and the first A condenser is connected, and a new generator and a refrigerant vapor passage are connected to the first condenser to form a third type of absorption heat pump with a regenerative double effect as a low temperature generation process.
57. 第三类吸收式热泵， 是在第 2-3、 21-28项内任一一项所述的第三类吸收式热泵中， 增加新增发生器、新增溶液节流阀和新增节流阀， 将第一发生器有浓溶液管路经第一溶液泵、 第一溶液热交换器和吸收-发生器与分汽室连通调整为第一发生器有浓溶液管路经新增溶液 节流阀和吸收-发生器与分汽室连通， 将吸收 -发生器有稀溶液管路经第一溶液热交换器与第 一发生器连通调整为吸收 -发生器有稀溶液管路第一溶液热交换器与新增发生器连通，新增发 生器还有浓溶液管路经第一溶液泵和第一溶液热交换器与第一发生器连通， 将第一发生器有 冷剂蒸汽通道与第一冷凝器连通调整为第一发生器有冷剂蒸汽通道与新增发生器连通后新增 发生器再有冷剂液管路经新增节流阀与第一冷凝器连通， 新增发生器还有冷剂蒸汽通道与第 一冷凝器连通； 取消第一蒸发器或第二蒸发器与吸收-发生器连通的冷剂蒸汽通道， 第一发生 器增设冷剂蒸汽通道与吸收-发生器连通， 取消第三溶液泵， 吸收器有稀溶液管路经第三溶液 热交换器与吸收-发生器连通， 形成以回热式双效为低温发生流程的第三类吸收式热泵。  57. The third type of absorption heat pump is a third type of absorption heat pump according to any one of items 2-3, 21-28, adding a new generator, a new solution throttle valve and a new one. The throttle valve is added, and the first generator has a concentrated solution pipeline connected to the first solution pump, the first solution heat exchanger, and the absorption-generator and the steam distribution chamber to adjust the first generator to have a concentrated solution pipeline through the new The increasing solution throttle valve and the absorption-generator are connected to the steam distribution chamber, and the absorption-generator has a dilute solution pipeline connected to the first generator through the first solution heat exchanger to adjust to an absorption-generator with a dilute solution pipeline The first solution heat exchanger is connected to the newly added generator, and the new generator and the concentrated solution pipeline are connected to the first generator via the first solution pump and the first solution heat exchanger, and the first generator has a refrigerant. The steam passage is connected to the first condenser to be adjusted so that the first generator has a refrigerant vapor passage connected with the newly added generator, and then the new generator is connected, and the refrigerant liquid pipeline is connected to the first condenser via the newly added throttle valve. The new generator also has a refrigerant vapor passage that communicates with the first condenser; The evaporator or the second evaporator is connected to the refrigerant vapor passage of the absorption-generator, the first generator is connected with the refrigerant vapor passage and communicates with the absorption-generator, cancels the third solution pump, and the absorber has a dilute solution pipeline. The three-solution heat exchanger is in communication with the absorption-generator to form a third type of absorption heat pump with a regenerative double effect as a low temperature generation process.
58. 第三类吸收式热泵， 是在第 52项所述的第三类吸收式热泵中， 增加新增第二发生 器、 新增第二溶液热交换器和新增第二节流阀， 将新增第一发生器有浓溶液管路经第一溶液 泵和新增第一溶液热交换器之后与第一发生器经第一溶液热交换器之后的浓溶液管路汇合调 整为新增第一发生器有浓溶液管路经新增第一溶液热交换器之后与第一发生器经第一溶液热 交换器之后的浓溶液管路汇合，吸收-发生器增设稀溶液管路经新增第二溶液热交换器与新增 第二发生器连通， 新增第二发生器还有浓溶液管路经第一溶液泵和新增第二溶液热交换器之 后与第一发生器经第一溶液热交换器之后的浓溶液管路汇合， 将新增第一发生器有冷剂蒸汽 通道与第一冷凝器连通调整为新增第一发生器有冷剂蒸汽通道与新增第二发生器连通后新增 第二发生器再有冷剂液管路经新增第二节流阀与第一冷凝器连通， 新增第二发生器还有冷剂 蒸汽通道与第一冷凝器连通， 形成以回热式三效为低温发生流程的第三类吸收式热泵。  58. The third type of absorption heat pump is a third type of absorption heat pump according to item 52, adding a second generator, adding a second solution heat exchanger and adding a second throttle valve. Adding a new first generator with a concentrated solution line through the first solution pump and adding a first solution heat exchanger to merge with the first generator through the first solution heat exchanger after the concentrated solution line is adjusted to be newly added The first generator has a concentrated solution pipeline which is merged with the concentrated solution pipeline after the first generator passes through the first solution heat exchanger after adding the first solution heat exchanger, and the absorption-generator adds a dilute solution pipeline through the new The second solution heat exchanger is connected with the newly added second generator, and the second generator and the concentrated solution pipeline are added to the first generator through the first solution pump and the second solution heat exchanger. The concentrated solution pipeline after the solution heat exchanger merges, and the newly added first generator has a refrigerant vapor passage connected with the first condenser to adjust the newly added first generator to have a refrigerant vapor passage and the second addition occurs. After the device is connected, the second generator is added and the refrigerant liquid pipeline is added. A second throttle valve is connected to the first condenser, and a second generator and a refrigerant vapor passage are connected to the first condenser to form a third type of absorption with a regenerative three-effect process. Heat pump.
59. 第三类吸收式热泵， 是在第 53项所述的第三类吸收式热泵中， 增加新增第二发生 器、 新增溶液热交换器和新增第二节流阔， 将新增第一发生器有浓溶液管路经第一溶液泵和 第一溶液热交换器与第一发生器经新增溶液节流阀之后的浓溶液管路汇合调整为新增第一发 生器有浓溶液管路经第一溶液热交换器之后与第一发生器经新增溶液节流阀之后的浓溶液管 路汇合， 吸收-发生器增设稀溶液管路经新增溶液热交换器与新增第二发生器连通， 新增第二 发生器还有浓溶液管路经第一溶液泵和新增溶液热交换器之后与第一发生器经新增溶液节流 阀之后的浓溶液管路汇合， 将新增第一发生器有冷剂蒸汽通道与第一冷凝器连通调整为新增 第一发生器有冷剂蒸汽通道与新增第二发生器连通后新增第二发生器再有冷剂液管路经新增 第二节流阀与第一冷凝器连通， 新增第二发生器还有冷剂蒸汽通道与第一冷凝器连通， 形成 以回热式三效为低温发生流程的第三类吸收式热泵。  59. The third type of absorption heat pump, in the third type of absorption heat pump described in item 53, adds a new second generator, a new solution heat exchanger and a new second section, which will be new. Increasing the first generator has a concentrated solution pipeline through the first solution pump and the first solution heat exchanger and the first generator through the new solution throttle valve after the concentrated solution pipeline is adjusted to be added to the first generator The concentrated solution pipeline passes through the first solution heat exchanger and merges with the concentrated solution pipeline of the first generator after adding the solution throttle valve, and the absorption-generator adds a dilute solution pipeline through the newly added solution heat exchanger and the new The second generator is connected, and the second generator and the concentrated solution pipeline are added after the first solution pump and the new solution heat exchanger are connected to the first generator through the new solution throttle valve. Convergence, the first generator is added with a refrigerant vapor channel and the first condenser is connected to adjust to add a new generator. The refrigerant vapor channel is connected with the newly added second generator, and the second generator is added. The refrigerant liquid pipeline is added with the second throttle valve and the first condenser Pass, as well as the new refrigerant vapor passage in communication with the second generator of the first condenser, recuperative form a three-way flow of the third occurrence of low absorption heat pump.
60. 第三类吸收式热泵， 是在第 59项所述的第三类吸收式热泵中， 将吸收 -发生器有稀 溶液管路直接与第一发生器连通调整为吸收-发生器有稀溶液管路经第一溶液热交换器与第 一发生器连通，将第一发生器有浓溶液管路经新增溶液节流阀和吸收-发生器与分汽室连通调 整为第一发生器有浓溶液管路经第一溶液热交换器和吸收-发生器与分汽室连通， 将吸收-发 生器有稀溶液管路经第一溶液热交换器与新增第一发生器连通调整为吸收-发生器有稀溶液 管路直接与新增第一发生器连通， 将新增第一发生器有浓溶液管路经第一溶液热交换器和吸 收-发生器与分汽室连通调整为新增第一发生器有浓溶液管路经新增溶液节流阀和吸收 -发生 器与分汽室连通，将第一发生器有冷剂蒸汽通道与吸收-发生器连通调整为新增第一发生器有 冷剂蒸汽通道与吸收-发生器连通， 形成以回热式三效为低温发生流程的第三类吸收式热泵。 60. The third type of absorption heat pump is a third type of absorption heat pump according to item 59, wherein the absorption-generator has a dilute solution line directly connected to the first generator to be adjusted to an absorption-generator The solution pipeline is connected to the first generator via the first solution heat exchanger, and the first generator has a concentrated solution pipeline connected to the first generator via the new solution throttle valve and the absorption-generator and the steam distribution chamber. The concentrated solution pipeline is connected to the steam distribution chamber through the first solution heat exchanger and the absorption-generator, and the absorption-generator has a dilute solution pipeline connected to the newly added first generator through the first solution heat exchanger to be adjusted to The absorption-generator has a dilute solution line directly connected to the newly added first generator, and the newly added first generator has a concentrated solution line that is connected to the first solution heat exchanger and the absorption-generator and the steam distribution chamber to adjust Added first generator with concentrated solution pipeline via new solution throttle valve and absorption-occurrence The device is connected to the steam distribution chamber, and the first generator has a refrigerant vapor passage and an absorption-generator connection, and is adjusted to be a new first generator having a refrigerant vapor passage and an absorption-generator connected to form a regenerative three-effect The third type of absorption heat pump for low temperature generation processes.
61. 第三类吸收式热泵， 是在第 54项所述的第三类吸收式热泵中， 增加新增第二发生 器、 新增第二溶液热交换器和新增第二节流阀， 将新增第一发生器有浓溶液管路经第一溶液 泵和新增第一溶液热交换器与第一溶液热交换器连通调整为新增第一发生器有浓溶液管路经 新增第二溶液热交换器与新增第二发生器连通， 新增第二发生器还有浓溶液管路经第一溶液 泵、 新增第二溶液热交换器和新增第一溶液热交换器与第一溶液热交换器连通， 将新增第一 发生器有冷剂蒸汽通道与第一冷凝器连通调整为新增第一发生器有冷剂蒸汽通道与新增第二 发生器连通后新增第二发生器再有冷剂液管路经新增第二节流阀与第一冷凝器连通， 新增第 二发生器还有冷剂蒸汽通道与第一冷凝器连通， 形成以回热式三效为低温发生流程的第三类 吸收式热泵。  61. The third type of absorption heat pump is a third type of absorption heat pump according to item 54, adding a new second generator, adding a second solution heat exchanger and adding a second throttle valve. Adding a new first generator with a concentrated solution pipeline through the first solution pump and adding a first solution heat exchanger to the first solution heat exchanger to adjust to add a new first generator with a concentrated solution pipeline added The second solution heat exchanger is connected with the newly added second generator, and the second generator and the concentrated solution line are added through the first solution pump, the second solution heat exchanger is added, and the first solution heat exchanger is added. Communicating with the first solution heat exchanger, connecting the newly added first generator refrigerant vapor passage to the first condenser to adjust to add a new first generator having a refrigerant vapor passage and connecting the newly added second generator The second generator further has a refrigerant liquid pipeline connected to the first condenser via a new second throttle valve, and a second generator and a refrigerant vapor passage are connected to the first condenser to form a heat recovery. The third type of absorption heat pump is a third type of low temperature generation process.
62. 第三类吸收式热泵， 是在第 55项所述的第三类吸收式热泵中， 增加新增第二发生 器、 新增溶液热交换器和新增第二节流阀， 将新增第一发生器有浓溶液管路经第一溶液泵与 第一溶液热交换器连通调整为新增第一发生器有浓溶液管路经新增溶液热交换器与新增第二 发生器连通， 新增第二发生器还有浓溶液管路经第一溶液泵和新增溶液热交换器与第一溶液 热交换器连通， 将新增第一发生器有冷剂蒸汽通道与第一冷凝器连通调整为新增第一发生器 有冷剂蒸汽通道与新增第二发生器连通后新增第二发生器再有冷剂液管路经新增第二节流阀 与第一冷凝器连通， 新增第二发生器还有冷剂蒸汽通道与第一冷凝器连通， 形成以回热式三 效为低温发生流程的第三类吸收式热泵。  62. The third type of absorption heat pump is the third type of absorption heat pump described in item 55. The addition of the second generator, the new solution heat exchanger and the addition of the second throttle valve will be new. The first generator has a concentrated solution pipeline connected to the first solution heat exchanger via the first solution pump and is adjusted to be a new first generator having a concentrated solution pipeline via a new solution heat exchanger and a second addition generator Connected, the second generator and the concentrated solution pipeline are connected to the first solution heat exchanger via the first solution pump and the new solution heat exchanger, and the first generator has a refrigerant vapor passage and the first The condenser is connected to adjust the new first generator to have a refrigerant vapor channel and the second generator is connected to add a second generator, and then the refrigerant liquid pipeline is added with the second throttle valve and the first condensation The device is connected, and a second generator and a refrigerant vapor channel are connected to the first condenser to form a third type of absorption heat pump with a regenerative three-effect process.
63. 第三类吸收式热泵， 是在第 62项所述的第三类吸收式热泵中， 增加新增溶液泵， 将吸收-发生器有稀溶液管路直接与第一发生器连通调整为吸收-发生器有稀溶液管路经新增 溶液泵和第一溶液热交换器与第一发生器连通， 将新增第二发生器有浓溶液管路经第一溶液 泵和新增溶液热交换器与第一溶液热交换器连通调整为新增第二发生器有浓溶液管路经第一 溶液泵和新增溶液热交换器与吸收-发生器连通， 将第一发生器有冷剂蒸汽通道与吸收-发生 器连通调整为新增第一发生器有冷剂蒸汽通道与吸收-发生器连通，形成以回热式三效为低温 发生流程的第三类吸收式热泵。  63. The third type of absorption heat pump is the third type of absorption heat pump described in item 62. The new solution pump is added, and the absorption-generator has a dilute solution line directly connected to the first generator. The absorption-generator has a dilute solution pipeline connected to the first generator via the new solution pump and the first solution heat exchanger, and the second generator has a concentrated solution pipeline through the first solution pump and the new solution heat The exchanger is connected to the first solution heat exchanger to be adjusted to add a second generator. The concentrated solution pipeline is connected to the absorption generator via the first solution pump and the new solution heat exchanger, and the first generator has a refrigerant. The steam passage and the absorption-generator connection are adjusted to add a first generator having a refrigerant vapor passage communicating with the absorption-generator to form a third type of absorption heat pump having a regenerative three-effect low temperature generation process.
64. 第三类吸收式热泵， 是在第 56项所述的第三类吸收式热泵中， 增加新增第二发生 器、新增第二溶液热交换器、 新增第二节流阀和新增第二溶液泵， 将吸收 -发生器有稀溶液管 路经第一溶液热交换器和新增第一溶液热交换器与新增第一发生器连通调整为吸收-发生器 有稀溶液管路经第一溶液热交换器、 新增第一溶液热交换器和新增第二溶液热交换器与新增 第二发生器连通， 新增第二发生器还有浓溶液管路经新增第二溶液泵和新增第二溶液热交换 器与新增第一发生器连通， 将新增第一发生器有冷剂蒸汽通道与第一冷凝器连通调整为新增 第一发生器有冷剂蒸汽通道与新增第二发生器连通后新增第二发生器再有冷剂液管路经新增 第二节流阀与第一冷凝器连通， 新增第二发生器还有冷剂蒸汽通道与第一冷凝器连通， 形成 以回热式三效为低温发生流程的第三类吸收式热泵。  64. The third type of absorption heat pump is a third type of absorption heat pump according to item 56, adding a new second generator, adding a second solution heat exchanger, adding a second throttle valve and Adding a second solution pump, adjusting the absorption-generator dilute solution line through the first solution heat exchanger and adding the first solution heat exchanger to the newly added first generator to adjust to the absorption-generator with dilute solution The pipeline is connected to the newly added second generator via the first solution heat exchanger, the newly added first solution heat exchanger and the newly added second solution heat exchanger, and the second generator and the concentrated solution pipeline are newly added. The second solution pump and the newly added second solution heat exchanger are connected with the newly added first generator, and the newly added first generator has a refrigerant vapor channel connected to the first condenser and is adjusted to be a new first generator. The refrigerant vapor channel is connected with the newly added second generator, and the second generator is added, and the refrigerant liquid pipeline is connected with the first condenser through the addition of the second throttle valve, and the second generator is added with cold. The vapor channel of the agent is in communication with the first condenser, and is formed in a regenerative three-effect manner to occur at a low temperature. The third process type absorption heat pump.
65. 第三类吸收式热泵， 是在第 57项所述的第三类吸收式热泵中， 增加新增第二发生 器、 新增溶液热交换器、 新增第二节流阀和新增溶液泵， 将吸收-发生器有稀溶液管路第一溶 液热交换器与新增第一发生器连通调整为吸收-发生器有稀溶液管路经第一溶液热交换器和 新增溶液热交换器与新增第二发生器连通， 新增第二发生器还有浓溶液管路经新增溶液泵和 新增溶液热交换器与新增第一发生器连通， 将新增第一发生器有冷剂蒸汽通道与第一冷凝器 连通调整为新增第一发生器有冷剂蒸汽通道与新增第二发生器连通后新增第二发生器再有冷 剂液管路经新增第二节流阀与第一冷凝器连通， 新增第二发生器还有冷剂蒸汽通道与第一冷 凝器连通， 形成以回热式三效为低温发生流程的第三类吸收式热泵。 65. The third type of absorption heat pump is the addition of the second generator, the new solution heat exchanger, the addition of the second throttle valve and the addition of the third type of absorption heat pump described in item 57. The solution pump, the absorption-generator has a dilute solution line, the first solution heat exchanger is connected with the newly added first generator, and is adjusted to absorb-the generator has a dilute solution line through the first solution heat exchanger and the new solution heat The exchanger is connected to the newly added second generator, and the second generator and the concentrated solution pipeline are connected to the newly added first generator via the new solution pump and the new solution heat exchanger, and the first occurrence occurs. a refrigerant vapor passage and a first condenser The connection is adjusted to add a first generator with a refrigerant vapor channel and a new second generator is connected, a second generator is added, and a refrigerant liquid pipeline is connected to the first condenser via a new second throttle valve. A second generator and a refrigerant vapor passage are connected to the first condenser to form a third type of absorption heat pump with a regenerative three-effect process.
66. 第三类吸收式热泵， 是在第 65项所述的第三类吸收式热泵中， 取消新增溶液节流 阀，将第一发生器有浓溶液管路经新增溶液节流阀和吸收-发生器与分汽室连通调整为第一发 生器有浓溶液管路经第一溶液热交换器和吸收-发生器与分汽室连通， 将吸收-发生器有稀溶 液管路经第一溶液热交换器和新增溶液热交换器与新增第二发生器连通调整为吸收-发生器 有稀溶液管路经新增溶液热交换器与新增第二发生器连通， 将第一发生器有冷剂蒸汽通道与 吸收-发生器连通调整为新增第一发生器增设冷剂蒸汽通道与吸收-发生器连通， 形成以回热 式三效为低温发生流程的第三类吸收式热泵。  66. The third type of absorption heat pump is the third type of absorption heat pump described in item 65. The new solution throttle valve is cancelled, and the first generator has a concentrated solution line through the newly added solution throttle valve. And the absorption-generator is connected to the steam separation chamber to adjust to the first generator, the concentrated solution pipeline is connected to the steam distribution chamber through the first solution heat exchanger and the absorption-generator, and the absorption-generator has a dilute solution pipeline The first solution heat exchanger and the newly added solution heat exchanger are connected to the newly added second generator to be adjusted to be an absorption-generator having a dilute solution line connected to the newly added second generator via the newly added solution heat exchanger, A generator has a refrigerant vapor channel and an absorption-generator connection adjusted to add a first generator to add a refrigerant vapor channel to communicate with the absorption-generator to form a third type of absorption with a regenerative three-effect process for low temperature generation. Heat pump.
67. 第三类吸收式热泵， 是在第 4、 29-36项内任一一项所述的第三类吸收式热泵中， 增加新增发生器、 新增溶液热交换器、新增节流阀和新增溶液泵， 吸收-发生器增设稀溶液管 路经新增溶液热交换器与新增发生器连通， 新增发生器还有浓溶液管路经新增溶液泵和新增 溶液热交换器与吸收 -发生器连通，将第一发生器有冷剂蒸汽通道与第一冷凝器连通调整为第 一发生器有冷剂蒸汽通道与新增发生器连通后新增发生器再有冷剂液管路经新增节流阀与第 一冷凝器连通， 新增发生器还有冷剂蒸汽通道与第一冷凝器连通， 形成以回热式双效为低温 发生流程的第三类吸收式热泵。  67. The third type of absorption heat pump is a third type of absorption heat pump according to any one of items 4, 29-36, adding a new generator, a new solution heat exchanger, and an additional section. Flow valve and new solution pump, absorption-generator added dilute solution pipeline through new solution heat exchanger and new generator connected, new generator and concentrated solution pipeline through new solution pump and new solution The heat exchanger is connected to the absorption-generator, and the first generator has a refrigerant vapor passage connected to the first condenser, and is adjusted to be a first generator having a refrigerant vapor passage connected with the newly added generator, and then adding a new generator. The refrigerant liquid pipeline is connected to the first condenser via a new throttle valve, and the newly added generator and the refrigerant vapor passage are connected with the first condenser to form a third type in which the regenerative double effect is a low temperature generating process. Absorption heat pump.
68. 第三类吸收式热泵， 是在第 4、 29- 36项内任一一项所述的第三类吸收式热泵中， 增加新增发生器、 新增溶液热交换器和新增节流阀， 将第一发生器有浓溶液管路经第一溶液 泵和第一溶液热交换器与吸收 -发生器连通调整为第一发生器有浓溶液管路经新增溶液热交 换器与新增发生器连通， 新增发生器还有浓溶液管路经第一溶液泵、 新增溶液热交换器和第 一溶液热交换器与吸收-发生器连通，将第一发生器有冷剂蒸汽通道与第一冷凝器连通调整为 第一发生器有冷剂蒸汽通道与新增发生器连通后新增发生器再有冷剂液管路经新增节流阀与 第一冷凝器连通， 新增发生器还有冷剂蒸汽通道与第一冷凝器连通， 形成以回热式双效为低 温发生流程的第三类吸收式热泵。  68. The third type of absorption heat pump is a third type of absorption heat pump according to any one of items 4, 29-36, adding a new generator, a new solution heat exchanger and an additional section. a flow valve, the first generator has a concentrated solution pipeline connected to the first solution pump and the first solution heat exchanger and the absorption-generator to adjust the first generator to have a concentrated solution pipeline through the new solution heat exchanger and New generator connection, new generator and concentrated solution pipeline are connected to the absorption-generator via the first solution pump, the new solution heat exchanger and the first solution heat exchanger, and the first generator has a refrigerant The steam passage is connected to the first condenser to be adjusted so that the first generator has a refrigerant vapor passage connected with the newly added generator, and then the new generator is connected, and the refrigerant liquid pipeline is connected to the first condenser via the newly added throttle valve. The new generator also has a refrigerant vapor passage that communicates with the first condenser to form a third type of absorption heat pump that uses a regenerative double effect as a low temperature generation process.
69. 第三类吸收式热泵， 是在第 4、 29-36项内任一一项所述的第三类吸收式热泵中， 增加新增发生器、 新增溶液热交换器、 新增节流阀和新增溶液泵， 将吸收 -发生器有稀溶液管 路经第一溶液热交换器与第一发生器连通调整为吸收-发生器有稀溶液管路第一溶液热交换 器和新增溶液热交换器与新增发生器连通， 新增发生器还有浓溶液管路经新增溶液泵和新增 溶液热交换器与第一发生器连通， 将第一发生器有冷剂蒸汽通道与第一冷凝器连通调整为第 一发生器有冷剂蒸汽通道与新增发生器连通后新增发生器再有冷剂液管路经新增节流阀与第 一冷凝器连通， 新增发生器还有冷剂蒸汽通道与第一冷凝器连通， 形成以回热式双效为低温 发生流程的第三类吸收式热泵。  69. The third type of absorption heat pump is a third type of absorption heat pump according to any one of items 4, 29-36, adding a new generator, a new solution heat exchanger, and an additional section. Flow valve and new solution pump, the absorption-generator has a dilute solution line connected to the first generator through the first solution heat exchanger to adjust to absorption-generator with dilute solution line first solution heat exchanger and new The increasing solution heat exchanger is connected with the newly added generator, and the newly added generator and the concentrated solution pipeline are connected to the first generator via the new solution pump and the newly added solution heat exchanger, and the first generator has the refrigerant vapor. The passage is connected to the first condenser to be adjusted so that the first generator has a refrigerant vapor passage connected with the newly added generator, and then the new generator is connected, and the refrigerant liquid pipeline is connected to the first condenser via the newly added throttle valve. The generator and the refrigerant vapor passage are in communication with the first condenser to form a third type of absorption heat pump with a regenerative double effect as a low temperature generation process.
70. 第三类吸收式热泵， 是在第 67项所述的第三类吸收式热泵中， 增加新增第二发生 器、新增第二溶液热交换器、 新增第二节流阔和新增第二溶液泵， 吸收-发生器增设稀溶液管 路经新增第二溶液热交换器与新增第二发生器连通， 新增第二发生器还有浓溶液管路经新增 第二溶液泵和新增第二溶液热交换器与吸收-发生器连通，将新增第一发生器有冷剂蒸汽通道 与第一冷凝器连通调整为新增第一发生器有冷剂蒸汽通道与新增第二发生器连通后新增第二 发生器再有冷剂液管路经新增第二节流阀与第一冷凝器连通， 新增第二发生器还有冷剂蒸汽 通道与第一冷凝器连通， 形成以回热式三效为低温发生流程的第三类吸收式热泵。 71. 第三类吸收式热泵， 是在第 68项所述的第三类吸收式热泵中， 增加新增第二发生 器、 新增第二溶液热交换器和新增第二节流阀， 将新增第一发生器有浓溶液管路经第一溶液 泵和新增第一溶液热交换器与第一溶液热交换器连通调整为新增第一发生器有浓溶液管路经 新增第二溶液热交换器与新增第二发生器连通， 新增第二发生器还有浓溶液管路经第一溶液 泵、 新增第二溶液热交换器和新增第一溶液热交换器与第一溶液热交换器连通， 将新增第一 发生器有冷剂蒸汽通道与第一冷凝器连通调整为新增第一发生器有冷剂蒸汽通道与新增第二 发生器连通后新增第二发生器再有冷剂液管路经新增第二节流阀与第一冷凝器连通， 新增第 二发生器还有冷剂蒸汽通道与第一冷凝器连通， 形成以回热式三效为低温发生流程的第三类 吸收式热泵。 70. The third type of absorption heat pump is a third type of absorption heat pump according to item 67, adding a new second generator, adding a second solution heat exchanger, adding a second section of the flow and A second solution pump is added, and an absorption-generator is added to the dilute solution line. The second solution heat exchanger is added to connect with the newly added second generator, and the second generator and the concentrated solution line are added. The two solution pump and the newly added second solution heat exchanger are connected with the absorption-generator, and the newly added first generator has a refrigerant vapor passage connected with the first condenser to adjust the newly added first generator to have a refrigerant vapor passage. After the second generator is connected, the second generator is added, and the refrigerant liquid pipeline is connected with the first condenser through the addition of the second throttle valve, and the second generator and the refrigerant vapor passage are added. The first condenser is connected to form a third type of absorption heat pump in which the regenerative three-effect is a low temperature generation process. 71. The third type of absorption heat pump is a third type of absorption heat pump according to item 68, adding a new second generator, adding a second solution heat exchanger and adding a second throttle valve. Adding a new first generator with a concentrated solution pipeline through the first solution pump and adding a first solution heat exchanger to the first solution heat exchanger to adjust to add a new first generator with a concentrated solution pipeline added The second solution heat exchanger is connected with the newly added second generator, and the second generator and the concentrated solution line are added through the first solution pump, the second solution heat exchanger is added, and the first solution heat exchanger is added. Communicating with the first solution heat exchanger, connecting the newly added first generator refrigerant vapor passage to the first condenser to adjust to add a new first generator having a refrigerant vapor passage and connecting the newly added second generator The second generator further has a refrigerant liquid pipeline connected to the first condenser via a new second throttle valve, and a second generator and a refrigerant vapor passage are connected to the first condenser to form a heat recovery. The third type of absorption heat pump is a third type of low temperature generation process.
72. 第三类吸收式热泵， 是在第 69项所述的第三类吸收式热泵中， 增加新增第二发生 器、新增第二溶液热交换器、 新增第二节流阀和新增第二溶液泵， 将吸收 -发生器有稀溶液管 路经第一溶液热交换器和新增第一溶液热交换器与新增第一发生器连通调整为吸收-发生器 有稀溶液管路经第一溶液热交换器、 新增第一溶液热交换器和新增第二溶液热交换器与新增 第二发生器连通， 新增第二发生器还有浓溶液管路经新增第二溶液泵和新增第二溶液热交换 器与新增第一发生器连通， 将新增第一发生器有冷剂蒸汽通道与第一冷凝器连通调整为新增 第一发生器有冷剂蒸汽通道与新增第二发生器连通后新增第二发生器再有冷剂液管路经新增 第二节流阀与第一冷凝器连通， 新增第二发生器还有冷剂蒸汽通道与第一冷凝器连通， 形成 以回热式三效为低温发生流程的第三类吸收式热泵。  72. The third type of absorption heat pump, in the third type of absorption heat pump described in item 69, adds a new second generator, adds a second solution heat exchanger, adds a second throttle valve, and Adding a second solution pump, adjusting the absorption-generator dilute solution line through the first solution heat exchanger and adding the first solution heat exchanger to the newly added first generator to adjust to the absorption-generator with dilute solution The pipeline is connected to the newly added second generator via the first solution heat exchanger, the newly added first solution heat exchanger and the newly added second solution heat exchanger, and the second generator and the concentrated solution pipeline are newly added. The second solution pump and the newly added second solution heat exchanger are connected with the newly added first generator, and the newly added first generator has a refrigerant vapor channel connected to the first condenser and is adjusted to be a new first generator. The refrigerant vapor channel is connected with the newly added second generator, and the second generator is added, and the refrigerant liquid pipeline is connected with the first condenser through the addition of the second throttle valve, and the second generator is added with cold. The vapor channel of the agent is in communication with the first condenser, and is formed in a regenerative three-effect manner to occur at a low temperature. The third process type absorption heat pump.
73. 第三类吸收式热泵， 是在第 1项所提及的单效-单效第三类吸收式热泵以及第 5-12 内任一第项所述的第三类吸收式热泵中， 增加新增冷剂液泵或新增节流阀、 新增溶液热交换 器和新增吸收-蒸发器，将吸收器有稀溶液管路经第一溶液热交换器与第一发生器连通调整为 吸收器有稀溶液管路经新增溶液热交换器与新增吸收-蒸发器连通， 新增吸收-蒸发器还有稀 溶液管路经第一溶液热交换器与第一发生器连通， 将第一发生器有浓溶液管路经第一溶液泵 和第一溶液热交换器与第二溶液热交换器连通调整为第一发生器有浓溶液管路经第一溶液 泵、 第一溶液热交换器和新增溶液热交换器与第二溶液热交换器连通， 将蒸发器有冷剂蒸汽 通道与吸收器连通调整为蒸发器有冷剂蒸汽通道与新增吸收-蒸发器连通，蒸发器或第一冷凝 器增设冷剂液管路经新增冷剂液泵与新增吸收-蒸发器连通后新增吸收-蒸发器再有冷剂蒸汽 通道与吸收器连通、或第二冷凝器增设冷剂液管路经新增节流阀与新增吸收-蒸发器连通后新 增吸收-蒸发器再有冷剂蒸汽通道与吸收器连通，形成以 1. 5级为低温发生流程的第三类吸收 式热泵。  73. The third type of absorption heat pump is the single-effect single-effect type III absorption heat pump mentioned in item 1 and the third type of absorption heat pump described in any of items 5-12. Add a new refrigerant liquid pump or a new throttle valve, a new solution heat exchanger and a new absorption-evaporator, and adjust the absorber with a dilute solution line through the first solution heat exchanger to the first generator. A dilute solution line for the absorber is connected to the newly added absorption-evaporator via the new solution heat exchanger, and the new absorption-evaporator and the dilute solution line are connected to the first generator via the first solution heat exchanger. The first generator has a concentrated solution pipeline connected to the first solution pump and the first solution heat exchanger and the second solution heat exchanger to adjust the first generator to have a concentrated solution pipeline through the first solution pump, the first solution The heat exchanger and the newly added solution heat exchanger are connected to the second solution heat exchanger, and the evaporator has a refrigerant vapor passage connected to the absorber to adjust the evaporator to have a refrigerant vapor passage and communicate with the newly added absorption-evaporator, and evaporate Or the first condenser adds a refrigerant liquid pipeline through the newly added refrigerant After the liquid pump is connected with the new absorption-evaporator, the absorption-evaporator is added, and then the refrigerant vapor channel is connected with the absorber, or the second condenser is added with the refrigerant liquid pipeline through the newly added throttle valve and newly absorbed- After the evaporator is connected, a new absorption-evaporator is added, and then a refrigerant vapor channel is connected to the absorber to form a third type of absorption heat pump having a flow rate of 1.5.
74. 第三类吸收式热泵， 是在第 1项所提及的单效-单效第三类吸收式热泵以及第 5-12 内任一第项所述的第三类吸收式热泵中， 增加新增溶液热交换器、 新增溶液泵、 新增吸收- 蒸发器、 新增冷剂液泵或新增节流阀， 将浓溶液提供器有浓溶液管路与吸收器连通调整为浓 溶液提供器有浓溶液管路经新增溶液热交换器与新增吸收-蒸发器连通， 新增吸收-蒸发器还 有稀溶液管路经新增溶液泵和新增溶液热交换器与吸收器连通， 将蒸发器有冷剂蒸汽通道与 吸收器连通调整为蒸发器有冷剂蒸汽通道与新增吸收-蒸发器连通，蒸发器或第一冷凝器增设 冷剂液管路经新增冷剂液泵与新增吸收 -蒸发器连通后新增吸收-蒸发器再有冷剂蒸汽通道与 吸收器连通、或第二冷凝器增设冷剂液管路经新增节流阀与新增吸收 -蒸发器连通后新增吸收 -蒸发器再有冷剂蒸汽通道与吸收器连通， 形成以 1. 5级为低温发生流程的第三类吸收式热 泵。 75. 第三类吸收式热泵， 是在第 1项所提及的单效-单效第三类吸收式热泵以及第 5-12 内任一第项所述的第三类吸收式热泵中， 增加新增溶液热交换器、 新增溶液泵、 新增吸收- 蒸发器、 新增冷剂液泵或新增节流阀， 将第一发生器有浓溶液管路经第一溶液泵和第一溶液 热交换器与第二溶液热交换器连通调整为第一发生器有浓溶液管路经第一溶液泵、 第一溶液 热交换器和新增溶液热交换器与新增吸收-蒸发器连通， 新增吸收-蒸发器还有稀溶液管路经 新增溶液泵和新增溶液热交换器与第二溶液热交换器连通， 将蒸发器有冷剂蒸汽通道与吸收 器连通调整为蒸发器有冷剂蒸汽通道与新增吸收 -蒸发器连通，蒸发器或第一冷凝器增设冷剂 液管路经新增冷剂液泵与新增吸收 -蒸发器连通后新增吸收 -蒸发器再有冷剂蒸汽通道与吸收 器连通、 或第二冷凝器增设冷剂液管路经新增节流阀与新增吸收-蒸发器连通后新增吸收-蒸 发器再有冷剂蒸汽通道与吸收器连通， 形成以 1. 5级为低温发生流程的第三类吸收式热泵。 74. The third type of absorption heat pump is the single-effect single-effect third-type absorption heat pump mentioned in item 1 and the third type absorption heat pump according to any one of items 5-12. Add new solution heat exchanger, new solution pump, new absorption-evaporator, new refrigerant liquid pump or new throttle valve, adjust the concentrated solution provider to the concentrated solution line and the absorber to adjust to thick The solution provider has a concentrated solution line connected to the new absorption-evaporator via a new solution heat exchanger, a new absorption-evaporator and a dilute solution line via a new solution pump and a new solution heat exchanger and absorption The device is connected, and the evaporator has a refrigerant vapor channel connected to the absorber to adjust the evaporator to have a refrigerant vapor channel connected with the new absorption-evaporator, and the evaporator or the first condenser adds a refrigerant liquid pipeline through the newly added cold. After the agent liquid pump is connected with the new absorption-evaporator, the absorption-evaporator is added, and then the refrigerant vapor channel is connected with the absorber, or the second condenser is added with the refrigerant liquid pipeline through the newly added throttle valve and newly absorbed. - Adding an absorption-evaporator and then a refrigerant vapor channel and absorber after the evaporator is connected Connected to form a third type of absorption heat pump with a stage of 0.5 low temperature generation. 75. The third type of absorption heat pump is the single-effect single-effect third-type absorption heat pump mentioned in item 1 and the third type absorption heat pump according to any one of items 5-12. Add a new solution heat exchanger, a new solution pump, a new absorption-evaporator, a new refrigerant pump or a new throttle valve, and the first generator has a concentrated solution line through the first solution pump and the first a solution heat exchanger is connected to the second solution heat exchanger to adjust the first generator to have a concentrated solution line through the first solution pump, the first solution heat exchanger and the new solution heat exchanger and the new absorption-evaporator Connected, the new absorption-evaporator and the dilute solution pipeline are connected to the second solution heat exchanger via the new solution pump and the new solution heat exchanger, and the evaporator has a refrigerant vapor passage connected to the absorber to adjust to evaporation. The refrigerant vapor passage is connected with the newly added absorption-evaporator, and the evaporator or the first condenser is added with a refrigerant liquid pipeline. The new refrigerant liquid pump is connected with the new absorption-evaporator to add an absorption-evaporator. Further, the refrigerant vapor passage is connected to the absorber, or the second condenser is provided with a refrigerant liquid. The pipeline is connected to the new absorption-evaporator via a new throttle valve, and then a new absorption-evaporator is connected to the refrigerant vapor passage to communicate with the absorber to form a third type of absorption type with a lower temperature generation process of 1.5. Heat pump.
76. 第三类吸收式热泵， 是在第 1、 13-20项内任一一项所述的第三类吸收式热泵中， 增加新增溶液热交换器、 新增吸收-蒸发器、 新增冷剂液泵或新增节流阀， 将吸收器有稀溶液 管路经第一溶液热交换器与第二吸收器连通调整为吸收器有稀溶液管路经新增溶液热交换器 与新增吸收-蒸发器连通， 新增吸收-蒸发器还有稀溶液管路经第一溶液热交换器与第二吸收 器连通， 将第三发生器有浓溶液管路经第一溶液泵和第一溶液热交换器与第二溶液热交换器 连通调整为第三发生器有浓溶液管路经第一溶液泵、 第一溶液热交换器和新增溶液热交换器 与第二溶液热交换器连通， 将蒸发器有冷剂蒸汽通道与吸收器连通调整为蒸发器有冷剂蒸汽 通道与新增吸收-蒸发器连通，蒸发器或第一冷凝器增设冷剂液管路经新增冷剂液泵与新增吸 收 -蒸发器连通后新增吸收-蒸发器再有冷剂蒸汽通道与吸收器连通、 或第二冷凝器增设冷剂 液管路经新增节流阀与新增吸收-蒸发器连通后新增吸收-蒸发器再有冷剂蒸汽通道与吸收器 连通， 形成以回热式 1. 5级为低温发生流程的第三类吸收式热泵。  76. The third type of absorption heat pump is a third type of absorption heat pump according to any one of items 1, 13-20, adding a new solution heat exchanger, adding an absorption-evaporator, a new a refrigerant liquid pump or a new throttle valve, and the dilute solution pipeline of the absorber is connected to the second absorber through the first solution heat exchanger to adjust the absorber to a dilute solution pipeline through the new solution heat exchanger and A new absorption-evaporator is connected, a new absorption-evaporator and a dilute solution line are connected to the second absorber via the first solution heat exchanger, and the third generator has a concentrated solution line through the first solution pump and The first solution heat exchanger is connected to the second solution heat exchanger to be adjusted to be a third generator having a concentrated solution line through the first solution pump, the first solution heat exchanger and the new solution heat exchanger and the second solution heat exchange The device is connected, and the evaporator has a refrigerant vapor channel connected to the absorber to adjust the evaporator to have a refrigerant vapor channel connected with the new absorption-evaporator, and the evaporator or the first condenser adds a refrigerant liquid pipeline through the newly added cold. Adding absorption after the agent pump is connected to the new absorption-evaporator - the evaporator is further connected with the refrigerant vapor passage and the absorber, or the second condenser is provided with a refrigerant liquid pipeline. After the new throttle valve is connected with the new absorption-evaporator, the absorption-evaporator is added and the refrigerant is added. The steam passage is connected to the absorber to form a third type of absorption heat pump in which the heat recovery type 1.5 is a low temperature generation process.
77. 第三类吸收式热泵， 是在第 1、 13-20项内任一一项所述的第三类吸收式热泵中， 增加新增溶液热交换器、 新增溶液泵、 新增吸收-蒸发器、 新增冷剂液泵或新增节流阀， 将浓 溶液提供器有浓溶液管路与吸收器连通调整为浓溶液提供器有浓溶液管路经新增溶液热交换 器与新增吸收-蒸发器连通， 新增吸收 -蒸发器还有稀溶液管路经新增溶液泵和新增溶液热交 换器与吸收器连通， 将蒸发器有冷剂蒸汽通道与吸收器连通调整为蒸发器有冷剂蒸汽通道与 新增吸收-蒸发器连通， 蒸发器或第一冷凝器增设冷剂液管路经新增冷剂液泵与新增吸收-蒸 发器连通后新增吸收 -蒸发器再有冷剂蒸汽通道与吸收器连通、或第二冷凝器增设冷剂液管路 经新增节流阀与新增吸收 -蒸发器连通后新增吸收-蒸发器再有冷剂蒸汽通道与吸收器连通， 形成以回热式 1. 5级为低温发生流程的第三类吸收式热泵。  77. The third type of absorption heat pump is a third type of absorption heat pump according to any one of items 1, 13-20, adding a new solution heat exchanger, adding a new solution pump, and newly adding absorption. - evaporator, new refrigerant liquid pump or new throttle valve, connect the concentrated solution provider with concentrated solution line and absorber to adjust the concentrated solution to the thick solution line through the new solution heat exchanger and New absorption-evaporator connection, new absorption-evaporator and dilute solution line are connected to the absorber through the new solution pump and the new solution heat exchanger, and the evaporator has a refrigerant vapor channel connected to the absorber. There is a refrigerant vapor channel for the evaporator to communicate with the new absorption-evaporator, and the evaporator or the first condenser is provided with a refrigerant liquid pipeline. The new refrigerant liquid pump is connected with the new absorption-evaporator to add absorption. The evaporator is further connected with the refrigerant vapor passage and the absorber, or the second condenser is connected with the refrigerant liquid pipeline. After the new throttle valve is connected with the new absorption-evaporator, the absorption-evaporator is added and the refrigerant vapor is added. 5级低低。 The channel is connected to the absorber, the formation is in the form of a regenerative type 1. A third process occurs absorption heat pump.
78. 第三类吸收式热泵， 是在第 1、 13-20项内任一一项所述的第三类吸收式热泵中， 增加新增溶液热交换器、 新增溶液泵、 新增吸收-蒸发器、 新增冷剂液泵或新增节流阀， 将第 三发生器有浓溶液管路经第一溶液泵和第一溶液热交换器与第二溶液热交换器连通调整为第 三发生器有浓溶液管路经第一溶液泵、 第一溶液热交换器和新增溶液热交换器与新增吸收- 蒸发器连通，新增吸收-蒸发器还有稀溶液管路经新增溶液泵和新增溶液热交换器与第二溶液 热交换器连通， 将蒸发器有冷剂蒸汽通道与吸收器连通调整为蒸发器有冷剂蒸汽通道与新增 吸收-蒸发器连通， 蒸发器或第一冷凝器增设冷剂液管路经新增冷剂液泵与新增吸收-蒸发器 连通后新增吸收-蒸发器再有冷剂蒸汽通道与吸收器连通、或第二冷凝器增设冷剂液管路经新 增节流阀与新增吸收 -蒸发器连通后新增吸收-蒸发器再有冷剂蒸汽通道与吸收器连通， 形成 以回热式 1. 5级为低温发生流程的第三类吸收式热泵。 79. 第三类吸收式热泵， 是在第 2-3、 21-28项内任一一所述且无第二蒸发器的第三类 吸收式热泵中， 取消第三溶液泵 21， 吸收器 3有稀溶液管路经第三溶液热交换器 15与吸收- 发生器 16连通； 增加新增冷剂液泵或新增节流阀， 取消第一蒸发器与吸收器连通的冷剂蒸汽 通道， 第一冷凝器或蒸发器增设冷剂液管路经新增冷剂液泵与吸收-发生器连通后吸收-发生 器还有冷剂蒸汽通道与吸收器连通、或第二冷凝器增设冷剂液管路经新增节流阀与新增吸收- 蒸发器连通后新增吸收-蒸发器再有冷剂蒸汽通道与吸收器连通，形成以回热式 1. 5级为低温 发生流程的第三类吸收式热泵。 78. The third type of absorption heat pump is the third type of absorption heat pump according to any one of items 1, 13-20, adding a new solution heat exchanger, adding a new solution pump, and newly adding absorption. - an evaporator, a new refrigerant liquid pump or a new throttle valve, and the third generator has a concentrated solution line connected to the first solution pump and the first solution heat exchanger and the second solution heat exchanger to adjust to The three generators have a concentrated solution line connected to the new absorption-evaporator via the first solution pump, the first solution heat exchanger and the new solution heat exchanger, and a new absorption-evaporator and a dilute solution line are newly added. The solution pump and the new solution heat exchanger are connected to the second solution heat exchanger, and the evaporator has a refrigerant vapor channel connected to the absorber to adjust the evaporator to have a refrigerant vapor channel and communicate with the newly added absorption-evaporator, and evaporate Adding a coolant liquid line to the first condenser or the new absorption liquid evaporator through the newly added refrigerant liquid pump, adding an absorption-evaporator and then having a refrigerant vapor passage communicating with the absorber, or the second condenser Additional coolant line is connected to the new absorption-evaporator via a new throttle valve After the addition of the absorption-evaporator and then the refrigerant vapor channel is connected to the absorber, forming a third type of absorption heat pump with a regenerative type 1.5 low temperature generation process. 79. The third type of absorption heat pump, in the third type of absorption heat pump described in any of items 2-3, 21-28 and without the second evaporator, cancels the third solution pump 21, the absorber 3 The dilute solution pipeline is connected to the absorption-generator 16 via the third solution heat exchanger 15; the new refrigerant liquid pump or the new throttle valve is added to cancel the refrigerant vapor passage connecting the first evaporator and the absorber The first condenser or the evaporator is provided with a refrigerant liquid pipeline connected to the absorption-generator through the newly added refrigerant liquid pump, the absorption-generator and the refrigerant vapor passage are connected to the absorber, or the second condenser is cooled. The liquid-liquid pipeline is connected to the newly-added absorption-evaporator, and then the absorption-evaporator is connected to the refrigerant vapor channel and the absorber is connected to form a regenerative type 1.5. The third type of absorption heat pump.
80. 第三类吸收式热泵， 是在第 2-3、 21-28项内任一一项所述的第三类吸收式热泵中， 增加新增吸收 -蒸发器、 新增冷剂液泵或新增节流阀， 将吸收-发生器有稀溶液管路经第一溶 液热交换器与第一发生器连通调整为吸收-发生器有稀溶液管路直接与新增吸收-蒸发器连 通， 新增吸收-蒸发器还有稀溶液管路经第一溶液热交换器与第一发生器连通， 将第一蒸发器 有冷剂蒸汽通道与吸收器连通调整为第一蒸发器有冷剂蒸汽通道与新增吸收 -蒸发器连通，第 一冷凝器或第一蒸发器增设冷剂液管路经新增冷剂液泵与吸收 -发生器连通后吸收-发生器还 有冷剂蒸汽通道与吸收器连通、或第二冷凝器增设冷剂液管路经新增节流阀与新增吸收 -蒸发 器连通后新增吸收-蒸发器再有冷剂蒸汽通道与吸收器连通，形成以回热式 1. 5级为低温发生 流程的第三类吸收式热泵。  80. The third type of absorption heat pump is a third type of absorption heat pump according to any one of items 2-3, 21-28, adding a new absorption-evaporator and a new refrigerant liquid pump. Or a new throttle valve, the absorption-generator has a dilute solution line connected to the first generator through the first solution heat exchanger to adjust to absorption - the generator has a dilute solution line directly connected to the new absorption-evaporator a new absorption-evaporator and a dilute solution line are connected to the first generator via the first solution heat exchanger, and the first evaporator has a refrigerant vapor passage connected to the absorber to adjust the first evaporator to have a refrigerant The steam passage is connected to the newly added absorption-evaporator, and the first condenser or the first evaporator adds a refrigerant liquid pipeline through the newly added refrigerant liquid pump and the absorption-generator, and the absorption-generator and the refrigerant vapor passage Connected to the absorber, or the second condenser is added with a refrigerant liquid pipeline. After the new throttle valve is connected with the new absorption-evaporator, a new absorption-evaporator is connected, and then a refrigerant vapor passage is connected with the absorber to form The regenerative type 1. 5 is the third type of absorption heat pump for the low temperature generation process.
81. 第三类吸收式热泵， 是在第 2-3、 21- 28项内任一一项所述的第三类吸收式热泵中， 增加新增溶液热交换器、 新增溶液泵、 新增吸收-蒸发器、 新增冷剂液泵或新增节流阀， 将浓 溶液提供器有浓溶液管路与吸收器连通调整为浓溶液提供器有浓溶液管路经新增溶液热交换 器与新增吸收-蒸发器连通， 新增吸收-蒸发器还有稀溶液管路经新增溶液泵和新增溶液热交 换器与吸收器连通， 将第一蒸发器有冷剂蒸汽通道与吸收器连通调整为第一蒸发器有冷剂蒸 汽通道与新增吸收-蒸发器连通，第一蒸发器或第一冷凝器增设冷剂液管路经新增冷剂液泵与 新增吸收-蒸发器连通后新增吸收-蒸发器再有冷剂蒸汽通道与吸收器连通、 或第二冷凝器增 设冷剂液管路经新增节流阀与新增吸收-蒸发器连通后新增吸收-蒸发器再有冷剂蒸汽通道与 吸收器连通， 形成以回热式 1. 5级为低温发生流程的第三类吸收式热泵。  81. The third type of absorption heat pump is a third type of absorption heat pump according to any one of items 2-3, 21-28, adding a new solution heat exchanger, a new solution pump, a new one. Adding absorption-evaporator, adding refrigerant liquid pump or adding new throttle valve, connecting concentrated solution provider with concentrated solution line and absorber to adjust to concentrated solution provider with concentrated solution line through new solution heat exchange The device is connected with the new absorption-evaporator, and the new absorption-evaporator and the dilute solution pipeline are connected to the absorber through the new solution pump and the new solution heat exchanger, and the first evaporator has a refrigerant vapor channel and The absorber is adjusted to be connected to the first evaporator with a refrigerant vapor passage communicating with the newly added absorption-evaporator, and the first evaporator or the first condenser is provided with a refrigerant liquid pipeline via a newly added refrigerant liquid pump and newly absorbed - After the evaporator is connected, the absorption-evaporator is added, and then the refrigerant vapor channel is connected with the absorber, or the second condenser is added with the refrigerant liquid pipeline. After the new throttle valve is connected with the new absorption-evaporator, the absorption is newly added. - the evaporator has a refrigerant vapor channel connected to the absorber to form a heat recovery Equation 1. Class 5 is the third type of absorption heat pump for the low temperature generation process.
82. 第三类吸收式热泵， 是在第 2-3、 21-28项内任一一项所述的第三类吸收式热泵中， 增加新增溶液热交换器、 新增溶液泵、 新增吸收-蒸发器、 新增冷剂液泵或新增节流阀， 将分 汽室有浓溶液管路经第二溶液泵和第三溶液热交换器与第二溶液热交换器连通调整为分汽室 有浓溶液管路经第二溶液泵、 第三溶液热交换器和新增溶液热交换器与新增吸收-蒸发器连 通，新增吸收-蒸发器还有稀溶液管路经新增溶液泵和新增溶液热交换器与第二溶液热交换器 连通， 将第一蒸发器有冷剂蒸汽通道与吸收器连通调整为第一蒸发器有冷剂蒸汽通道与新增 吸收-蒸发器连通， 蒸发器或第一冷凝器增设冷剂液管路经新增冷剂液泵与新增吸收-蒸发器 连通后新增吸收-蒸发器再有冷剂蒸汽通道与吸收器连通、或第二冷凝器增设冷剂液管路经新 增节流阔与新增吸收 -蒸发器连通后新增吸收-蒸发器再有冷剂蒸汽通道与吸收器连通， 形成 以回热式 1. 5级为低温发生流程的第三类吸收式热泵。  82. The third type of absorption heat pump is a third type of absorption heat pump according to any one of items 2-3, 21-28, adding a new solution heat exchanger, adding a new solution pump, new The absorption-evaporator, the newly added refrigerant liquid pump or the newly added throttle valve adjusts the concentrated solution line in the steam distribution chamber through the second solution pump and the third solution heat exchanger to the second solution heat exchanger to The steam distribution chamber has a concentrated solution pipeline connected to the new absorption-evaporator via the second solution pump, the third solution heat exchanger and the new solution heat exchanger, and the new absorption-evaporator and the dilute solution pipeline are newly added. The increasing solution pump and the new solution heat exchanger are in communication with the second solution heat exchanger, and the first evaporator has a refrigerant vapor channel connected to the absorber to adjust the first evaporator to have a refrigerant vapor channel and a new absorption-evaporation Connected to the evaporator or the first condenser to add a refrigerant liquid pipeline. After the new refrigerant liquid pump is connected with the new absorption-evaporator, a new absorption-evaporator is connected, and then the refrigerant vapor passage is connected to the absorber, or The second condenser adds a refrigerant liquid pipeline through a new throttle and a new absorption-steaming After the communication is new absorber - evaporator, then the refrigerant vapor passage in communication with the absorbent, to form a regenerative heat process occurring level 1.5 third category is the low temperature absorption heat pump.
83. 第三类吸收式热泵， 是在第 4、 29- 36项内任一一项所述的第三类吸收式热泵中， 增加新增溶液热交换器、 新增吸收-蒸发器、 新增冷剂液泵或新增节流阀， 将吸收器有稀溶液 管路经第三溶液热交换器和吸收-发生器与分汽室连通调整为吸收器有稀溶液管路经新增溶 液热交换器与新增吸收-蒸发器连通， 新增吸收-蒸发器还有稀溶液管路经第三溶液热交换器 和吸收-发生器与分汽室连通，将第二溶液泵有浓溶液管路经第三溶液热交换器与第二溶液热 交换器连通调整为第二溶液泵有浓溶液管路经第三溶液热交换器和新增溶液热交换器与第二 溶液热交换器连通， 将第二蒸发器有冷剂蒸汽通道与吸收器连通调整为第二蒸发器有冷剂蒸 汽通道与新增吸收-蒸发器连通，第三冷凝器或第二蒸发器增设冷剂液管路经新增冷剂液泵与 新增吸收 -蒸发器连通后新增吸收-蒸发器再有冷剂蒸汽通道与吸收器连通、 或第二冷凝器增 设冷剂液管路经新增节流阀与新增吸收-蒸发器连通后新增吸收-蒸发器再有冷剂蒸汽通道与 吸收器连通， 以回热式 1. 5级为低温发生流程的第三类吸收式热泵。 83. The third type of absorption heat pump is a third type of absorption heat pump according to any one of items 4, 29-36, adding a new solution heat exchanger, adding an absorption-evaporator, a new The refrigerant liquid pump or the newly added throttle valve, the diluted solution pipeline of the absorber is connected to the steam distribution chamber through the third solution heat exchanger and the absorption-generator and the steam distribution chamber to adjust the absorber to have a dilute solution pipeline through the new solution The heat exchanger is connected to the newly added absorption-evaporator, and the new absorption-evaporator and the dilute solution pipeline are connected to the steam distribution chamber through the third solution heat exchanger and the absorption-generator, and the second solution pump has a concentrated solution. The pipeline passes through the third solution heat exchanger and the second solution heat The exchanger is connected to the second solution pump, and the concentrated solution pipeline is connected to the second solution heat exchanger via the third solution heat exchanger and the new solution heat exchanger, and the second evaporator has a refrigerant vapor passage and an absorber. The connection adjustment is such that the second evaporator has a refrigerant vapor passage communicating with the newly added absorption-evaporator, and the third condenser or the second evaporator is provided with a refrigerant liquid pipeline via the newly added refrigerant liquid pump and the newly added absorption-evaporator After the connection, the absorption-evaporator is added, and then the refrigerant vapor channel is connected with the absorber, or the second condenser is added with the refrigerant liquid pipeline. After the new throttle valve is connected with the new absorption-evaporator, the absorption-evaporation is newly added. The refrigerant flow channel is connected to the absorber, and the third type of absorption heat pump is a regenerative type 1.5 low temperature generating process.
84. 第三类吸收式热泵， 是在第 4、 29- 36项内任一一项所述的第三类吸收式热泵中， 增加新增溶液热交换器、 新增溶液泵、 新增吸收-蒸发器、 新增冷剂液泵或新增节流阀， 将浓 溶液提供器有浓溶液管路与吸收器连通调整为浓溶液提供器有浓溶液管路经新增溶液热交换 器与新增吸收-蒸发器连通， 新增吸收 -蒸发器还有稀溶液管路经新增溶液泵和新增溶液热交 换器与吸收器连通， 将第二蒸发器有冷剂蒸汽通道与吸收器连通调整为第二蒸发器有冷剂蒸 汽通道与新增吸收-蒸发器连通，第三冷凝器或第二蒸发器增设冷剂液管路经新增冷剂液泵与 新增吸收 -蒸发器连通后新增吸收-蒸发器再有冷剂蒸汽通道与吸收器连通、 或第二冷凝器增 设冷剂液管路经新增节流阀与新增吸收 -蒸发器连通后新增吸收-蒸发器再有冷剂蒸汽通道与 吸收器连通， 形成以回热式 1. 5级为低温发生流程的第三类吸收式热泵。  84. The third type of absorption heat pump is a third type of absorption heat pump according to any one of items 4, 29-36, adding a new solution heat exchanger, adding a new solution pump, and newly adding absorption. - evaporator, new refrigerant liquid pump or new throttle valve, connect the concentrated solution provider with concentrated solution line and absorber to adjust the concentrated solution to the thick solution line through the new solution heat exchanger and A new absorption-evaporator connection is added, a new absorption-evaporator and a dilute solution line are connected to the absorber via a new solution pump and a new solution heat exchanger, and the second evaporator has a refrigerant vapor channel and an absorber. The connection adjustment is such that the second evaporator has a refrigerant vapor passage communicating with the newly added absorption-evaporator, and the third condenser or the second evaporator is provided with a refrigerant liquid pipeline via the newly added refrigerant liquid pump and the newly added absorption-evaporator After the connection, the absorption-evaporator is added, and then the refrigerant vapor channel is connected with the absorber, or the second condenser is added with the refrigerant liquid pipeline. After the new throttle valve is connected with the new absorption-evaporator, the absorption-evaporation is newly added. The refrigerant vapor passage is connected to the absorber to form a back 1.5 The third type absorption heat pump using a low temperature process occurs.
85. 第三类吸收式热泵， 是在第 4、 29-36项内任一一项所述的第三类吸收式热泵中， 增加新增溶液热交换器、 新增溶液泵、 新增吸收-蒸发器、 新增冷剂液泵或新增节流阀， 将分 汽室有浓溶液管路经第二溶液泵和第三溶液热交换器与第二溶液热交换器连通调整为分汽室 有浓溶液管路经第二溶液泵、 第三溶液热交换器和新增溶液热交换器与新增吸收-蒸发器连 通，新增吸收-蒸发器还有稀溶液管路经新增溶液泵和新增溶液热交换器与第二溶液热交换器 连通， 将第二蒸发器有冷剂蒸汽通道与吸收器连通调整为第二蒸发器有冷剂蒸汽通道与新增 吸收-蒸发器连通， 第三冷凝器或第二蒸发器增设冷剂液管路经新增冷剂液泵与新增吸收-蒸 发器连通后新增吸收 -蒸发器再有冷剂蒸汽通道与吸收器连通、或第二冷凝器增设冷剂液管路 经新增节流阀与新增吸收 -蒸发器连通后新增吸收-蒸发器再有冷剂蒸汽通道与吸收器连通， 形成以回热式 1. 5级为低温发生流程的第三类吸收式热泵。  The third type of absorption heat pump is a third type of absorption heat pump according to any one of items 4, 29-36, adding a new solution heat exchanger, adding a new solution pump, and newly adding absorption. - an evaporator, a new refrigerant liquid pump or a new throttle valve, and the concentrated solution line in the steam distribution chamber is connected to the second solution heat exchanger and the second solution heat exchanger via the second solution pump and the second solution heat exchanger to adjust the steam separation The concentrated solution line in the chamber is connected to the newly added absorption-evaporator via the second solution pump, the third solution heat exchanger and the new solution heat exchanger, and the new absorption-evaporator and the dilute solution line are added through the new solution. The pump and the new solution heat exchanger are in communication with the second solution heat exchanger, and the second evaporator has a refrigerant vapor passage connected to the absorber to be adjusted to a second evaporator having a refrigerant vapor passage connected to the newly added absorption-evaporator , the third condenser or the second evaporator is added with a refrigerant liquid pipeline, and the new refrigerant liquid pump is connected with the new absorption-evaporator, and then the absorption-vaporizer is connected, and then the refrigerant vapor channel is connected with the absorber, or The second condenser adds a refrigerant liquid pipeline through the addition of a new throttle valve and new absorption - After the evaporator is connected, a new absorption-evaporator is connected, and then a refrigerant vapor channel is connected with the absorber to form a third type of absorption heat pump with a regenerative type 1.5 as a low temperature generation process.
86. 第三类吸收式热泵， 是在第 4、 29-36项内任一一项所述的第三类吸收式热泵中， 增加新增溶液热交换器、 新增吸收-蒸发器和新增冷剂液泵， 将吸收 -发生器有稀溶液管路经 第一溶液热交换器与第一发生器连通调整为吸收-发生器有稀溶液管路经第一溶液热交换器 与新增吸收-蒸发器连通， 新增吸收-蒸发器还有稀溶液管路经新增溶液热交换器与第一发生 器连通，将第一发生器有浓溶液管路经第一溶液泵和第一溶液热交换器与吸收-发生器连通调 整为第一发生器有浓溶液管路经第一溶液泵、新增溶液热交换器和第一溶液热交换器与吸收- 发生器连通，将第一蒸发器有冷剂蒸汽通道与吸收-发生器连通调整为第一蒸发器有冷剂蒸汽 通道与新增吸收-蒸发器连通， 第一冷凝器或第一蒸发器增设冷剂液管路经新增吸收-蒸发器 连通后新增吸收-蒸发器还有冷剂蒸汽通道与吸收-发生器连通， 形成以回热式 1. 5级为低温 发生流程的第三类吸收式热泵。  The third type of absorption heat pump is a third type of absorption heat pump according to any one of items 4, 29-36, adding a new solution heat exchanger, adding an absorption-evaporator and a new one. a refrigerant pump, the absorption-generator has a dilute solution line connected to the first generator through the first solution heat exchanger to adjust to absorption-the generator has a dilute solution line through the first solution heat exchanger and newly added The absorption-evaporator is connected, the new absorption-evaporator and the dilute solution pipeline are connected to the first generator via the new solution heat exchanger, and the first generator has a concentrated solution pipeline through the first solution pump and the first The solution heat exchanger is connected to the absorption-generator to adjust the first generator to have a concentrated solution line through the first solution pump, the new solution heat exchanger and the first solution heat exchanger to communicate with the absorption-generator, which will be first The evaporator has a refrigerant vapor passage and an absorption-generator connection, and the first evaporator has a refrigerant vapor passage connected with the new absorption-evaporator, and the first condenser or the first evaporator adds a refrigerant liquid pipeline through the new Increased absorption-evaporator connection, new absorption-evaporator and cold The agent vapor channel is connected to the absorption-generator to form a third type of absorption heat pump with a regenerative type 1.5 low temperature generation process.
87. 第三类吸收式热泵， 是在第 4、 29-36项内任一一项所述的第三类吸收式热泵中， 增加新增溶液热交换器、 新增溶液泵、 新增吸收 -蒸发器和新增冷剂液泵， 将第一发生器有浓 溶液管路经第一溶液泵和第一溶液热交换器与吸收-发生器连通调整为第一发生器有浓溶液 管路经第一溶液泵和第一溶液热交换器与新增吸收-蒸发器连通， 新增吸收-蒸发器还有稀溶 液管路经新增溶液泵和新增溶液热交换器与吸收-发生器连通， 将吸收-发生器有稀溶液管路 经第一溶液热交换器与第一发生器连通调整为吸收-发生器有稀溶液管路经新增溶液热交换 器和第一溶液热交换器与第一发生器连通，将第一蒸发器有冷剂蒸汽通道与吸收 -发生器连通 调整为第一蒸发器有冷剂蒸汽通道与新增吸收-蒸发器连通，第一冷凝器或第一蒸发器增设冷 剂液管路经新增吸收 -蒸发器连通后新增吸收-蒸发器还有冷剂蒸汽通道与吸收-发生器连通， 形成以回热式 1. 5级为低温发生流程的第三类吸收式热泵。 87. The third type of absorption heat pump is a third type of absorption heat pump according to any one of items 4, 29-36, adding a new solution heat exchanger, adding a new solution pump, and newly adding absorption. - an evaporator and a new refrigerant liquid pump, the first generator has a concentrated solution line connected to the first solution pump and the first solution heat exchanger and the absorption-generator to adjust the first generator to have a concentrated solution line The first solution pump and the first solution heat exchanger are connected to the newly added absorption-evaporator, and the new absorption-evaporator and the dilute solution pipeline are added to the new solution pump and the new solution heat exchanger and the absorption-generator. Connected, the absorption-generator has a dilute solution line The first solution heat exchanger is connected to the first generator to be adjusted to be an absorption-generator having a dilute solution line connected to the first generator via the new solution heat exchanger and the first solution heat exchanger, and the first evaporator is The refrigerant vapor passage and the absorption-generator are connected to each other to adjust the first evaporator to have a refrigerant vapor passage communicating with the new absorption-evaporator, and the first condenser or the first evaporator to add a refrigerant liquid pipeline is newly absorbed. - After the evaporator is connected, a new absorption-evaporator and a refrigerant vapor channel are connected to the absorption-generator to form a third type of absorption heat pump in which the regenerative type 1.5 is a low temperature generation process.
附图说明： BRIEF DESCRIPTION OF THE DRAWINGS:
图 1是单效 -单效第三类吸收式热泵结构和流程图  Figure 1 is a single-effect single-effect third-class absorption heat pump structure and flow chart
图 2是依据本发明所提供的单效 -回热式单效第三类吸收式热泵第 1种结构和流程图。 图 3是依据本发明所提供的单效 -回热式单效第三类吸收式热泵第 2种结构和流程图。 图 4是依据本发明所提供的单效 -回热式单效第三类吸收式热泵第 3种结构和流程图。 图 5是依据本发明所提供的单效 -回热式单效第三类吸收式热泵第 4种结构和流程图。 图 6是依据本发明所提供的单效 -回热式单效第三类吸收式热泵第 5种结构和流程图。 图 7是依据本发明所提供的双效 -单效第三类吸收式热泵第 1种结构和流程图。  2 is a first configuration and flow diagram of a single-effect-recovery single-effect third-class absorption heat pump according to the present invention. Figure 3 is a second construction and flow diagram of a single-effect-recovery single-effect third-class absorption heat pump according to the present invention. Figure 4 is a third construction and flow diagram of a single-effect-recovery single-effect third-class absorption heat pump according to the present invention. Figure 5 is a fourth configuration and flow diagram of a single-effect-recovery single-effect third-class absorption heat pump according to the present invention. Figure 6 is a fifth configuration and flow diagram of a single-effect-recovery single-effect third-class absorption heat pump according to the present invention. Figure 7 is a first construction and flow diagram of a double-effect-single-effect third-type absorption heat pump according to the present invention.
图 8是依据本发明所提供的双效 -单效第三类吸收式热泵第 2种结构和流程图。  Figure 8 is a second construction and flow diagram of a double effect-single effect third type absorption heat pump provided in accordance with the present invention.
图 9是依据本发明所提供的双效 -单效第三类吸收式热泵第 3种结构和流程图。  Figure 9 is a third construction and flow diagram of a double-effect-single-effect third-type absorption heat pump according to the present invention.
图 10是依据本发明所提供的三效 -单效第三类吸收式热泵第 1种结构和流程图。  Figure 10 is a first construction and flow diagram of a three-effect-single-effect third-type absorption heat pump according to the present invention.
图 11是依据本发明所提供的三效 -单效第三类吸收式热泵第 2种结构和流程图。  Figure 11 is a second construction and flow diagram of a three-effect-single-effect third-type absorption heat pump according to the present invention.
图 12是依据本发明所提供的三效 -单效第三类吸收式热泵第 3种结构和流程图。  Figure 12 is a third construction and flow diagram of a three-effect-single-effect third-type absorption heat pump according to the present invention.
图 13是依据本发明所提供的单效 -双效第三类吸收式热泵第 1种结构和流程图。  Figure 13 is a first construction and flow diagram of a single-effect, double-effect, third-class absorption heat pump in accordance with the present invention.
图 14是依据本发明所提供的单效 -双效第三类吸收式热泵第 2种结构和流程图。  Figure 14 is a second construction and flow diagram of a single-effect, double-effect, third-class absorption heat pump in accordance with the present invention.
图 15是依据本发明所提供的单效 -双效第三类吸收式热泵第 3种结构和流程图。  Figure 15 is a third construction and flow diagram of a single-effect, double-effect, third-class absorption heat pump in accordance with the present invention.
图 16是依据本发明所提供的单效 -三效第三类吸收式热泵第 1种结构和流程图。  Figure 16 is a first construction and flow diagram of a single-effect - three-effect third type absorption heat pump according to the present invention.
图 17是依据本发明所提供的单效 -三效第三类吸收式热泵第 2种结构和流程图。  Figure 17 is a second construction and flow diagram of a single-effect three-effect third type absorption heat pump according to the present invention.
图 18是依据本发明所提供的单效 -三效第三类吸收式热泵第 3种结构和流程图。  Figure 18 is a third construction and flow diagram of a single-effect three-effect third type absorption heat pump according to the present invention.
图 19是依据本发明所提供的单效 -回热式双效第三类吸收式热泵第 1种结构和流程图。 图 20是依据本发明所提供的单效 -回热式双效第三类吸收式热泵第 2种结构和流程图。 图 21是依据本发明所提供的单效 -回热式双效第三类吸收式热泵第 3种结构和流程图。 图 22是依据本发明所提供的单效 -回热式双效第三类吸收式热泵第 4种结构和流程图。 图 23是依据本发明所提供的单效 -回热式双效第三类吸收式热泵第 5种结构和流程图。 图 24是依据本发明所提供的单效 -回热式双效第三类吸收式热泵第 6种结构和流程图。 图 25是依据本发明所提供的单效 -回热式双效第三类吸收式热泵第 7种结构和流程图。 图 26是依据本发明所提供的单效 -回热式双效第三类吸收式热泵第 8种结构和流程图。 图 27是依据本发明所提供的单效 -回热式双效第三类吸收式热泵第 9种结构和流程图。 图 38是依据本发明所提供的单效 -回热式双效第三类吸收式热泵第 10种结构和流程图。 图 29是依据本发明所提供的单效 -回热式三效第三类吸收式热泵第 1种结构和流程图。 图 30是依据本发明所提供的单效 -回热式三效第三类吸收式热泵第 2种结构和流程图。 图 31是依据本发明所提供的单效 -回热式三效第三类吸收式热泵第 3种结构和流程图。 图 32是依据本发明所提供的单效 -回热式三效第三类吸收式热泵第 4种结构和流程图。 图 33是依据本发明所提供的单效 -回热式三效第三类吸收式热泵第 5种结构和流程图。 图 34是依据本发明所提供的单效 -回热式三效第三类吸收式热泵第 6种结构和流程图。 图 35是依据本发明所提供的单效 -回热式三效第三类吸收式热泵第 7种结构和流程图。 图 36是依据本发明所提供的单效 -回热式三效第三类吸收式热泵第 8种结构和流程图。 图 37是依据本发明所提供的单效 -回热式三效第三类吸收式热泵第 9种结构和流程图。 图 38是依据本发明所提供的单效 -回热式三效第三类吸收式热泵第 10种结构和流程图。 图 39是依据本发明所提供的单效 -回热式三效第三类吸收式热泵第 11种结构和流程图。 图 40是依据本发明所提供的单效 -回热式三效第三类吸收式热泵第 12种结构和流程图。 图 41是依据本发明所提供的单效 -1. 5级第三类吸收式热泵第 1种结构和流程图。 Figure 19 is a first configuration and flow diagram of a single-effect-recovery double-effect third-class absorption heat pump according to the present invention. Figure 20 is a second construction and flow diagram of a single-effect-recovery double-effect third-class absorption heat pump according to the present invention. Figure 21 is a third configuration and flow diagram of a single-effect-recovery double-effect third-class absorption heat pump according to the present invention. Figure 22 is a fourth configuration and flow diagram of a single-effect-recovery double-effect third-class absorption heat pump according to the present invention. Figure 23 is a fifth configuration and flow diagram of a single-effect-recovery double-effect third-class absorption heat pump according to the present invention. Figure 24 is a sixth configuration and flow diagram of a single-effect-recovery double-effect third-class absorption heat pump according to the present invention. Figure 25 is a seventh configuration and flow diagram of a single-effect-recovery double-effect third-class absorption heat pump according to the present invention. Figure 26 is a diagram showing the eighth structure and flow chart of a single-effect-recovery double-effect third-class absorption heat pump according to the present invention. Figure 27 is a ninth configuration and flow diagram of a single-effect-recovery double-effect third-class absorption heat pump according to the present invention. Figure 38 is a tenth configuration and flow diagram of a single-effect-recovery double-effect third-class absorption heat pump according to the present invention. Figure 29 is a first configuration and flow diagram of a single-effect-recovery three-effect third-class absorption heat pump according to the present invention. Figure 30 is a second construction and flow diagram of a single-effect-recovery three-effect third-class absorption heat pump according to the present invention. Figure 31 is a third configuration and flow diagram of a single-effect-recovery three-effect third-class absorption heat pump according to the present invention. Figure 32 is a fourth configuration and flow diagram of a single-effect-recovery three-effect third-class absorption heat pump according to the present invention. Figure 33 is a fifth configuration and flow diagram of a single-effect-recovery three-effect third-class absorption heat pump according to the present invention. Figure 34 is a sixth configuration and flow diagram of a single-effect-recovery three-effect third-class absorption heat pump according to the present invention. Figure 35 is a seventh configuration and flow diagram of a single-effect-recovery three-effect third-class absorption heat pump according to the present invention. Figure 36 is a diagram showing the eighth structure and flow chart of a single-effect-recovery three-effect third-class absorption heat pump according to the present invention. Figure 37 is a ninth configuration and flow diagram of a single-effect-recovery three-effect third-class absorption heat pump according to the present invention. Figure 38 is a tenth configuration and flow diagram of a single-effect-recovery three-effect third-class absorption heat pump according to the present invention. Figure 39 is a diagram showing the eleventh structure and flow chart of a single-effect-recovery three-effect third-class absorption heat pump according to the present invention. Figure 40 is a twelfth structure and flow chart of a single-effect-recovery three-effect third-class absorption heat pump according to the present invention. Figure 41 is a first configuration and flow diagram of a single-acting-1. 5 third-class absorption heat pump according to the present invention.
图 42是依据本发明所提供的单效 -1. 5级第三类吸收式热泵第 2种结构和流程图。  Figure 42 is a second construction and flow diagram of a single-effect -1.5 class third type absorption heat pump provided in accordance with the present invention.
图 43是依据本发明所提供的单效 -1. 5级第三类吸收式热泵第 3种结构和流程图。  Figure 43 is a third construction and flow diagram of a single-effect -1.5 primary absorption heat pump according to the present invention.
图 44是依据本发明所提供的单效-回热式 1. 5级第三类吸收式热泵第 1种结构和流程图。 图 45是依据本发明所提供的单效-回热式 1. 5级第三类吸收式热泵第 2种结构和流程图。 图 46是依据本发明所提供的单效-回热式 1. 5级第三类吸收式热泵第 3种结构和流程图。 图 47是依据本发明所提供的单效-回热式 1. 5级第三类吸收式热泵第 4种结构和流程图。 图 48是依据本发明所提供的单效-回热式 1. 5级第三类吸收式热泵第 5种结构和流程图。 图 49是依据本发明所提供的单效-回热式 1. 5级第三类吸收式热泵第 6种结构和流程图。 图 50是依据本发明所提供的单效-回热式 1. 5级第三类吸收式热泵第 7种结构和流程图。 图 51是依据本发明所提供的单效-回热式 1. 5级第三类吸收式热泵第 8种结构和流程图。 图 52是依据本发明所提供的单效-回热式 1. 5级第三类吸收式热泵第 9种结构和流程图。 图 53是依据本发明所提供的单效-回热式 1. 5级第三类吸收式热泵第 10种结构和流程图。 图 54是依据本发明所提供的单效-回热式 1. 5级第三类吸收式热泵第 11种结构和流程图。 图 55是依据本发明所提供的单效-回热式 1. 5级第三类吸收式热泵第 12种结构和流程图。 图中， 1一第一发生器， 2—第二发生器， 3—吸收器 /第一吸收器， 4一第一冷凝器， 5— 第二冷凝器， 6—蒸发器 /第一蒸发器， 7—溶液泵 /第一溶液泵， 8—冷剂液泵 /第一冷剂液泵， 9一节流阀 /第一节流阀， 10—第一溶液热交换器， 11一第二溶液热交换器， 12—第三发生器， 13—第二吸收器， 14一第二溶液泵， 15—第三溶液热交换器， 16—吸收-发生器， 17—分汽室， 18—第三冷凝器， 19一第二蒸发器， 20—第二冷剂液泵， 21—第三溶液泵， 22—第二节流阀， 23—第四发生器， 24—第四溶液热交换器， 25—第三节流阀； A—新增发生器 /新增第一发生 器， B—新增溶液热交换器 /新增第一溶液热交换器， C一新增节流阔 /新增第一节流阀， D—新 增溶液泵 /新增第一溶液泵， E—新增第二发生器， F—新增第二溶液热交换器， G—新增第二 节流阀， H—新增第二溶液泵， I一新增第三节流阀， J一新增溶液节流阀， K一新增吸收-蒸发 器， L一新增冷剂液泵。  Figure 44 is a first configuration and flow diagram of a single-effect-recovery type 1.5 third-class absorption heat pump according to the present invention. Figure 45 is a second construction and flow diagram of a single-effect-recovery type 1.5 third-class absorption heat pump provided in accordance with the present invention. Figure 46 is a third construction and flow diagram of a single-effect-recovery type 1.5 third-class absorption heat pump provided in accordance with the present invention. Figure 47 is a fourth construction and flow diagram of a single-effect-recovery type 1.5 third-class absorption heat pump according to the present invention. Figure 48 is a fifth configuration and flow diagram of a single-effect-recovery type 1.5 third-class absorption heat pump provided in accordance with the present invention. Figure 49 is a sixth configuration and flow diagram of a single-effect-recovery type 1.5 third-class absorption heat pump according to the present invention. Figure 50 is a seventh configuration and flow diagram of a single-effect-recovery type 1.5 third-class absorption heat pump according to the present invention. Figure 51 is a diagram showing the eighth construction and flow chart of a single-effect-recovery type 1.5 third-class absorption heat pump according to the present invention. Figure 52 is a diagram showing the ninth structure and flow chart of a single-effect-recovery type 1.5 third-class absorption heat pump according to the present invention. Figure 53 is a diagram showing the tenth structure and flow chart of a single-effect-recovery type 1.5 third-class absorption heat pump according to the present invention. Figure 54 is a diagram showing the eleventh structure and flow chart of a single-effect-recovery type 1.5 third-class absorption heat pump according to the present invention. Figure 55 is a diagram showing the structure and flow chart of a single-effect-recovery type 1.5 third-class absorption heat pump according to the present invention. In the figure, 1 - first generator, 2 - second generator, 3 - absorber / first absorber, 4 - first condenser, 5 - second condenser, 6 - evaporator / first evaporator , 7—solution pump/first solution pump, 8—coolant pump/first coolant pump, 9 throttle valve/first throttle valve, 10—first solution heat exchanger, 11 first Solution heat exchanger, 12 - third generator, 13 - second absorber, 14 - second solution pump, 15 - third solution heat exchanger, 16 - absorption - generator, 17 - steam compartment, 18 - Third condenser, 19 - second evaporator, 20 - second refrigerant liquid pump, 21 - third solution pump, 22 - second throttle valve, 23 - fourth generator, 24 - fourth solution heat exchange , 25—third throttle valve; A—new generator/new first generator, B—new solution heat exchanger/new first solution heat exchanger, C added new throttle/ New first throttle valve, D - new solution pump / new first solution pump, E - new second generator, F - new second solution heat exchanger, G - new second throttle Valve, H Add a second solution pump, I add a third throttle, J throttle a new solution, K a new absorber - evaporator, L a new refrigerant pump.
需要定义和说明的是：  What needs to be defined and explained is:
(1)浓溶液提供器——是指经第二溶液热交换器 11、 或分别经第二溶液热交换器 11和第 三溶液热交换器 15以及分别经第二溶液热交换器 11、 第三溶液热交换器 15和第四溶液热交 换器 24向吸收器 3提供浓溶液的部件； 其中， 浓溶液为并列两路或三路时， 可视为分路进入 或汇合成一路进入吸收器 3。  (1) a concentrated solution provider - means passing through the second solution heat exchanger 11, or passing through the second solution heat exchanger 11 and the third solution heat exchanger 15, respectively, and respectively passing through the second solution heat exchanger 11, The three-solution heat exchanger 15 and the fourth solution heat exchanger 24 provide a component of the concentrated solution to the absorber 3; wherein, when the concentrated solution is two or three in parallel, it can be regarded as a branching into or into a single absorber into the absorber. 3.
(2)以图 3所示为例， 图 3中第一溶液泵 7用于调节溶液流经吸收-发生器 16吸热汽化时 的压力， 此时分汽室 17的冷剂蒸汽压力 （即第三冷凝器 18内的冷剂蒸汽压力） 高于第一冷 凝器 4的冷剂蒸汽压力；选择第三冷凝器 18的冷剂蒸汽压力低于第一冷凝器 4的冷剂蒸汽压 力时， 则不设置第一冷剂液泵 7。 (3)以图 4所示为例，图 4中第三溶液泵 21的主要作用在于克服溶液流经第三溶液热交换 器 15的阻力以及管路阻力。 (2) Taking the example shown in FIG. 3, the first solution pump 7 in FIG. 3 is used to adjust the pressure at which the solution flows through the absorption-generator 16 during the endothermic vaporization, and at this time, the refrigerant vapor pressure of the steam separation chamber 17 (ie, The refrigerant vapor pressure in the triple condenser 18 is higher than the refrigerant vapor pressure of the first condenser 4; when the refrigerant vapor pressure of the third condenser 18 is selected to be lower than the refrigerant vapor pressure of the first condenser 4, The first refrigerant liquid pump 7 is not provided. (3) Taking the example shown in Fig. 4, the main function of the third solution pump 21 in Fig. 4 is to overcome the resistance of the solution flowing through the third solution heat exchanger 15 and the resistance of the line.
(4)以图 1所示为例， 在采用诸如氨水溶液为工作介质时， 发生器为精馏塔， 第一精熘塔 1还有冷却介质管路与外部连通， 第二精镏塔 2还有被加热介质管路与外部连通。  (4) Taking the example shown in Fig. 1 as an example, when a working medium such as an aqueous ammonia solution is used, the generator is a rectification tower, and the first refinery tower 1 and the cooling medium pipeline are connected to the outside, and the second refinery tower 2 There is also a heated medium line that communicates with the outside.
(5)以图 3所示为例， 在采用诸如氨水溶液为工作介质时， 分汽室的分汽需要精馏过程， 此时分汽室增加冷却介质管路与外部连通。  (5) Taking the example shown in Fig. 3, when a working medium such as an aqueous ammonia solution is used, the steam separation of the steam separation chamber requires a rectification process, and at this time, the steam distribution chamber increases the communication medium line to communicate with the outside.
具体实施方式： detailed description:
首先要说明的是， 在结构和流程的表述上， 非必要情况下不进行重复表述。 下面结合附 图和实例来详细描述本发明。  The first thing to note is that in the description of the structure and process, repeated representations are not required if not necessary. The invention will be described in detail below with reference to the drawings and examples.
图 1所示的单效 -单效第三类吸收式热泵是这样实现的：  The single-effect, single-effect, third-class absorption heat pump shown in Figure 1 is implemented as follows:
①结构上， 它主要由第一发生器、 第二发生器、 吸收器、 第一冷凝器、 第二冷凝器、 蒸 发器、 溶液泵、 冷剂液泵、 节流阀、 第一溶液热交换器和第二溶液热交换器所组成； 第一发 生器 1有浓溶液管路经溶液泵 7、 第一溶液热交换器 10和第二溶液热交换器 11与第二发生 器 2连通， 第二发生器 2还有浓溶液管路经第二溶液热交换器 11与吸收器 3连通， 吸收器 3 还有稀溶液管路经第一溶液热交换器 10与第一发生器 1连通，第一发生器 1还有冷剂蒸汽通 道与第一冷凝器 4连通， 第一冷凝器 4还有冷剂液管路经冷剂液泵 8与蒸发器 6连通， 第二 发生器 2还有冷剂蒸汽通道与第二冷凝器 5连通， 第二冷凝器 5还有冷剂液管路经节流阀 9 与蒸发器 6连通， 蒸发器 6还有冷剂蒸汽通道与吸收器 3连通， 第一发生器 1和蒸发器 6还 分别有余热介质管路与外部连通， 第二发生器 2还有驱动热介质管路与外部连通， 吸收器 3 和第二冷凝器 5还分别有被加热介质管路与外部连通， 第一冷凝器 4还有冷却介质管路与外 部连通。  1 structurally, it mainly consists of a first generator, a second generator, an absorber, a first condenser, a second condenser, an evaporator, a solution pump, a refrigerant liquid pump, a throttle valve, a first solution heat exchange And the second solution heat exchanger; the first generator 1 has a concentrated solution line connected to the second generator 2 via the solution pump 7, the first solution heat exchanger 10 and the second solution heat exchanger 11 The second generator 2 and the concentrated solution line are connected to the absorber 3 via the second solution heat exchanger 11, and the absorber 3 and the dilute solution line are connected to the first generator 1 via the first solution heat exchanger 10, A generator 1 and a refrigerant vapor passage are in communication with the first condenser 4, and the first condenser 4 and the refrigerant liquid line are connected to the evaporator 6 via the refrigerant liquid pump 8, and the second generator 2 is also cooled. The refrigerant vapor passage is in communication with the second condenser 5, and the second condenser 5 and the refrigerant liquid pipeline are connected to the evaporator 6 via the throttle valve 9, and the evaporator 6 and the refrigerant vapor passage are connected to the absorber 3, A generator 1 and an evaporator 6 respectively have a residual heat medium pipe connected to the outside The second generator 2 also has a driving heat medium pipe connected to the outside, and the absorber 3 and the second condenser 5 are respectively connected to the outside by the heated medium pipe, and the first condenser 4 has a cooling medium pipe and the outside. Connected.
②流程上， 吸收器 3的稀溶液经第一溶液热交换器 10进入第一发生器 1， 余热介质流经 第一发生器 1、 加热进入其内的溶液释放并向第一冷凝器 4提供冷剂蒸汽， 第一冷凝器 4的 冷剂蒸汽放热于冷却介质成冷剂液， 第一冷凝器 4的冷剂液经冷剂液泵 8加压进入蒸发器 6; 第一发生器 1的浓溶液经溶液泵 7、 第一溶液热交换器 10和第二溶液热交换器 11进入第二 发生器 2， 驱动热介质流经第二发生器 2、加热进入其内的溶液释放并向第二冷凝器 5提供冷 剂蒸汽，第二冷凝器 5的冷剂液经节流阀 9节流降压后进入蒸发器 6;余热介质流经蒸发器 6、 加热进入其内的冷剂液成冷剂蒸汽并向吸收器 3提供， 第二发生器 2的浓溶液经第二溶液热 交换器 11进入吸收器 3、 吸收来自蒸发器 6的冷剂蒸汽并放热于被加热介质， 吸收器 3的稀 溶液经第一溶液热交换器 10进入第一发生器 1 ; 第二冷凝器 5的冷剂蒸汽放热于被加热介质 成冷剂液，； 形成单效 -单效第三类吸收式热泵。  2 In the process, the dilute solution of the absorber 3 enters the first generator 1 through the first solution heat exchanger 10, and the residual heat medium flows through the first generator 1, and the solution heated therein is released and supplied to the first condenser 4. The refrigerant vapor, the refrigerant vapor of the first condenser 4 is radiated to the cooling medium to form a refrigerant liquid, and the refrigerant liquid of the first condenser 4 is pressurized by the refrigerant liquid pump 8 into the evaporator 6; the first generator 1 The concentrated solution enters the second generator 2 via the solution pump 7, the first solution heat exchanger 10 and the second solution heat exchanger 11, drives the heat medium to flow through the second generator 2, and the solution heated into the solution is released and directed The second condenser 5 supplies refrigerant vapor, and the refrigerant liquid of the second condenser 5 is throttled and depressurized by the throttle valve 9 to enter the evaporator 6; the waste heat medium flows through the evaporator 6, and the refrigerant liquid which is heated therein is heated. The refrigerant vapor is supplied to the absorber 3, and the concentrated solution of the second generator 2 enters the absorber 3 through the second solution heat exchanger 11, absorbs the refrigerant vapor from the evaporator 6, and radiates heat to the heated medium, absorbing The dilute solution of the device 3 enters the first solution through the first solution heat exchanger 10 a generator 1; the refrigerant vapor of the second condenser 5 is exothermic to the heated medium to form a refrigerant liquid; and a single-effect single-effect third type absorption heat pump is formed.
图 2所示的回热式第三类吸收式热泵是这样实现的：  The regenerative third type absorption heat pump shown in Figure 2 is implemented as follows:
①结构上， 在图 1所示的第三类吸收式热泵中， 增加第三发生器、 第二吸收器、 第二溶 液泵和第三溶液热交换器， 将吸收器 3有稀溶液管路经第一溶液热交换器 10与第一发生器 1 连通调整为吸收器 3有稀溶液管路经第一溶液热交换器 10与第二吸收器 13连通， 第二吸收 器 13还有稀溶液管路经第二溶液泵 14和第三溶液热交换器 15与第一发生器 1连通，将第一 发生器 1有浓溶液管路经第一溶液泵 7、 第一溶液热交换器 10和第二溶液热交换器 11与第 二发生器 2连通调整为第一发生器 1有浓溶液管路经第三溶液热交换器 15与第三发生器 12 连通， 第三发生器 12还有浓溶液管路经第一溶液泵 7、 第一溶液热交换器 10和第二溶液热 交换器 11与第二发生器 2连通，第三发生器 12还分别有冷剂蒸汽通道与第二吸收器 13连通 和有余热介质管路与外部连通， 第二吸收器 13还有冷却介质管路与外部连通。 1 structurally, in the third type of absorption heat pump shown in FIG. 1, the third generator, the second absorber, the second solution pump and the third solution heat exchanger are added, and the absorber 3 has a dilute solution line. The first solution heat exchanger 10 is connected to the first generator 1 to be adjusted so that the absorber 3 has a dilute solution line communicating with the second absorber 13 via the first solution heat exchanger 10, and the second absorber 13 has a dilute solution. The pipeline is connected to the first generator 1 via the second solution pump 14 and the third solution heat exchanger 15, and the first generator 1 has a concentrated solution pipeline through the first solution pump 7, the first solution heat exchanger 10, and The second solution heat exchanger 11 is connected to the second generator 2 to be adjusted so that the first generator 1 has a concentrated solution line connected to the third generator 12 via the third solution heat exchanger 15, and the third generator 12 is further rich. The solution line is in communication with the second generator 2 via the first solution pump 7, the first solution heat exchanger 10 and the second solution heat exchanger 11, the third generator 12 further having a refrigerant vapor channel and a second absorber, respectively 13 connectivity And the residual heat medium pipeline communicates with the outside, and the second absorber 13 and the cooling medium pipeline communicate with the outside.
②流程上， 吸收器 3的稀溶液经第一溶液热交换器 10进入第二吸收器 13、 吸收来自第 三发生器 12的冷剂蒸汽并放热于冷却介质，第二吸收器 13的稀溶液经第二溶液泵 14和第三 溶液热交换器 15进入第一发生器 1 ; 第一发生器 1的浓溶液经第三溶液热交换器 15进入第 三发生器 12， 余热介质流经第三发生器 12、 加热进入其内的溶液释放并向第二吸收器 13提 供冷剂蒸汽； 第三发生器 12的浓溶液经第一溶液泵 7、 第一溶液热交换器 10和第二溶液热 交换器 11进入第二发生器 2， 形成回热式第三类吸收式热泵。  2 In the process, the dilute solution of the absorber 3 enters the second absorber 13 through the first solution heat exchanger 10, absorbs the refrigerant vapor from the third generator 12, and radiates heat to the cooling medium, and the second absorber 13 is diluted. The solution enters the first generator 1 via the second solution pump 14 and the third solution heat exchanger 15; the concentrated solution of the first generator 1 enters the third generator 12 via the third solution heat exchanger 15, and the residual heat medium flows through the first a three generator 12, a solution heated therein to release and supply refrigerant vapor to the second absorber 13; a concentrated solution of the third generator 12 passes through the first solution pump 7, the first solution heat exchanger 10, and the second solution The heat exchanger 11 enters the second generator 2 to form a recuperative third type absorption heat pump.
图 3所示的回热式第三类吸收式热泵是这样实现的：  The regenerative third type absorption heat pump shown in Figure 3 is implemented as follows:
①结构上， 在图 1所示的第三类吸收式热泵中， 增加第二溶液泵、 第三溶液热交换器、 吸收-发生器、 分汽室、 第三冷凝器、 第二蒸发器和第二冷剂液泵， 将吸收器 3有稀溶液管路 经第一溶液热交换器 10与第一发生器 1连通调整为吸收器 3有稀溶液管路经第三溶液热交换 器 15与吸收-发生器 16连通， 吸收-发生器 16还有稀溶液管路经第一溶液热交换器 10与第 一发生器 1连通， 将第一发生器 1有浓溶液管路经第一溶液泵 7、 第一溶液热交换器 10和第 二溶液热交换器 11与第二发生器 2连通调整为第一发生器 1有浓溶液管路经第一溶液泵 7、 第一溶液热交换器 10和吸收-发生器 16与分汽室 17连通，分汽室 17还有浓溶液管路经第二 溶液泵 14、 第三溶液热交换器 15和第二溶液热交换器 11与第二发生器 2连通， 分汽室 17 还有冷剂蒸汽通道与第三冷凝器 18连通， 第三冷凝器 18还有冷剂液管路经第二冷剂液泵 20 与第二蒸发器 19连通， 第二蒸发器 19还有冷剂蒸汽通道与吸收-发生器 16连通， 第三冷凝 器 18还有冷却介质管路与外部连通， 第二蒸发器 19还有余热介质管路与外部连通。  1 structurally, in the third type of absorption heat pump shown in FIG. 1, adding a second solution pump, a third solution heat exchanger, an absorption-generator, a steam separation chamber, a third condenser, a second evaporator, and a second refrigerant liquid pump, the absorber 3 has a dilute solution line connected to the first generator 1 through the first solution heat exchanger 10 to adjust the absorber 3 has a dilute solution line through the third solution heat exchanger 15 and The absorption-generator 16 is connected, the absorption-generator 16 and the dilute solution line are connected to the first generator 1 via the first solution heat exchanger 10, and the first generator 1 has a concentrated solution line through the first solution pump. 7. The first solution heat exchanger 10 and the second solution heat exchanger 11 are connected to the second generator 2 to be adjusted so that the first generator 1 has a concentrated solution line through the first solution pump 7 and the first solution heat exchanger 10. And the absorption-generator 16 is in communication with the steam dividing chamber 17, and the steam dividing chamber 17 has a concentrated solution line passing through the second solution pump 14, the third solution heat exchanger 15 and the second solution heat exchanger 11 and the second generator 2 connected, the steam dividing chamber 17 and the refrigerant vapor passage are connected to the third condenser 18, The third condenser 18 also has a refrigerant liquid line connected to the second evaporator 19 via the second refrigerant liquid pump 20, and the second evaporator 19 also has a refrigerant vapor passage communicating with the absorption-generator 16 for the third condensation. The device 18 also has a cooling medium line communicating with the outside, and the second evaporator 19 and the residual heat medium line are in communication with the outside.
②流程上， 吸收器 3的稀溶液经第三溶液热交换器 15进入吸收-发生器 16、 吸收来自第 二蒸发器 19的冷剂蒸汽并放热于流经吸收-发生器 16的溶液， 吸收-发生器 16的稀溶液经第 第一溶液热交换器 10进入第一发生器 1； 第一发生器 1的浓溶液经第一溶液泵 7和第一溶液 热交换器 10之后再流经吸收-发生器 16、 吸热部分汽化进入分汽室 17， 分汽室 17释放的冷 剂蒸汽进入第三冷凝器 18、 放热于冷却介质成冷剂液， 第三冷凝器 18的冷剂液经第二冷剂 液泵 20加压进入第二蒸发器 19、 吸收余热成冷剂蒸汽并向吸收-发生器 16提供， 分汽室 17 的浓溶液经第二溶液泵 14、第三溶液热交换器 15和第二溶液热交换器 11进入第二发生器 2， 形成单效-回热式单效第三类吸收式热泵。  2 In the scheme, the dilute solution of the absorber 3 enters the absorption-generator 16 via the third solution heat exchanger 15, absorbs the refrigerant vapor from the second evaporator 19, and releases the solution flowing through the absorption-generator 16 The dilute solution of the absorption-generator 16 enters the first generator 1 via the first solution heat exchanger 10; the concentrated solution of the first generator 1 passes through the first solution pump 7 and the first solution heat exchanger 10 and then flows through The absorption-generator 16 and the endothermic portion are vaporized into the steam dividing chamber 17, and the refrigerant vapor released from the steam dividing chamber 17 enters the third condenser 18, radiates heat to the cooling medium to form a refrigerant liquid, and the refrigerant of the third condenser 18 The liquid is pressurized into the second evaporator 19 via the second refrigerant liquid pump 20, absorbs the residual heat into the refrigerant vapor and is supplied to the absorption generator 16, and the concentrated solution of the steam separation chamber 17 passes through the second solution pump 14, the third solution. The heat exchanger 15 and the second solution heat exchanger 11 enter the second generator 2 to form a single-effect regenerative single-effect third-class absorption heat pump.
图 4所示的回热式第三类吸收式热泵是这样实现的- The regenerative third type absorption heat pump shown in Figure 4 is realized in this way -
①结构上， 在图 1所示的第三类吸收式热泵中， 增加第二溶液泵、 第三溶液热交换器、 吸收-发生器、 分汽室、 第三冷凝器、 第二冷剂液泵和第三溶液泵， 将吸收器 3有稀溶液管路 经第一溶液热交换器 10与第一发生器 1连通调整为吸收器 3有稀溶液管路经第三溶液泵 21 和第三溶液热交换器 15与吸收-发生器 16连通，吸收-发生器 16还有稀溶液管路经第一溶液 热交换器 10与第一发生器 1连通， 将第一发生器 1有浓溶液管路经第一溶液泵 7、 第一溶液 热交换器 10和第二溶液热交换器 11与第二发生器 2连通调整为第一发生器 1有浓溶液管路 经第一溶液泵 7、 第一溶液热交换器 10和吸收-发生器 16与分汽室 17连通， 分汽室 17还有 浓溶液管路经第二溶液泵 14、 第三溶液热交换器 15和第二溶液热交换器 11与第二发生器 2 连通， 吸收-发生器 16还有被加热介质管路与外部连通， 分汽室 17还有冷剂蒸汽通道与第三 冷凝器 18连通， 第三冷凝器 18还有冷剂液管路经第二冷剂液泵 20与蒸发器 6连通， 蒸发器 6增设冷剂蒸汽通道与吸收-发生器 16连通， 第三冷凝器 18还有冷却介质管路与外部连通。 1 structurally, in the third type of absorption heat pump shown in FIG. 1, adding a second solution pump, a third solution heat exchanger, an absorption-generator, a steam separation chamber, a third condenser, and a second coolant liquid The pump and the third solution pump adjust the absorber 3 having a dilute solution line through the first solution heat exchanger 10 to the first generator 1 to adjust the absorber 3 to have a dilute solution line through the third solution pump 21 and the third The solution heat exchanger 15 is in communication with the absorption-generator 16 and the absorption-generator 16 and the dilute solution line are in communication with the first generator 1 via the first solution heat exchanger 10, and the first generator 1 has a concentrated solution tube. Passing through the first solution pump 7, the first solution heat exchanger 10 and the second solution heat exchanger 11 and the second generator 2 to adjust to the first generator 1 having a concentrated solution line through the first solution pump 7, A solution heat exchanger 10 and an absorption-generator 16 are in communication with the steam dividing chamber 17, and the steam dividing chamber 17 has a concentrated solution line passing through the second solution pump 14, the third solution heat exchanger 15, and the second solution heat exchanger. 11 is connected to the second generator 2, and the absorption-generator 16 has a heated medium tube Communicating with the outside, the steam dividing chamber 17 also has a refrigerant vapor passage communicating with the third condenser 18, and the third condenser 18 and the refrigerant liquid pipeline are connected to the evaporator 6 via the second refrigerant liquid pump 20, the evaporator 6 The refrigerant vapor passage is connected to the absorption-generator 16 , and the third condenser 18 and the cooling medium conduit are in communication with the outside.
②流程上， 吸收器 3的稀溶液经第三溶液泵 21和第三溶液热交换器 15进入吸收-发生器 16、 吸收来自蒸发器 6的冷剂蒸汽并分别放热于被加热介质和流经吸收-发生器 16的溶液， 吸收-发生器 16的稀溶液经第第一溶液热交换器 10进入第一发生器 1 ; 第一发生器 1的浓溶 液经第一溶液泵 7和第一溶液热交换器 10之后再流经吸收-发生器 16、 吸热部分汽化进入分 汽室 17， 分汽室 17释放的冷剂蒸汽进入第三冷凝器 18、 放热于冷却介质成冷剂液， 第三冷 凝器 18的冷剂液经第二冷剂液泵 20加压进入蒸发器 6， 蒸发器 6产生的冷剂蒸汽分别向吸 收器 3和吸收-发生器 16提供； 分汽室 17的浓溶液经第二溶液泵 14、 第三溶液热交换器 15 和第二溶液热交换器 11进入第二发生器 2， 形成单效-回热式单效第三类吸收式热泵。 2 In the process, the dilute solution of the absorber 3 enters the absorption-generator via the third solution pump 21 and the third solution heat exchanger 15. 16. Absorbing refrigerant vapor from the evaporator 6 and respectively radiating heat to the heated medium and the solution flowing through the absorption-generator 16, the dilute solution of the absorption-generator 16 entering the first through the first solution heat exchanger 10 The generator 1 ; the concentrated solution of the first generator 1 passes through the first solution pump 7 and the first solution heat exchanger 10 and then flows through the absorption-generator 16 , and the heat absorption portion is vaporized into the steam separation chamber 17 , and the steam separation chamber 17 The released refrigerant vapor enters the third condenser 18, radiates heat to the cooling medium to form a refrigerant liquid, and the refrigerant liquid of the third condenser 18 is pressurized into the evaporator 6 through the second refrigerant liquid pump 20, and the evaporator 6 generates The refrigerant vapor is supplied to the absorber 3 and the absorption-generator 16 respectively; the concentrated solution of the steam separation chamber 17 enters the second occurrence via the second solution pump 14, the third solution heat exchanger 15, and the second solution heat exchanger 11 2, forming a single-effect-recovery single-effect third-class absorption heat pump.
图 5所示的回热式第三类吸收式热泵是这样实现的：  The regenerative third type absorption heat pump shown in Figure 5 is implemented as follows:
在图 4所示的第三类吸收式热泵中， 取消吸收-发生器 16与外部连通的被加热介质管路， 取消第二冷剂液泵 20, 增加第二节流阀 22， 将第三冷凝器 18有冷剂液管路经第二冷剂液泵 20与蒸发器 6连通调整为第三冷凝器 18有冷剂液管路经第二节流阀 22与第一冷凝器 4连通。  In the third type of absorption heat pump shown in FIG. 4, the heated medium line in which the absorption-generator 16 communicates with the outside is canceled, the second refrigerant liquid pump 20 is cancelled, the second throttle valve 22 is added, and the third The condenser 18 has a refrigerant liquid line connected to the evaporator 6 via the second refrigerant liquid pump 20 to be adjusted to a third condenser 18, and a refrigerant liquid line is connected to the first condenser 4 via the second throttle valve 22.
这里要说明的是， 采用第二节流阀 22取代第二冷剂液泵 20, 是为了减少冷剂液泵的数 量； 付出的代价是冷剂液泵 8耗能的少量增加。  It is to be noted that the second throttle pump 22 is replaced by the second throttle valve 22 in order to reduce the amount of the refrigerant liquid pump; the price paid is a small increase in the energy consumption of the refrigerant liquid pump 8.
图 6所示的回热式第三类吸收式热泵是这样实现的：  The regenerative third type absorption heat pump shown in Figure 6 is realized in this way:
①结构上， 在图 1所示的第三类吸收式热泵中， 增加第二溶液泵、 第三溶液热交换器、 吸收-发生器、 分汽室、 第三冷凝器、 第二蒸发器和第二冷剂液泵， 将第一发生器 1有浓溶液 管路经第一溶液泵 7、 第一溶液热交换器 10和第二溶液热交换器 11与第二发生器 2连通调 整为第一发生器 1有浓溶液管路经第一溶液泵 7和第一溶液热交换器 10与吸收-发生器 16连 通， 吸收-发生器 16还有稀溶液管路经第一溶液热交换器 10与第一发生器 1连通， 将吸收器 3有稀溶液管路经第一溶液热交换器 10与第一发生器 1连通调整为吸收器 3有稀溶液管路经 第三溶液热交换器 15和吸收-发生器 16与分汽室 17连通，分汽室 17还有浓溶液管路经第二 溶液泵 14、 第三溶液热交换器 15和第二溶液热交换器 11与第二发生器 2连通， 将第一冷凝 器 4有冷剂液管路经第一冷剂液泵 8与第一蒸发器 6连通调整为第一冷凝器 4有冷剂液管路 经第一冷剂液泵 8与第二蒸发器 19连通， 第二蒸发器 19还有冷剂蒸汽通道与吸收-发生器 16连通， 分汽室 17还有冷剂蒸汽通道与第三冷凝器 18连通， 第三冷凝器 18还有冷剂液管 路经第二冷剂液泵 20与第一蒸发器 6连通， 第三冷凝器 18还有冷却介质管路与外部连通， 第二蒸发器 19还有余热介质管路与外部连通。  1 structurally, in the third type of absorption heat pump shown in FIG. 1, adding a second solution pump, a third solution heat exchanger, an absorption-generator, a steam separation chamber, a third condenser, a second evaporator, and The second refrigerant liquid pump adjusts the first generator 1 concentrated solution line to the first solution pump 7, the first solution heat exchanger 10, and the second solution heat exchanger 11 and the second generator 2 A generator 1 has a concentrated solution line connected to the absorption-generator 16 via the first solution pump 7 and the first solution heat exchanger 10, and the absorption-generator 16 and the dilute solution line are passed through the first solution heat exchanger 10. In communication with the first generator 1, the dilute solution line of the absorber 3 is communicated with the first generator 1 via the first solution heat exchanger 10 to adjust the absorber 3 to have a dilute solution line through the third solution heat exchanger 15 And the absorption-generator 16 is in communication with the steam dividing chamber 17, and the steam dividing chamber 17 has a concentrated solution line passing through the second solution pump 14, the third solution heat exchanger 15 and the second solution heat exchanger 11 and the second generator 2 connected, the first condenser 4 has a refrigerant liquid pipeline through the first refrigerant liquid pump 8 and An evaporator 6 is connected to adjust the first condenser 4 to have a refrigerant liquid pipeline connected to the second evaporator 19 via the first refrigerant liquid pump 8, and the second evaporator 19 has a refrigerant vapor passage and an absorption-generator 16 communicating, the steam dividing chamber 17 and the refrigerant vapor passage are in communication with the third condenser 18, and the third condenser 18 and the refrigerant liquid pipeline are connected to the first evaporator 6 via the second refrigerant liquid pump 20, The triple condenser 18 also has a cooling medium line communicating with the outside, and the second evaporator 19 and the residual heat medium line are in communication with the outside.
②流程上，吸收器 3的稀溶液经第三溶液热交换器 15降温降压后再流经吸收-发生器 16、 吸热部分汽化后进入分汽室 17， 分汽室 17释放的冷剂蒸汽进入第三冷凝器 18、 放热于冷却 介质成冷剂液， 第三冷凝器 18的冷剂液经第二冷剂液泵 20加压进入蒸发器 6， 分汽室 17的 浓溶液经第二溶液泵 14、 第三溶液热交换器 15和第二溶液热交换器 11进入第二发生器 2; 第一发生器 1产生的冷剂蒸汽进入第一冷凝器 4， 第一冷凝器 4的冷剂液经第一冷剂液泵 8 进入第二蒸发器 19、 吸收余热成冷剂蒸汽并向吸收-发生器 16提供， 第一发生器 1的浓溶液 经第一溶液泵 7和第一溶液热交换器 10进入吸收-发生器 16，吸收来自第二蒸发器 19的冷剂 蒸汽并放热于流经吸收-发生器 16的溶液， 吸收-发生器 16的稀溶液经第一溶液热交换器 10 进入第一发生器 1， 形成单效 -回热式单效第三类吸收式热泵。  2 In the process, the diluted solution of the absorber 3 is cooled and depressurized by the third solution heat exchanger 15, and then flows through the absorption-generator 16, and the endothermic portion is vaporized and then enters the steam dividing chamber 17, and the refrigerant released from the steam dividing chamber 17 The steam enters the third condenser 18, exotherms in the cooling medium to form a refrigerant liquid, and the refrigerant liquid of the third condenser 18 is pressurized into the evaporator 6 through the second refrigerant liquid pump 20, and the concentrated solution of the steam separation chamber 17 passes through The second solution pump 14, the third solution heat exchanger 15 and the second solution heat exchanger 11 enter the second generator 2; the refrigerant vapor generated by the first generator 1 enters the first condenser 4, the first condenser 4 The refrigerant liquid enters the second evaporator 19 via the first refrigerant liquid pump 8, absorbs the residual heat into the refrigerant vapor and supplies it to the absorption generator 16, and the concentrated solution of the first generator 1 passes through the first solution pump 7 and A solution heat exchanger 10 enters the absorption-generator 16, absorbs the refrigerant vapor from the second evaporator 19 and exotherms the solution flowing through the absorption-generator 16, and the dilute solution of the absorption-generator 16 passes through the first solution. The heat exchanger 10 enters the first generator 1 to form a single-effect-recovery single effect The third type of absorption heat pump.
图 7所示的双效 -单效第三类吸收式热泵是这样实现的：  The double-effect-single-effect third-type absorption heat pump shown in Figure 7 is implemented as follows:
①结构上， 在图 1所示的第三类吸收式热泵中， 增加第三发生器、 第三溶液热交换器和 第二节流阀，第一发生器 1经第一溶液泵 7和第一溶液热交换器 10之后增设浓溶液管路并再 经第三溶液热交换器 15与第三发生器 12连通，第三发生器 12还有浓溶液管路经第三溶液热 交换器 15与吸收器 3连通，将第二发生器 2有冷剂蒸汽通道与第二冷凝器 5连通调整为第二 发生器 2有冷剂蒸汽通道与第三发生器 12连通后第三发生器 12再有冷剂液管路经第二节流 m 22与第二冷凝器 5连通， 第三发生器 12还有冷剂蒸汽通道与第二冷凝器 5连通。 1 structurally, in the third type of absorption heat pump shown in FIG. 1, the third generator, the third solution heat exchanger and the second throttle valve are added, and the first generator 1 passes through the first solution pump 7 and the first After the solution heat exchanger 10 is added with a concentrated solution line and then communicated with the third generator 12 via the third solution heat exchanger 15, the third generator 12 also has a concentrated solution line through the third solution heat The exchanger 15 is in communication with the absorber 3, and the second generator 2 has a refrigerant vapor passage communicating with the second condenser 5 to be adjusted to a second generator 2 having a refrigerant vapor passage communicating with the third generator 12 to occur third. The refrigerant 12 is further connected to the second condenser 5 via the second throttle m 22, and the third generator 12 and the refrigerant vapor passage are in communication with the second condenser 5.
②流程上， 第二发生器 2产生的冷剂蒸汽提供给第三发生器 12作驱动热介质，第一发生 器 1的浓溶液经溶液泵 7和第一溶液热交换器 10之后分别再经第二溶液热交换器 11进入第 二发生器 2和再经第三溶液热交换器 15进入第三发生器 12; 冷剂蒸汽流经第三发生器 12、 加热进入其内的溶液释放并向第二冷凝器 5提供冷剂蒸汽，第三发生器 12的浓溶液经第三溶 液热交换器 15进入吸收器 3 , 流经第三发生器 12的冷剂蒸汽放热成冷剂液、 再经第二节流 阀 22节流进入第二冷凝器 5， 形成双效 -单效第三类吸收式热泵。  2 In the process, the refrigerant vapor generated by the second generator 2 is supplied to the third generator 12 to drive the heat medium, and the concentrated solution of the first generator 1 passes through the solution pump 7 and the first solution heat exchanger 10, respectively. The second solution heat exchanger 11 enters the second generator 2 and then enters the third generator 12 via the third solution heat exchanger 15; the refrigerant vapor flows through the third generator 12, and the solution heated therein is released and directed The second condenser 5 supplies refrigerant vapor, and the concentrated solution of the third generator 12 enters the absorber 3 through the third solution heat exchanger 15, and the refrigerant vapor flowing through the third generator 12 is released into a refrigerant liquid, and then The second throttle valve 22 is throttled into the second condenser 5 to form a double-effect-single-effect third-type absorption heat pump.
图 8所示的双效 -单效第三类吸收式热泵是这样实现的：  The double-effect-single-effect third-type absorption heat pump shown in Figure 8 is implemented as follows:
①结构上， 在图 1所示的第三类吸收式热泵中， 增加第三发生器、 第三溶液热交换器和 第二节流阀， 将第一发生器 1有浓溶液管路经第一溶液泵 7、 第一溶液热交换器 10和第二溶 液热交换器 11与第二发生器 2连通调整为第一发生器 1有浓溶液管路经第一溶液泵 7、 第一 溶液热交换器 10、 第二溶液热交换器 11和第三溶液热交换器 15与第二发生器 2连通， 将第 二发生器 2有浓溶液管路经第二溶液热交换器 11与吸收器 3连通调整为第二发生器 2有浓溶 液管路经第三溶液热交换器 15与第三发生器 12连通，第三发生器 12还有浓溶液管路经第二 溶液热交换器 11与吸收器 3连通，将第二发生器 2有冷剂蒸汽通道与第二冷凝器 5连通调整 为第二发生器 2有冷剂蒸汽通道与第三发生器 12连通后第三发生器 12再有冷剂液管路经第 二节流阀 22与第二冷凝器 5连通， 第三发生器 12还有冷剂蒸汽通道与第二冷凝器 5连通。  1 structurally, in the third type of absorption heat pump shown in FIG. 1, the third generator, the third solution heat exchanger and the second throttle valve are added, and the first generator 1 has a concentrated solution pipeline. A solution pump 7, a first solution heat exchanger 10 and a second solution heat exchanger 11 are connected to the second generator 2 to be adjusted so that the first generator 1 has a concentrated solution line through the first solution pump 7, the first solution heat The exchanger 10, the second solution heat exchanger 11 and the third solution heat exchanger 15 are in communication with the second generator 2, and the second generator 2 has a concentrated solution line through the second solution heat exchanger 11 and the absorber 3. The communication is adjusted to be that the second generator 2 has a concentrated solution line that communicates with the third generator 12 via the third solution heat exchanger 15, and the third generator 12 also has a concentrated solution line that passes through the second solution heat exchanger 11 and absorbs The third generator 12 is connected to the second generator 2 and has a refrigerant vapor passage communicating with the second condenser 5 to adjust the second generator 2 to have a refrigerant vapor passage communicating with the third generator 12. The agent liquid pipeline communicates with the second condenser 5 via the second throttle valve 22, and the third There refrigerant vapor passage communicating with the second condenser 5 generator 12.
②流程上， 第一发生器 1的浓溶液经溶液泵 7、 第一溶液热交换器 10、 第二溶液热交换 器 11和第三溶液热交换器 15进入第二发生器 2， 第二发生器 2产生的冷剂蒸汽提供给第三 发生器 12作驱动热介质， 第二发生器 2的浓溶液经第三溶液热交换器 15进入吸收器 3 ; 冷 剂蒸汽流经第三发生器 12、 加热进入其内的溶液释放并向第二冷凝器 5提供冷剂蒸汽， 第三 发生器 12的浓溶液经第二溶液热交换器 11进入吸收器 3， 流经第三发生器 12的冷剂蒸汽放 热成冷剂液、 再经第二节流阀 22节流进入第二冷凝器 5， 形成双效 -单效第三类吸收式热泵。  2, the concentrated solution of the first generator 1 enters the second generator 2 via the solution pump 7, the first solution heat exchanger 10, the second solution heat exchanger 11 and the third solution heat exchanger 15, the second occurrence The refrigerant vapor generated by the device 2 is supplied to the third generator 12 to drive the heat medium, and the concentrated solution of the second generator 2 enters the absorber 3 through the third solution heat exchanger 15; the refrigerant vapor flows through the third generator 12 The solution heated into the solution is released and the refrigerant vapor is supplied to the second condenser 5, and the concentrated solution of the third generator 12 enters the absorber 3 through the second solution heat exchanger 11, and flows through the cold of the third generator 12. The agent vapor is exothermic into a refrigerant liquid, and then throttled into the second condenser 5 through the second throttle valve 22 to form a double-effect-single-effect third type absorption heat pump.
图 9所示的双效 -单效第三类吸收式热泵是这样实现的- The double-effect-single-effect third-class absorption heat pump shown in Figure 9 is implemented in this way -
①结构上， 在图 1所示的第三类吸收式热泵中， 增加第三发生器、 第三溶液热交换器、 第二溶液泵和第二节流阀， 将第一发生器 1有浓溶液管路经第一溶液泵 7、 第一溶液热交换 器 10和第二溶液热交换器 11与第二发生器 2连通调整为第一发生器 1有浓溶液管路经第一 溶液泵 7、 第一溶液热交换器 10和第二溶液热交换器 11与第三发生器 12连通， 第三发生器 12还有浓溶液管路经第二溶液泵 14和第三溶液热交换器 15与第二发生器 2连通， 将第二发 生器 2有浓溶液管路经第二溶液热交换器 11与吸收器 3连通调整为第二发生器 2有浓溶液管 路经第三溶液热交换器 15和第二溶液热交换器 11与吸收器 3连通， 将第二发生器 2有冷剂 蒸汽通道与第二冷凝器 5连通调整为第二发生器 2有冷剂蒸汽通道与第三发生器 12连通后第 三发生器 12再有冷剂液管路经第二节流阀 22与第二冷凝器 5连通，第三发生器 12还有冷剂 蒸汽通道与第二冷凝器 5连通。 1 structurally, in the third type of absorption heat pump shown in FIG. 1, the third generator, the third solution heat exchanger, the second solution pump and the second throttle valve are added, and the first generator 1 is thick The solution line is connected to the second generator 2 via the first solution pump 7, the first solution heat exchanger 10, and the second solution heat exchanger 11 to be adjusted to be the first generator 1 having the concentrated solution line passing through the first solution pump 7 The first solution heat exchanger 10 and the second solution heat exchanger 11 are in communication with the third generator 12, and the third generator 12 has a concentrated solution line through the second solution pump 14 and the third solution heat exchanger 15 and The second generator 2 is connected, and the second generator 2 has a concentrated solution pipeline connected to the absorber 3 via the second solution heat exchanger 11 to be adjusted to a second generator 2 having a concentrated solution pipeline through the third solution heat exchanger 15 and the second solution heat exchanger 11 is in communication with the absorber 3, and the second generator 2 has a refrigerant vapor passage communicating with the second condenser 5 to adjust the second generator 2 to have a refrigerant vapor passage and a third generator. After the 12 is connected, the third generator 12 has a refrigerant liquid line through the second throttle valve 2 2 is in communication with the second condenser 5, and the third generator 12 also has a refrigerant vapor passage communicating with the second condenser 5.
②流程上， 第一发生器 1的浓溶液经第一溶液泵 7、 第一溶液热交换器 10和第二溶液热 交换器 11进入第三发生器 12， 第二发生器 2产生的冷剂蒸汽提供给第三发生器 12作驱动热 介质， 冷剂蒸汽流经第三发生器 12、 加热进入其内的溶液释放并向第二冷凝器 5提供冷剂蒸 汽， 第三发生器 12的浓溶液经第二溶液泵 14和第三溶液热交换器 15进入第二发生器 2， 流 经第三发生器 12的冷剂蒸汽放热成冷剂液、 再经第二节流阀 22节流进入第二冷凝器 5， 第 二发生器 1的浓溶液经第三溶液热交换器 15和第二溶液热交换器 11进入吸收器 3， 形成双 效 -单效第三类吸收式热泵。 2 In the process, the concentrated solution of the first generator 1 enters the third generator 12 via the first solution pump 7, the first solution heat exchanger 10 and the second solution heat exchanger 11, and the refrigerant generated by the second generator 2 The steam is supplied to the third generator 12 as a driving heat medium, the refrigerant vapor flows through the third generator 12, the solution heated therein is released, and the refrigerant vapor is supplied to the second condenser 5, and the third generator 12 is concentrated. The solution enters the second generator 2 through the second solution pump 14 and the third solution heat exchanger 15 The refrigerant vapor passing through the third generator 12 is exothermic into a refrigerant liquid, and then throttled into the second condenser 5 via the second throttle valve 22, and the concentrated solution of the second generator 1 passes through the third solution heat exchanger 15 And the second solution heat exchanger 11 enters the absorber 3 to form a double-effect-single-effect third-type absorption heat pump.
图 10所示的三效 -单效第三类吸收式热泵是这样实现的：  The three-effect-single-effect third-class absorption heat pump shown in Figure 10 is implemented as follows:
①结构上， 在图 7所示的第三类吸收式热泵中， 增加第四发生器、 第四溶液热交换器和 第三节流阀， 第一溶液热交换器 10增设浓溶液管路经第四溶液热交换器 24与第四发生器 23 连通， 第四发生器 23还有浓溶液管路经第四溶液热交换器 24与吸收器 3连通， 将第三发生 器 12有冷剂蒸汽通道与第二冷凝器 5连通调整为第三发生器 12有冷剂蒸汽通道与第四发生 器 23连通后第四发生器 23再有冷剂液管路经第三节流阀 25与第二冷凝器 5连通，第四发生 器 23还有冷剂蒸汽通道与第二冷凝器 5连通。  1Structurally, in the third type absorption heat pump shown in FIG. 7, the fourth generator, the fourth solution heat exchanger and the third throttle valve are added, and the first solution heat exchanger 10 is provided with a concentrated solution pipeline. The fourth solution heat exchanger 24 is in communication with the fourth generator 23, and the fourth generator 23 and the concentrated solution line are in communication with the absorber 3 via the fourth solution heat exchanger 24, and the third generator 12 has refrigerant vapor. The passage is connected to the second condenser 5 to be adjusted so that the third generator 12 has a refrigerant vapor passage communicating with the fourth generator 23, and then the fourth generator 23 has a refrigerant liquid pipeline passing through the third throttle valve 25 and the second The condenser 5 is in communication, and the fourth generator 23 and the refrigerant vapor passage are in communication with the second condenser 5.
②流程上， 第三发生器 12产生的冷剂蒸汽提供给第四发生器 23作驱动热介质， 第一发 生器 1的部分浓溶液经溶液泵 7、 第一溶液热交换器 10和第四溶液热交换器 24进入第四发 生器 23， 冷剂蒸汽流经第四发生器 23、加热进入其内的溶液释放并向第二冷凝器 5提供冷剂 蒸汽， 第四发生器 23的浓溶液经第四溶液热交换器 24进入吸收器 3， 流经第四发生器 23的 冷剂蒸汽放热成冷剂液、 再经第三节流阀 25节流进入第二冷凝器 5， 形成三效 -单效第三类 吸收式热泵。  2 In the process, the refrigerant vapor generated by the third generator 12 is supplied to the fourth generator 23 as a driving heat medium, and a part of the concentrated solution of the first generator 1 passes through the solution pump 7, the first solution heat exchanger 10 and the fourth The solution heat exchanger 24 enters the fourth generator 23, the refrigerant vapor flows through the fourth generator 23, the solution heated therein is released, and the refrigerant vapor is supplied to the second condenser 5, and the concentrated solution of the fourth generator 23 After entering the absorber 3 through the fourth solution heat exchanger 24, the refrigerant vapor flowing through the fourth generator 23 is released into a refrigerant liquid, and then throttled through the third throttle valve 25 into the second condenser 5 to form three Effect - single effect third type absorption heat pump.
图 11所示的三效 -单效第三类吸收式热泵是这样实现的- The three-effect-single-effect third-class absorption heat pump shown in Figure 11 is realized in this way -
①结构上， 在图 8所示的第三类吸收式热泵中， 增加第四发生器、 第四溶液热交换器和 第三节流阀， 将第二溶液热交换器 11有浓溶液管路经第三溶液热交换器 15与第二发生器 2 连通调整为第二溶液热交换器 11有浓溶液管路经第四溶液热交换器 24和第三溶液热交换器 15与第二发生器 2连通， 将第三发生器 12有浓溶液管路经第二溶液热交换器 11与吸收器 3 连通调整为第三发生器 12有浓溶液管路经第第四溶液热交换器 24与第四发生器 23连通，第 四发生器 23还有浓溶液管路经第二溶液热交换器 11与吸收器 3连通，将第三发生器 12有冷 剂蒸汽通道与第二冷凝器 5连通调整为第三发生器 12有冷剂蒸汽通道与第四发生器 23连通 后第四发生器 23再有冷剂液管路经第三节流阀 25与第二冷凝器 5连通，第四发生器 23还有 冷剂蒸汽通道与第二冷凝器 5连通。 1Structurally, in the third type absorption heat pump shown in FIG. 8, the fourth generator, the fourth solution heat exchanger and the third throttle valve are added, and the second solution heat exchanger 11 has a concentrated solution pipeline. Through the third solution heat exchanger 15 and the second generator 2, the second solution heat exchanger 11 has a concentrated solution pipeline through the fourth solution heat exchanger 24 and the third solution heat exchanger 15 and the second generator. 2 communicating, the third generator 12 has a concentrated solution pipeline connected to the absorber 3 through the second solution heat exchanger 11 to be adjusted to a third generator 12 having a concentrated solution pipeline through the fourth solution heat exchanger 24 and The fourth generator 23 is connected, the fourth generator 23 and the concentrated solution pipeline are connected to the absorber 3 via the second solution heat exchanger 11, and the third generator 12 has a refrigerant vapor passage connected to the second condenser 5. After the third generator 12 has a refrigerant vapor passage communicating with the fourth generator 23, the fourth generator 23 is further connected to the second condenser 5 via the third throttle valve 25, and the fourth generator 23 also has a refrigerant vapor passage communicating with the second condenser 5.
②流程上， 第一发生器 1的浓溶液经溶液泵 7、 第一溶液热交换器 10、 第二溶液热交换 器 11、 第四溶液热交换器 24和第三溶液热交换器 15进入第二发生器 2， 第二发生器 2的浓 溶液经第三溶液热交换器 15进入第三发生器 12， 第三发生器 12的浓溶液经第四溶液热交换 器 24进入第四发生器 23 ; 第三发生器 12产生的冷剂蒸汽提供给第四发生器 23作驱动热介 质，冷剂蒸汽流经第四发生器 23、加热进入其内的溶液释放并向第二冷凝器 5提供冷剂蒸汽， 第四发生器 23的浓溶液经第二溶液热交换器 11进入吸收器 3， 流经第四发生器 23的冷剂蒸 汽放热成冷剂液、 再经第三节流阀 25进入第二冷凝器 5， 形成三效 -单效第三类吸收式热泵。  In the second scheme, the concentrated solution of the first generator 1 enters the first through the solution pump 7, the first solution heat exchanger 10, the second solution heat exchanger 11, the fourth solution heat exchanger 24, and the third solution heat exchanger 15. The second generator 2, the concentrated solution of the second generator 2 enters the third generator 12 via the third solution heat exchanger 15, and the concentrated solution of the third generator 12 enters the fourth generator 23 via the fourth solution heat exchanger 24. The refrigerant vapor generated by the third generator 12 is supplied to the fourth generator 23 for driving the heat medium, and the refrigerant vapor flows through the fourth generator 23, and the solution heated therein is released and provides cold to the second condenser 5. The vapor of the agent, the concentrated solution of the fourth generator 23 enters the absorber 3 via the second solution heat exchanger 11, and the refrigerant vapor flowing through the fourth generator 23 is released into a refrigerant liquid, and then passes through the third throttle valve 25 Entering the second condenser 5, a three-effect-single-effect third-type absorption heat pump is formed.
图 12所示的三效 -单效第三类吸收式热泵是这样实现的- The three-effect-single-effect third-class absorption heat pump shown in Figure 12 is realized in this way -
①结构上， 在图 9所示的第三类吸收式热泵中， 增加第四发生器、 第四溶液热交换器、 第三节流阀和第三溶液泵， 将第二溶液热交换器 11有浓溶液管路与第三发生器 12连通调整 为第二溶液热交换器 11有浓溶液管路与第四发生器 23连通，第四发生器 23还有浓溶液管路 经第三溶液泵 21和第四溶液热交换器 24与第三发生器 12连通，将第二发生器 2有浓溶液管 路经第三溶液热交换器 15和第二溶液热交换器 11与吸收器 3连通调整为第二发生器 2有浓 溶液管路经第三溶液热交换器 15、 第四溶液热交换器 24和第二溶液热交换器 11与吸收器 3 连通， 将第三发生器 12有冷剂蒸汽通道与第二冷凝器 5连通调整为第三发生器 12有冷剂蒸 汽通道与第四发生器 23连通后第四发生器 23再有冷剂液管路经第三节流阀 25与第二冷凝器 5连通， 第四发生器 23还有冷剂蒸汽通道与第二冷凝器 5连通。 1 Structurally, in the third type of absorption heat pump shown in FIG. 9, the fourth generator, the fourth solution heat exchanger, the third throttle valve, and the third solution pump are added, and the second solution heat exchanger 11 is added. The concentrated solution line is connected to the third generator 12 to be adjusted to be the second solution heat exchanger 11 has a concentrated solution line connected to the fourth generator 23, and the fourth generator 23 has a concentrated solution line through the third solution pump The 21 and fourth solution heat exchangers 24 are in communication with the third generator 12, and the second generator 2 has a concentrated solution line connected to the absorber 3 via the third solution heat exchanger 15 and the second solution heat exchanger 11 a second solution 2 having a concentrated solution line through the third solution heat exchanger 15, the fourth solution heat exchanger 24, and the second solution heat exchanger 11 and the absorber 3 Connected, the third generator 12 has a refrigerant vapor passage communicating with the second condenser 5 to be adjusted to a third generator 12 having a refrigerant vapor passage communicating with the fourth generator 23, and then the fourth generator 23 is further provided with a refrigerant liquid The pipeline communicates with the second condenser 5 via a third throttle valve 25, and the fourth generator 23 also has a refrigerant vapor passage communicating with the second condenser 5.
②流程上， 第一发生器 1的浓溶液经第一溶液泵 7、 第一溶液热交换器 10和第二溶液热 交换器 11进入第四发生器 23， 第三发生器 12产生的冷剂蒸汽提供给第四发生器 23作驱动 热介质， 冷剂蒸汽流经第四发生器 23、 加热进入其内的溶液释放并向第二冷凝器 5提供冷剂 蒸汽， 第四发生器 23的浓溶液经第三溶液泵 21和第四溶液热交换器 24进入第三发生器 12， 流经第四发生器 23的冷剂蒸汽放热成冷剂液、 再经第三节流阔 25进入第二冷凝器 5， 第二 发生器 2的浓溶液经第三溶液热交换器 15、 第四溶液热交换器 24和第二溶液热交换器 11进 入吸收器 3 , 形成三效-单效第三类吸收式热泵。  2 In the process, the concentrated solution of the first generator 1 enters the fourth generator 23 via the first solution pump 7, the first solution heat exchanger 10 and the second solution heat exchanger 11, and the refrigerant generated by the third generator 12 The steam is supplied to the fourth generator 23 for driving the heat medium, the refrigerant vapor flows through the fourth generator 23, the solution heated therein is released, and the refrigerant vapor is supplied to the second condenser 5, and the fourth generator 23 is concentrated. The solution enters the third generator 12 through the third solution pump 21 and the fourth solution heat exchanger 24, and the refrigerant vapor flowing through the fourth generator 23 is released into a refrigerant liquid, and then enters the third section through the third section. The second condenser 5, the concentrated solution of the second generator 2 enters the absorber 3 through the third solution heat exchanger 15, the fourth solution heat exchanger 24 and the second solution heat exchanger 11, forming a three-effect-single-effect third Absorption heat pump.
图 13所示的单效 -双效第三类吸收式热泵是这样实现的：  The single-effect, double-effect, third-class absorption heat pump shown in Figure 13 is implemented as follows:
①结构上， 在图 1所示的第三类吸收式热泵中， 增加新增发生器、 新增溶液热交换器、 新增节流阀和新增溶液泵， 吸收器 3增设稀溶液管路经新增溶液热交换器 B与新增发生器 A 连通， 新增发生器 A还有浓溶液管路经新增溶液泵 D和新增溶液热交换器 B之后与第一发生 器 1经溶液泵 7和第一溶液热交换器 10之后的浓溶液管路汇合，将第一发生器 1有冷剂蒸汽 通道与第一冷凝器 4连通调整为第一发生器 1有冷剂蒸汽通道与新增发生器 A连通后新增发 生器 A再有冷剂液管路经新增节流阀 C与第一冷凝器 4连通， 新增发生器 A还有冷剂蒸汽通 道与第一冷凝器 4连通。  1Structurally, in the third type of absorption heat pump shown in Fig. 1, a new generator, a new solution heat exchanger, a new throttle valve and a new solution pump are added, and the absorber 3 is provided with a dilute solution pipeline. The new solution heat exchanger B is connected to the newly added generator A, and the new generator A and the concentrated solution pipeline are added to the first generator 1 through the new solution pump D and the new solution heat exchanger B. The pump 7 and the concentrated solution pipeline after the first solution heat exchanger 10 meet, and the first generator 1 has a refrigerant vapor passage connected to the first condenser 4 to adjust the first generator 1 to have a refrigerant vapor passage and a new one. After the generator A is connected, the generator A is newly added, and then the refrigerant liquid pipeline is connected to the first condenser 4 via the newly added throttle valve C, and the new generator A is also provided with the refrigerant vapor passage and the first condenser 4 Connected.
②流程上， 吸收器 3的稀溶液经新增溶液热交换器 B进入新增发生器 A， 第一发生器 1 产生的冷剂蒸汽提供给新增发生器 A作驱动热介质， 冷剂蒸汽流经新增发生器 A、 加热进入 其内的溶液释放并向第一冷凝器 4提供冷剂蒸汽，新增发生器 A的浓溶液经新增溶液泵 D和 新增溶液热交换器 B之后与第一发生器 1经溶液泵 7和第一溶液热交换器 10之后的浓溶液 汇合、 再经第二溶液热交换器 11进入第二发生器 2， 流经新增发生器 A的冷剂蒸汽放热成冷 剂液、 再经新增节流阀 C节流进入第一冷凝器 4， 形成单效 -双效第三类吸收式热泵。  2 In the process, the dilute solution of the absorber 3 enters the newly added generator A through the newly added solution heat exchanger B, and the refrigerant vapor generated by the first generator 1 is supplied to the newly added generator A as the driving heat medium, the refrigerant vapor Flowing through the new generator A, heating the solution into it and releasing the refrigerant vapor to the first condenser 4, adding the concentrated solution of the generator A after adding the solution pump D and the new solution heat exchanger B Converging with the concentrated solution after the first generator 1 passes the solution pump 7 and the first solution heat exchanger 10, and then enters the second generator 2 via the second solution heat exchanger 11, flowing through the refrigerant of the newly added generator A The steam is exothermic into a refrigerant liquid, and then throttled into the first condenser 4 by a new throttle valve C to form a single-effect-double-effect third-type absorption heat pump.
图 14所示的单效 -双效第三类吸收式热泵是这样实现的：  The single-effect, double-effect, third-class absorption heat pump shown in Figure 14 is implemented as follows:
①结构上， 在图 1所示的第三类吸收式热泵中， 增加新增发生器、 新增溶液热交换器和 新增节流阀，将第一发生器 1有浓溶液管路经溶液泵 7和第一溶液热交换器 10与第二溶液热 交换器 11连通调整为第一发生器 1有浓溶液管路经新增溶液热交换器 B与新增发生器 A连通， 新增发生器 A还有浓溶液管路经溶液泵 7、 新增溶液热交换器 B和第一溶液热交换器 10与第 二溶液热交换器 11连通，将第一发生器 1有冷剂蒸汽通道与第一冷凝器 4连通调整为第一发 生器 1有冷剂蒸汽通道与新增发生器 A连通后新增发生器 A再有冷剂液管路经新增节流阀 C 与第一冷凝器 4连通， 新增发生器 A还有冷剂蒸汽通道与第一冷凝器 4连通。  1Structurally, in the third type of absorption heat pump shown in Fig. 1, a new generator, a new solution heat exchanger and a new throttle valve are added, and the first generator 1 has a concentrated solution pipeline through the solution. The pump 7 and the first solution heat exchanger 10 are connected to the second solution heat exchanger 11 to be adjusted so that the first generator 1 has a concentrated solution line connected to the newly added generator A via the new solution heat exchanger B, and newly added occurs. The A and the concentrated solution line are connected to the second solution heat exchanger 11 via the solution pump 7, the new solution heat exchanger B and the first solution heat exchanger 10, and the first generator 1 has a refrigerant vapor channel and The first condenser 4 is connected to be adjusted so that the first generator 1 has a refrigerant vapor passage connected with the newly added generator A, and then the generator A is newly added, and the refrigerant liquid pipeline is added through the newly added throttle valve C and the first condenser. 4 connected, the new generator A and the refrigerant vapor passage are in communication with the first condenser 4.
②流程上， 第一发生器 1的浓溶液经新增溶液热交换器 B新增发生器 A， 第一发生器 1 产生的冷剂蒸汽提供给新增发生器 A作驱动热介质， 冷剂蒸汽流经新增发生器 A、 加热进入 其内的溶液释放并向第一冷凝器 4提供冷剂蒸汽， 新增发生器 A的浓溶液经溶液泵 7、 新增 溶液热交换器 B、第一溶液热交换器 10和第二溶液热交换器 11进入第二发生器 2，流经新增 发生器 A的冷剂蒸汽放热成冷剂液、再经新增节流阀 C进入第一冷凝器 4， 形成单效-双效第 三类吸收式热泵。  2 In the process, the concentrated solution of the first generator 1 is newly added to the generator A via the new solution heat exchanger B, and the refrigerant vapor generated by the first generator 1 is supplied to the newly added generator A for driving the heat medium, the refrigerant The steam flows through the newly added generator A, the solution heated into it is released, and the refrigerant vapor is supplied to the first condenser 4, and the concentrated solution of the generator A is newly added to the solution pump 7, the new solution heat exchanger B, the first A solution heat exchanger 10 and a second solution heat exchanger 11 enter the second generator 2, and the refrigerant vapor flowing through the newly added generator A is released into a refrigerant liquid, and then enters the first through the new throttle valve C. The condenser 4 forms a single-effect double-effect third type absorption heat pump.
图 15所示的单效 -双效第三类吸收式热泵是这样实现的：  The single-effect, double-effect, third-class absorption heat pump shown in Figure 15 is implemented as follows:
①结构上， 在图 1所示的第三类吸收式热泵中， 增加新增发生器、 新增溶液热交换器、 新增节流阀和新增溶液泵， 将吸收器 3有稀溶液管路经第一溶液热交换器 10与第一发生器 1 连通调整为吸收器 3有稀溶液管路经第一溶液热交换器 10和新增溶液热交换器 B与新增发生 器 A连通， 新增发生器 A还有浓溶液管路经新增溶液泵 D和新增溶液热交换器 B与第一发生 器 1连通， 将第一发生器 1有冷剂蒸汽通道与第一冷凝器 4连通调整为第一发生器 1有冷剂 蒸汽通道与新增发生器 A连通后新增发生器 A再有冷剂液管路经新增节流阀 C与第一冷凝器 4连通， 新增发生器 A还有冷剂蒸汽通道与第一冷凝器 4连通。 1Structure, in the third type of absorption heat pump shown in Figure 1, adding new generators, new solution heat exchangers, A new throttle valve and a new solution pump are added, and the dilute solution line of the absorber 3 is connected to the first generator 1 through the first solution heat exchanger 10 to be adjusted to the absorber 3, and the dilute solution line is heated by the first solution. The exchanger 10 and the new solution heat exchanger B are connected to the newly added generator A, and the new generator A and the concentrated solution pipeline are added to the new solution pump D and the new solution heat exchanger B and the first generator 1 Connected, the first generator 1 has a refrigerant vapor passage connected to the first condenser 4 to be adjusted to be the first generator 1 has a refrigerant vapor passage connected with the newly added generator A, and then adds the generator A and then the refrigerant liquid The pipeline is connected to the first condenser 4 via a new throttle valve C, and a new generator A and a refrigerant vapor passage are connected to the first condenser 4.
②流程上， 吸收器 3的稀溶液经第一溶液热交换器 10和新增溶液热交换器 B进入新增 发生器 A， 第一发生器 1产生的冷剂蒸汽提供给新增发生器 A作驱动热介质， 冷剂蒸汽流经 新增发生器 A、 加热进入其内的溶液释放并向第一冷凝器 4提供冷剂蒸汽， 新增发生器 A的 浓溶液经新增溶液泵 D和新增溶液热交换器 B进入第一发生器 1，流经新增发生器 A的冷剂 蒸汽放热成冷剂液、再经新增节流阀 C进入第一冷凝器 4，形成单效 -双效第三类吸收式热泵。  2 In the process, the dilute solution of the absorber 3 enters the newly added generator A through the first solution heat exchanger 10 and the newly added solution heat exchanger B, and the refrigerant vapor generated by the first generator 1 is supplied to the newly added generator A. As the driving heat medium, the refrigerant vapor flows through the newly added generator A, the solution heated into the solution is released, and the refrigerant vapor is supplied to the first condenser 4, and the concentrated solution of the generator A is newly added through the new solution pump D and The new solution heat exchanger B enters the first generator 1, and the refrigerant vapor flowing through the newly added generator A is released into a refrigerant liquid, and then enters the first condenser 4 through the newly added throttle valve C to form a single effect. - Double-effect third-class absorption heat pump.
图 16所示的单效 -三效第三类吸收式热泵是这样实现的：  The single-effect, three-effect, third-class absorption heat pump shown in Figure 16 is implemented as follows:
①结构上， 在图 13所示的第三类吸收式热泵中， 增加新增第二发生器、 新增第二溶液热 交换器、 新增第二节流陶和新增第二溶液泵， 吸收器 3增设稀溶液管路经新增第二溶液热交 换器 F与新增第二发生器 E连通， 新增第二发生器 E还有浓溶液管路经新增第二溶液泵 H和 新增第二溶液热交换器 F之后与第一发生器 1经溶液泵 7和第一溶液热交换器 10之后的浓溶 液管路汇合， 将新增第一发生器 A有冷剂蒸汽通道与第一冷凝器 4连通调整为新增第一发生 器 A有冷剂蒸汽通道与新增第二发生器 E连通后新增第二发生器 E再有冷剂液管路经新增第 二节流阀 G与第一冷凝器 4连通，新增第二发生器 E还有冷剂蒸汽通道与第一冷凝器 4连通。  1Structurally, in the third type of absorption heat pump shown in FIG. 13, adding a new second generator, adding a second solution heat exchanger, adding a second throttle pottery, and adding a second solution pump, The addition of the dilute solution pipeline to the absorber 3 is connected to the newly added second generator E by adding the second solution heat exchanger F, and the second generator E and the concentrated solution pipeline are newly added by the second solution pump H and After the addition of the second solution heat exchanger F, it merges with the concentrated solution line after the first generator 1 passes the solution pump 7 and the first solution heat exchanger 10, and the first generator A is added with the refrigerant vapor channel and The first condenser 4 is connected and adjusted to add a new first generator A. The refrigerant vapor channel is connected with the newly added second generator E, and the second generator E is added, and then the refrigerant liquid pipeline is added by the second section. The flow valve G is in communication with the first condenser 4, and the second generator E and the refrigerant vapor passage are connected to communicate with the first condenser 4.
②流程上， 吸收器 3的部分稀溶液经新增第二溶液热交换器 F进入新增第二发生器 E， 新增第一发生器 A产生的冷剂蒸汽提供给新增第二发生器 E作驱动热介质， 冷剂蒸汽流经新 增第二发生器 E、 加热进入其内的溶液释放并向第一冷凝器 4提供冷剂蒸汽， 新增第二发生 器 E的浓溶液经新增第二溶液泵 H和新增第二溶液热交换器 F之后与第一发生器 1经溶液泵 7和第一溶液热交换器 10之后的浓溶液汇合、 再经第二溶液热交换器 11进入第二发生器 2， 流经新增第二发生器 E的冷剂蒸汽放热成冷剂液、再经新增第二节流阀 G进入第一冷凝器 4， 形成单效-三效第三类吸收式热泵。  2 In the process, a part of the dilute solution of the absorber 3 is added to the second solution heat exchanger F to enter the newly added second generator E, and the refrigerant vapor generated by the first generator A is newly added to the second generator. E is used to drive the heat medium, and the refrigerant vapor flows through the newly added second generator E, the solution heated into it is released, and the refrigerant vapor is supplied to the first condenser 4, and the concentrated solution of the second generator E is newly added. After adding the second solution pump H and adding the second solution heat exchanger F, it is merged with the concentrated solution after the first generator 1 passes the solution pump 7 and the first solution heat exchanger 10, and then passes through the second solution heat exchanger 11 Entering the second generator 2, the refrigerant vapor flowing through the newly added second generator E is radiated into the refrigerant liquid, and then the second throttle valve G is added to enter the first condenser 4, forming a single-effect-three effect The third type of absorption heat pump.
图 17所示的单效 -三效第三类吸收式热泵是这样实现的：  The single-effect, three-effect, third-class absorption heat pump shown in Figure 17 is implemented as follows:
①结构上， 在图 14所示的第三类吸收式热泵中， 增加新增第二发生器、 新增第二溶液热 交换器和新增第二节流阔， 将新增第一发生器 A有浓溶液管路经溶液泵 7、 新增第一溶液热 交换器 B和第一溶液热交换器 10与第二溶液热交换器 11连通调整为新增第一发生器 A有浓 溶液管路经新增第二溶液热交换器 F与新增第二发生器 E连通， 新增第二发生器 E还有浓溶 液管路经溶液泵 7、新增第二溶液热交换器£、新增第一溶液热交换器 B和第一溶液热交换器 10与第二溶液热交换器 11连通， 将新增第一发生器 A有冷剂蒸汽通道与第一冷凝器 4连通 调整为新增第一发生器 A有冷剂蒸汽通道与新增第二发生器 E连通后新增第二发生器 E再有 冷剂液管路经新增第二节流阀 G与第一冷凝器 4连通， 新增第二发生器 E还有冷剂蒸汽通道 与第一冷凝器 4连通。  1Structurally, in the third type of absorption heat pump shown in Figure 14, the addition of the second generator, the addition of the second solution heat exchanger and the addition of the second section of the flow, the first generator will be added. A concentrated solution line is connected to the solution pump 7, the first solution heat exchanger B and the first solution heat exchanger 10 are connected to the second solution heat exchanger 11 to be newly added to the first generator A with a concentrated solution tube. The second solution heat exchanger F is newly connected with the newly added second generator E, and the second generator E and the concentrated solution pipeline are added through the solution pump 7, and the second solution heat exchanger is added. The first solution heat exchanger B and the first solution heat exchanger 10 are connected to the second solution heat exchanger 11 to adjust the newly added first generator A refrigerant vapor passage to the first condenser 4 to be newly added. The first generator A has a refrigerant vapor passage connected with the newly added second generator E, and then adds a second generator E and then a refrigerant liquid pipeline is connected to the first condenser 4 via a new second throttle valve G. The second generator E and the refrigerant vapor passage are connected to the first condenser 4.
②流程上， 新增第一发生器 A的浓溶液经新增第二溶液热交换器 F进入新增第二发生器 E, 新增第一发生器 A产生的冷剂蒸汽提供给新增第二发生器 E作驱动热介质， 冷剂蒸汽流 经新增第二发生器 E、 加热进入其内的溶液释放并向第一冷凝器 4提供冷剂蒸汽， 新增第二 发生器 E的浓溶液经溶液泵 7、新增第二溶液热交换器？、新增第一溶液热交换器8、第一溶 液热交换器 10和第二溶液热交换器 11进入第二发生器 2， 流经新增第二发生器 E的冷剂蒸 汽放热成冷剂液、 再经新增第二节流阀 G进入第一冷凝器 4， 形成单效-三效第三类吸收式热 泵。 2 In the process, the concentrated solution of the first generator A is newly added to the second solution E by adding the second solution heat exchanger F, and the refrigerant vapor generated by the first generator A is newly added to the new one. The second generator E serves as a driving heat medium, and the refrigerant vapor flows through the newly added second generator E, the solution heated into the solution is released, and the refrigerant vapor is supplied to the first condenser 4, and the second generator E is added. The solution is passed through the solution pump 7, and the second solution heat exchanger is added. , adding the first solution heat exchanger 8, the first solution The liquid heat exchanger 10 and the second solution heat exchanger 11 enter the second generator 2, and the refrigerant vapor flowing through the newly added second generator E is radiated into a refrigerant liquid, and then the second throttle valve G is added. Entering the first condenser 4, a single-effect three-effect third type absorption heat pump is formed.
图 18所示的单效 -三效第三类吸收式热泵是这样实现的：  The single-effect, three-effect, third-class absorption heat pump shown in Figure 18 is implemented as follows:
①结构上， 在图 15所示的第三类吸收式热泵中， 增加新增第二发生器、 新增第二溶液热 交换器、 新增第二节流阀和新增第二溶液泵， 将吸收器 3有稀溶液管路经第一溶液热交换器 10和新增第一溶液热交换器 B与新增第一发生器 A连通调整为吸收器 3有稀溶液管路经第一 溶液热交换器 10、 新增第一溶液热交换器 B和新增第二溶液热交换器 F与新增第二发生器 E 连通， 新增第二发生器 E还有浓溶液管路经新增第二溶液泵 H和新增第二溶液热交换器 F与 新增第一发生器 A连通， 将新增第一发生器 A有冷剂蒸汽通道与第一冷凝器 4连通调整为新 增第一发生器 A有冷剂蒸汽通道与新增第二发生器 E连通后新增第二发生器 E再有冷剂液管 路经新增第二节流阀 G与第一冷凝器 4连通， 新增第二发生器 E还有冷剂蒸汽通道与第一冷 凝器 4连通。  1Structurally, in the third type of absorption heat pump shown in FIG. 15, a new second generator is added, a second solution heat exchanger is added, a second throttle valve is added, and a second solution pump is added. The absorber 3 has a dilute solution line through the first solution heat exchanger 10 and the newly added first solution heat exchanger B and the newly added first generator A is connected to adjust the absorber 3 to have a dilute solution line through the first solution The heat exchanger 10, the newly added first solution heat exchanger B and the newly added second solution heat exchanger F are connected with the newly added second generator E, and the second generator E and the concentrated solution pipeline are newly added. The second solution pump H and the newly added second solution heat exchanger F are in communication with the newly added first generator A, and the newly added first generator A has a refrigerant vapor passage connected to the first condenser 4 to be newly added. A generator A has a refrigerant vapor passage connected with the newly added second generator E, and then a second generator E is added, and then a refrigerant liquid pipeline is connected to the first condenser 4 via a new second throttle valve G. A second generator E is added and a refrigerant vapor passage is connected to the first condenser 4.
②流程上， 吸收器 3的稀溶液经第一溶液热交换器 10、新增第一溶液热交换器 B和新增 第二溶液热交换器 F进入新增第二发生器 E， 新增第一发生器 A产生的冷剂蒸汽提供给新增 第二发生器 E作驱动热介质， 冷剂蒸汽流经新增第二发生器 E、 加热进入其内的溶液释放并 向第一冷凝器 4提供冷剂蒸汽， 新增第二发生器 E的浓溶液经新增第二溶液泵 H和新增第二 溶液热交换器 F进入新增第一发生器 A， 流经新增第二发生器 E的冷剂蒸汽放热成冷剂液、 再经新增第二节流阀 G进入第一冷凝器 4， 形成单效 -三效第三类吸收式热泵。  2 In the process, the dilute solution of the absorber 3 enters the newly added second generator E through the first solution heat exchanger 10, the newly added first solution heat exchanger B, and the newly added second solution heat exchanger F, adding a new The refrigerant vapor generated by a generator A is supplied to the newly added second generator E as a driving heat medium, and the refrigerant vapor flows through the newly added second generator E, and the solution heated into the same is released to the first condenser 4 Providing refrigerant vapor, adding a concentrated solution of the second generator E to the newly added first generator A by adding a second solution pump H and adding a second solution heat exchanger F, flowing through the newly added second generator The refrigerant vapor of E is exothermic into a refrigerant liquid, and then added to the second throttle valve G to enter the first condenser 4 to form a single-effect-three-effect third type absorption heat pump.
图 19所示的单效 -回热式双效第三类吸收式热泵是这样实现的：  The single-effect-recovery double-effect third-class absorption heat pump shown in Figure 19 is implemented as follows:
①结构上， 在图 2所示的第三类吸收式热泵中， 增加新增发生器、 新增溶液热交换器和 新增节流阀， 第二溶液泵 14增设稀溶液管路经新增溶液热交换器 B与新增发生器 A连通， 新 增发生器 A还有浓溶液管路经新增溶液热交换器 B与第三发生器 12连通，将第一发生器 1有 冷剂蒸汽通道与第一冷凝器 4连通调整为第一发生器 1有冷剂蒸汽通道与新增发生器 A连通 后新增发生器 A再有冷剂液管路经新增节流阔 C与第一冷凝器 4连通， 新增发生器 A还有冷 剂蒸汽通道与第一冷凝器 4连通。  1Structurally, in the third type of absorption heat pump shown in FIG. 2, a new generator, a new solution heat exchanger and a new throttle valve are added, and a second solution pump 14 is added with a dilute solution pipeline. The solution heat exchanger B is in communication with the newly added generator A, and the new generator A and the concentrated solution line are connected to the third generator 12 via the new solution heat exchanger B, and the first generator 1 has refrigerant vapor. The passage is connected to the first condenser 4 to be adjusted so that the first generator 1 has a refrigerant vapor passage connected with the newly added generator A, and then the new generator A is added and the refrigerant liquid pipeline is added with a new throttle C and the first The condenser 4 is connected, and the newly added generator A and the refrigerant vapor passage are in communication with the first condenser 4.
②流程上， 第二吸收器 13的部分稀溶液经第二溶液泵 14和新增溶液热交换器 B进入新 增发生器八， 第一发生器 1产生的冷剂蒸汽提供给新增发生器 A作驱动热介质， 冷剂蒸汽流 经新增发生器 A、 加热进入其内的溶液释放并向第一冷凝器 4提供冷剂蒸汽， 新增发生器 A 的浓溶液经新增溶液热交换器 B进入第三发生器 12，流经新增发生器 A的冷剂蒸汽放热成冷 剂液、 再经新增节流阀 C节流进入第一冷凝器 4， 形成单效 -回热式双效第三类吸收式热泵。  2 In the process, a part of the dilute solution of the second absorber 13 enters the newly added generator 8 through the second solution pump 14 and the newly added solution heat exchanger B, and the refrigerant vapor generated by the first generator 1 is supplied to the newly added generator. A acts as a driving heat medium, and the refrigerant vapor flows through the newly added generator A, and the solution heated therein is released and supplies the refrigerant vapor to the first condenser 4, and the concentrated solution of the new generator A is heated by the added solution. The device B enters the third generator 12, and the refrigerant vapor flowing through the newly added generator A is radiated into a refrigerant liquid, and then throttled into the first condenser 4 through the addition of a new throttle valve C to form a single-effect heat. Double-effect third-class absorption heat pump.
图 20所示的单效 -回热式双效第三类吸收式热泵是这样实现的：  The single-effect-recovery double-effect third-class absorption heat pump shown in Figure 20 is implemented as follows:
①结构上， 在图 2所示的第三类吸收式热泵中， 增加新增发生器、 新增溶液热交换器和 新增节流阔， 将第二溶液泵 14有稀溶液管路经第三溶液热交换器 15与第一发生器 1连通调 整为第二溶液泵 14有稀溶液管路经新增溶液热交换器 B和第三溶液热交换器 15与第一发生 器 1连通， 将第一发生器 1有浓溶液管路经第三溶液热交换器 15与第三发生器 12连通调整 为第一发生器 1有浓溶液管路经第三溶液热交换器 15与新增发生器 A连通，新增发生器 A还 有浓溶液管路经新增溶液热交换器 B与第三发生器 12连通，将第一发生器 1有冷剂蒸汽通道 与第一冷凝器 4连通调整为第一发生器 1有冷剂蒸汽通道与新增发生器 A连通后新增发生器 A再有冷剂液管路经新增节流阀 C与第一冷凝器 4连通， 新增发生器 A还有冷剂蒸汽通道与 第一冷凝器 4连通。 1Structurally, in the third type of absorption heat pump shown in Fig. 2, the new generator, the new solution heat exchanger and the new throttle are added, and the second solution pump 14 has a dilute solution pipeline. The three-solution heat exchanger 15 is connected to the first generator 1 to be adjusted to be a second solution pump 14 having a dilute solution line connected to the first generator 1 via the new solution heat exchanger B and the third solution heat exchanger 15 The first generator 1 has a concentrated solution line connected to the third generator 12 via the third solution heat exchanger 15 and is adjusted to be a first generator 1 having a concentrated solution line through the third solution heat exchanger 15 and a new generator A communication, the new generator A and the concentrated solution pipeline are connected to the third generator 12 via the new solution heat exchanger B, and the first generator 1 has a refrigerant vapor passage connected to the first condenser 4 to be adjusted to The first generator 1 has a refrigerant vapor passage connected with the newly added generator A, and then adds a generator A and then a refrigerant liquid pipeline is connected to the first condenser 4 via a new throttle valve C, and a new generator A is added. There are also refrigerant vapor channels and The first condenser 4 is in communication.
②流程上， 第二吸收器 13的稀溶液经第二溶液泵 14、 新增溶液热交换器 B和第三溶液 热交换器 15进入第一发生器 1， 第一发生器 1的浓溶液经第三溶液热交换器 15进入新增发 生器 A， 新增发生器 A的浓溶液经新增溶液热交换器 B进入第三发生器 12; 第一发生器 1 产生的冷剂蒸汽提供给新增发生器 A作驱动热介质， 冷剂蒸汽流经新增发生器 A、 加热进入 其内的溶液释放并向第一冷凝器 4提供冷剂蒸汽， 流经新增发生器 A的冷剂蒸汽放热成冷剂 液、 再经新增节流阔 C节流进入第一冷凝器 4， 形成单效 -回热式双效第三类吸收式热泵。  In the second process, the dilute solution of the second absorber 13 enters the first generator 1 via the second solution pump 14, the new solution heat exchanger B and the third solution heat exchanger 15, and the concentrated solution of the first generator 1 is The third solution heat exchanger 15 enters the newly added generator A, and the concentrated solution of the newly added generator A enters the third generator 12 via the newly added solution heat exchanger B; the refrigerant vapor generated by the first generator 1 is supplied to the new The generator A is driven to drive the heat medium, and the refrigerant vapor flows through the newly added generator A, and the solution heated therein is released and supplies the refrigerant vapor to the first condenser 4, and flows through the refrigerant vapor of the newly added generator A. The exotherm is formed into a refrigerant liquid, and then added to the first condenser 4 by a new throttled C-throttle to form a single-effect-recovery double-effect third-class absorption heat pump.
图 21所示的单效 -回热式双效第三类吸收式热泵是这样实现的：  The single-effect-recovery double-effect third-class absorption heat pump shown in Figure 21 is implemented as follows:
在图 20所示的第三类吸收式热泵中， 取消第三发生器 12与外部连通的余热介质管路， 增加新增第二节流阀， 第一发生器 1增设冷剂蒸汽通道与第三发生器 12连通后第三发生器 12再有冷剂液管路经新增第二节流阀 G与第一冷凝器 4连通； 第一发生器 1产生的冷剂蒸汽 分别提供给新增发生器 A和第三发生器 12作驱动热介质， 流经第三发生器 12的冷剂蒸汽放 热成冷剂液、 再经新增第二节流阀 G节流进入第一冷凝器 4， 形成以回热式双效为低温发生 流程的第三类吸收式热泵。  In the third type of absorption heat pump shown in FIG. 20, the residual heat medium line connecting the third generator 12 with the outside is canceled, and the second throttle valve is added, and the first generator 1 is provided with a refrigerant vapor passage and the first After the three generators 12 are connected, the third generator 12 has a refrigerant liquid pipeline connected to the first condenser 4 via the addition of the second throttle valve G; the refrigerant vapor generated by the first generator 1 is separately supplied to the new generator The generator A and the third generator 12 act as a driving heat medium, and the refrigerant vapor flowing through the third generator 12 is radiated into a refrigerant liquid, and then throttled into the first condenser 4 by adding a second throttle valve G. A third type of absorption heat pump with a regenerative double effect as a low temperature generation process is formed.
图 22所示的单效 -回热式双效第三类吸收式热泵是这样实现的：  The single-effect-recovery double-effect third-class absorption heat pump shown in Figure 22 is implemented as follows:
①结构上， 在图 2所示的第三类吸收式热泵中， 增加新增发生器、 新增溶液热交换器、 新增节流阀和新增溶液泵， 将第二溶液泵 14有稀溶液管路经第三溶液热交换器 15与第一发 生器 1连通调整为第二溶液泵 14有稀溶液管路经第三溶液热交换器 15与新增发生器 A连通， 新增发生器 A还有浓溶液管路经新增溶液泵 D和新增溶液热交换器 B与第一发生器 1连通， 将第一发生器 1有浓溶液管路经第三溶液热交换器 15与第三发生器 12连通调整为第一发生 器 1有浓溶液管路经新增溶液热交换器 B和第三溶液热交换器 15与第三发生器 12连通， 将 第一发生器 1有冷剂蒸汽通道与第一冷凝器 4连通调整为第一发生器 1有冷剂蒸汽通道与新 增发生器 A连通后新增发生器 A再有冷剂液管路经新增节流阀 C与第一冷凝器 4连通， 新增 发生器 A还有冷剂蒸汽通道与第一冷凝器 4连通。  1Structurally, in the third type of absorption heat pump shown in FIG. 2, a new generator, a new solution heat exchanger, a new throttle valve and a new solution pump are added, and the second solution pump 14 is diluted. The solution line is connected to the first generator 1 via the third solution heat exchanger 15 to be adjusted to be a second solution pump 14 having a dilute solution line connected to the newly added generator A via the third solution heat exchanger 15 to add a generator A also has a concentrated solution line connected to the first generator 1 via a new solution pump D and a new solution heat exchanger B, and the first generator 1 has a concentrated solution line through the third solution heat exchanger 15 and The three generators 12 are connected to be adjusted so that the first generator 1 has a concentrated solution line connected to the third generator 12 via the new solution heat exchanger B and the third solution heat exchanger 15, and the first generator 1 has a refrigerant. The steam passage is connected to the first condenser 4 to be adjusted so that the first generator 1 has a refrigerant vapor passage connected with the newly added generator A, and then the generator A is newly added, and the refrigerant liquid pipeline is added through the new throttle valve C and the first A condenser 4 is connected, and a new generator A and a refrigerant vapor passage are connected to the first condenser 4 through.
②流程上， 第一发生器 1产生的冷剂蒸汽提供给新增发生器 A作驱动热介质， 第一发生 器 1的浓溶液经新增溶液热交换器 B和第三溶液热交换器 15进入第三发生器 12; 第二吸收 器 13的稀溶液经第二溶液泵 14和第三溶液热交换器 15进入新增发生器 A，冷剂蒸汽流经新 增发生器八、 加热进入其内的溶液释放并向第一冷凝器 4提供冷剂蒸汽， 新增发生器 A的浓 溶液经新增溶液泵 D和新增溶液热交换器 B进入第一发生器 1，流经新增发生器 A的冷剂蒸 汽放热成冷剂液、 再经新增节流阀 C节流进入第一冷凝器 4， 形成单效-回热式双效第三类吸 收式热泵。  2 In the process, the refrigerant vapor generated by the first generator 1 is supplied to the newly added generator A as a driving heat medium, and the concentrated solution of the first generator 1 is passed through the newly added solution heat exchanger B and the third solution heat exchanger 15 Entering the third generator 12; the dilute solution of the second absorber 13 enters the new generator A through the second solution pump 14 and the third solution heat exchanger 15, and the refrigerant vapor flows through the newly added generator. The solution inside releases and supplies the refrigerant vapor to the first condenser 4, and the concentrated solution of the newly added generator A enters the first generator 1 through the new solution pump D and the new solution heat exchanger B, and the flow occurs newly. The refrigerant vapor of the device A is radiated into a refrigerant liquid, and then throttled into the first condenser 4 by a new throttle valve C to form a single-effect-recovery double-effect third-class absorption heat pump.
图 23所示的单效 -回热式双效第三类吸收式热泵是这样实现的：  The single-effect-recovery double-effect third-class absorption heat pump shown in Figure 23 is implemented as follows:
①结构上， 在图 4所示的第三类吸收式热泵中， 取消吸收-发生器 16与外部连通的被加 热介质管路， 增加新增发生器、 新增溶液热交换器和新增节流阀， 将第一发生器 1有浓溶液 管路经第一溶液泵 7、 第一溶液热交换器 10和吸收-发生器 16与分汽室 17连通调整为第一 发生器 1有浓溶液管路经第一溶液热交换器 10和吸收-发生器 16与分汽室 17连通， 吸收- 发生器 16增设稀溶液管路经新增溶液热交换器 B与新增发生器 A连通，新增发生器 A还有浓 溶液管路经第一溶液泵 Ί和新增溶液热交换器 B之后与第一发生器 1经第一溶液热交换器 10 之后的浓溶液管路汇合， 将第一发生器 1有冷剂蒸汽通道与第一冷凝器 4连通调整为第一发 生器 1有冷剂蒸汽通道与新增发生器 A连通后新增发生器 A再有冷剂液管路经新增节流阀 C 与第一冷凝器 4连通， 新增发生器 A还有冷剂蒸汽通道与第一冷凝器 4连通。 1Structurally, in the third type of absorption heat pump shown in FIG. 4, the heated medium line connecting the absorption-generator 16 to the outside is eliminated, and the new generator, the new solution heat exchanger and the new section are added. a flow valve, the first generator 1 has a concentrated solution pipeline connected to the first solution pump 7, the first solution heat exchanger 10, and the absorption-generator 16 and the steam distribution chamber 17 to be adjusted to have a concentrated solution of the first generator 1 The pipeline is connected to the steam distribution chamber 17 via the first solution heat exchanger 10 and the absorption-generator 16 , and the absorption-generator 16 is provided with a dilute solution pipeline connected to the newly added generator A via the new solution heat exchanger B. The generator A and the concentrated solution line are merged with the concentrated solution line after the first solution 1 passes through the first solution heat exchanger 10 via the first solution pump and the new solution heat exchanger B, and will be first The generator 1 has a refrigerant vapor passage communicating with the first condenser 4 to adjust the first generator 1 to have a refrigerant vapor passage and the new generator A is connected, and the new generator A is added and the refrigerant liquid pipeline is newly added. Throttle valve C In communication with the first condenser 4, a new generator A and a refrigerant vapor passage are in communication with the first condenser 4.
②流程上， 吸收-发生器 16的部分稀溶液经新增溶液热交换器 B进入新增发生器 A， 第 一发生器 1产生的冷剂蒸汽提供给新增发生器 A作驱动热介质， 第一发生器 1的浓溶液经第 一溶液热交换器 10升温降压后再流经吸收-发生器 16、 吸热部分汽化进入分汽室 17; 冷剂蒸 汽流经新增发生器 A、 加热进入其内的溶液释放并向第一冷凝器 4提供冷剂蒸汽， 新增发生 器 A的浓溶液经第一溶液泵 7和新增溶液热交换器 B之后与第一发生器 1经第一溶液热交换 器 10之后的浓溶液管路汇合、 再流经吸收-发生器 16、 吸热部分汽化进入分汽室 17， 流经新 增发生器 A的冷剂蒸汽放热成冷剂液、再经新增节流阀 C节流进入第一冷凝器 4， 形成单效- 回热式双效第三类吸收式热泵。  2 In the process, a part of the dilute solution of the absorption-generator 16 enters the newly added generator A through the newly added solution heat exchanger B, and the refrigerant vapor generated by the first generator 1 is supplied to the newly added generator A as a driving heat medium. The concentrated solution of the first generator 1 is heated and depressurized by the first solution heat exchanger 10, then flows through the absorption-generator 16, and the endothermic portion is vaporized into the steam dividing chamber 17; the refrigerant vapor flows through the newly added generator A, The solution heated into the solution is released and the refrigerant vapor is supplied to the first condenser 4, and the concentrated solution of the new generator A is added to the first generator 1 through the first solution pump 7 and the newly added solution heat exchanger B. The concentrated solution line after the solution heat exchanger 10 merges, flows through the absorption-generator 16, and the heat absorption portion vaporizes into the steam separation chamber 17, and the refrigerant vapor flowing through the newly added generator A is released into a refrigerant liquid. Then, the new throttle valve C is throttled into the first condenser 4 to form a single-effect-recovery double-effect third-class absorption heat pump.
图 24所示的单效 -回热式双效第三类吸收式热泵是这样实现的：  The single-effect-recovery double-effect third-class absorption heat pump shown in Figure 24 is implemented as follows:
①结构上， 在图 4所示的第三类吸收式热泵中， 取消吸收-发生器 16与外部连通的被加 热介质管路， 取消第三溶液泵 21， 吸收器 3有稀溶液管路经第三溶液热交换器 15与吸收-发 生器 16连通； 增加新增发生器、 新增节流阀和新增溶液节流阀， 将第一发生器 1有浓溶液管 路经第一溶液泵 7、 第一溶液热交换器 10和吸收-发生器 16与分汽室 17连通调整为第一发 生器 1有浓溶液管路经溶液节流阀 J和吸收-发生器 16与分汽室 17连通， 将吸收-发生器 16 有稀溶液管路经第一溶液热交换器 10与第一发生器 1连通调整为吸收-发生器 16有稀溶液管 路直接与第一发生器 1连通，吸收-发生器 16增设稀溶液管路经第一溶液热交换器 10与新增 发生器 A连通，新增发生器 A还有浓溶液管路经第一溶液泵 7和第一溶液热交换器 10之后与 第一发生器 1经溶液节流阀 J之后的浓溶液管路汇合， 将第一发生器 1有冷剂蒸汽通道与第 一冷凝器 4连通调整为第一发生器 1有冷剂蒸汽通道与新增发生器 A连通后新增发生器 A再 有冷剂液管路经新增节流阀 C与第一冷凝器 4连通， 新增发生器 A还有冷剂蒸汽通道与第一 冷凝器 4连通； 取消蒸发器 6与吸收-发生器 16连通的冷剂蒸汽通道， 第一发生器 1增设冷 剂蒸汽通道与吸收-发生器 16连通。  1 Structurally, in the third type of absorption heat pump shown in FIG. 4, the heated medium line in which the absorption-generator 16 communicates with the outside is canceled, the third solution pump 21 is eliminated, and the absorber 3 has a dilute solution line. The third solution heat exchanger 15 is in communication with the absorption-generator 16; a new generator, a new throttle valve and a new solution throttle valve are added, and the first generator 1 has a concentrated solution line through the first solution pump 7. The first solution heat exchanger 10 and the absorption-generator 16 are connected to the steam dividing chamber 17 to be adjusted so that the first generator 1 has a concentrated solution line through the solution throttle valve J and the absorption-generator 16 and the steam dividing chamber 17 Connected, the absorption-generator 16 has a dilute solution line connected to the first generator 1 through the first solution heat exchanger 10 to be adjusted to absorb-the generator 16 has a dilute solution line directly connected to the first generator 1 to absorb - The generator 16 is provided with a dilute solution line connected to the newly added generator A via the first solution heat exchanger 10, and the new generator A and the concentrated solution line are passed through the first solution pump 7 and the first solution heat exchanger 10 After that, the concentrated solution after the first generator 1 passes through the solution throttle valve J The road merges, the first generator 1 has a refrigerant vapor passage connected to the first condenser 4 to be adjusted to be the first generator 1 has a refrigerant vapor passage connected with the newly added generator A, and then adds the generator A and then has a refrigerant. The liquid pipeline is connected to the first condenser 4 via a new throttle valve C, and the new generator A and the refrigerant vapor passage are connected to the first condenser 4; the cold connection between the evaporator 6 and the absorption-generator 16 is cancelled. The agent steam passage, the first generator 1 is provided with a refrigerant vapor passage communicating with the absorption-generator 16.
②流程上， 吸收器 3的稀溶液经第三溶液热交换器 15降温降压后进入吸收-发生器 16、 吸收来自第一发生器 1 的冷剂蒸汽并放热于流经吸收-发生器 16的溶液； 吸收-发生器 16的 稀溶液分成两路——第一路直接进入第一发生器 1， 第二路经第一溶液热交换器 10进入新增 发生器 A; 第一发生器 1产生的冷剂蒸汽分别提供给新增发生器 A和吸收-发生器 16, 第一 发生器 1的浓溶液经新增溶液节流阀 J节流后再流经吸收-发生器 16、吸热部分汽化进入分汽 室 17; 冷剂蒸汽流经新增发生器 A、 加热进入其内的溶液释放并向第一冷凝器 4提供冷剂蒸 汽， 新增发生器 A的浓溶液经第一溶液泵 7和第一溶液热交换器 10之后再流经吸收-发生器 16、 吸热部分汽化进入分汽室 17， 流经新增发生器 A的冷剂蒸汽放热成冷剂液、 再经新增节 流阀 C节流进入第一冷凝器 4， 形成单效 -回热式双效第三类吸收式热泵。  2 In the process, the diluted solution of the absorber 3 is cooled down by the third solution heat exchanger 15 to enter the absorption-generator 16, absorbs the refrigerant vapor from the first generator 1, and radiates heat through the absorption-generator. The solution of 16; the dilute solution of the absorption-generator 16 is divided into two paths - the first path directly enters the first generator 1, and the second path passes through the first solution heat exchanger 10 to enter the new generator A; 1 The generated refrigerant vapor is supplied to the newly added generator A and the absorption-generator 16, respectively, and the concentrated solution of the first generator 1 is throttled by the added solution throttle valve J, and then flows through the absorption-generator 16, sucking The hot portion is vaporized into the steam dividing chamber 17; the refrigerant vapor flows through the newly added generator A, the solution heated into it is released, and the refrigerant vapor is supplied to the first condenser 4, and the concentrated solution of the generator A is newly added. The solution pump 7 and the first solution heat exchanger 10 are then passed through the absorption-generator 16, and the endothermic portion is vaporized into the steam dividing chamber 17, and the refrigerant vapor flowing through the newly added generator A is released into a refrigerant liquid, and then After the new throttle valve C is throttled into the first condenser 4, a single effect is formed - Regenerative double-effect third-class absorption heat pump.
图 25所示的单效 -回热式双效第三类吸收式热泵是这样实现的- The single-effect-recovery double-effect third-class absorption heat pump shown in Figure 25 is realized in this way -
①结构上， 在图 4所示的第三类吸收式热泵中， 取消吸收-发生器 16与外部连通的被加 热介质管路， 增加新增发生器、 新增溶液热交换器和新增节流阀， 将第一发生器 1有浓溶液 管路经第一溶液泵 7、 第一溶液热交换器 10和吸收-发生器 16与分汽室 17连通调整为第一 发生器 1有浓溶液管路经新增溶液热交换器 B与新增发生器 A连通， 新增发生器 A还有浓溶 液管路经第一溶液泵 7、 新增溶液热交换器 B、 第一溶液热交换器 10和吸收-发生器 16与分 汽室 17连通，将第一发生器 1有冷剂蒸汽通道与第一冷凝器 4连通调整为第一发生器 1有冷 剂蒸汽通道与新增发生器 A连通后新增发生器 A再有冷剂液管路经新增节流阀 C与第一冷凝 器 4连通， 新增发生器 A还有冷剂蒸汽通道与第一冷凝器 4连通。 1Structurally, in the third type of absorption heat pump shown in FIG. 4, the heated medium line connecting the absorption-generator 16 to the outside is eliminated, and the new generator, the new solution heat exchanger and the new section are added. a flow valve, the first generator 1 has a concentrated solution pipeline connected to the first solution pump 7, the first solution heat exchanger 10, and the absorption-generator 16 and the steam distribution chamber 17 to be adjusted to have a concentrated solution of the first generator 1 The pipeline is connected to the newly added generator A via the new solution heat exchanger B, and the new generator A and the concentrated solution pipeline are passed through the first solution pump 7, the new solution heat exchanger B, and the first solution heat exchanger. 10 and the absorption-generator 16 is in communication with the steam dividing chamber 17, and the first generator 1 has a refrigerant vapor passage communicating with the first condenser 4 to adjust the first generator 1 to have a refrigerant vapor passage and a new generator A. After the connection, the generator A is added and then the refrigerant liquid pipeline is added through the new throttle valve C and the first condensation. The device 4 is connected, and the newly added generator A and the refrigerant vapor passage are in communication with the first condenser 4.
②流程上， 第一发生器 1的浓溶液经新增溶液热交换器 B进入新增发生器 A， 第一发生 器 1产生的冷剂蒸汽提供给新增发生器 A作驱动热介质， 冷剂蒸汽流经新增发生器 A、 加热 进入其内的溶液释放并向第一冷凝器 4提供冷剂蒸汽， 新增发生器 A的浓溶液经第一溶液泵 7、 新增溶液热交换器 B和第一溶液热交换器 10之后再流经吸收-发生器 16、 吸热部分汽化 进入分汽室 17，流经新增发生器 A的冷剂蒸汽放热成冷剂液、再经新增节流阀 C节流进入第 一冷凝器 4， 形成单效 -回热式双效第三类吸收式热泵。  2 In the process, the concentrated solution of the first generator 1 enters the newly added generator A through the newly added solution heat exchanger B, and the refrigerant vapor generated by the first generator 1 is supplied to the newly added generator A as a driving heat medium, which is cold. The agent vapor flows through the newly added generator A, the solution heated into the solution is released, and the refrigerant vapor is supplied to the first condenser 4, and the concentrated solution of the generator A is newly added to the first solution pump 7, and the new solution heat exchanger B and the first solution heat exchanger 10 are then passed through the absorption-generator 16, and the endothermic portion is vaporized into the steam dividing chamber 17, and the refrigerant vapor flowing through the newly added generator A is released into a refrigerant liquid, and then passed through a new The throttle valve C is throttled into the first condenser 4 to form a single-effect-recovery double-effect third-class absorption heat pump.
图 26所示的单效 -回热式双效第三类吸收式热泵是这样实现的：  The single-effect-recovery double-effect third-class absorption heat pump shown in Figure 26 is implemented as follows:
①结构上， 在图 4所示的第三类吸收式热泵中， 取消吸收-发生器 16与外部连通的被加 热介质管路， 取消第三溶液泵， 吸收器 3有稀溶液管路经第三溶液热交换器 15与吸收 -发生 器 16连通； 增加新增发生器和新增节流阀， 将吸收-发生器 16有稀溶液管路经第一溶液热交 换器 10与第一发生器 1连通调整为吸收-发生器 16有稀溶液管路直接与第一发生器 1连通， 将第一发生器 1有浓溶液管路经第一溶液泵 7、 第一溶液热交换器 10和吸收-发生器 16与分 汽室 17连通调整为第一发生器 1有浓溶液管路经第一溶液热交换器 10与新增发生器 A连通， 新增发生器 A还有浓溶液管路经第一溶液泵 7、 第一溶液热交换器 10和吸收-发生器 16与分 汽室 17连通，将第一发生器 1有冷剂蒸汽通道与第一冷凝器 4连通调整为第一发生器 1有冷 剂蒸汽通道与新增发生器 A连通后新增发生器 A再有冷剂液管路经新增节流阀 C与第一冷凝 器 4连通， 新增发生器 A还有冷剂蒸汽通道与第一冷凝器 4连通； 取消蒸发器 6与吸收 -发生 器 16连通的冷剂蒸汽通道， 第一发生器 1增设冷剂蒸汽通道与吸收-发生器 16连通。  1Structurally, in the third type of absorption heat pump shown in FIG. 4, the heated medium line in which the absorption-generator 16 communicates with the outside is canceled, the third solution pump is canceled, and the absorber 3 has a dilute solution line through the first The three-solution heat exchanger 15 is in communication with the absorption-generator 16; an additional generator is added and a new throttle valve is added, and the absorption-generator 16 has a dilute solution line through the first solution heat exchanger 10 and the first generator 1 connected to the absorption-generator 16 has a dilute solution line directly connected to the first generator 1, the first generator 1 has a concentrated solution line through the first solution pump 7, the first solution heat exchanger 10 and absorption - The generator 16 is connected to the steam dividing chamber 17 to be adjusted so that the first generator 1 has a concentrated solution line connected to the newly added generator A via the first solution heat exchanger 10, and the newly added generator A and the concentrated solution line are The first solution pump 7, the first solution heat exchanger 10 and the absorption-generator 16 are in communication with the steam dividing chamber 17, and the first generator 1 has a refrigerant vapor passage connected to the first condenser 4 to be adjusted to the first generator. 1The refrigerant vapor channel is connected with the new generator A and newly added. Then, the refrigerant liquid pipeline is connected to the first condenser 4 via the newly added throttle valve C, and the new generator A and the refrigerant vapor passage are connected to the first condenser 4; the evaporator 6 and the absorption are cancelled. The coolant 16 is connected to the refrigerant vapor passage, and the first generator 1 is provided with a refrigerant vapor passage communicating with the absorption-generator 16.
②流程上， 吸收器 3的稀溶液经第三溶液热交换器 15降温降压后进入吸收-发生器 16、 吸收来自第一发生器 1的冷剂蒸汽并放热于流经吸收-发生器 16的溶液， 吸收-发生器 16的 稀溶液直接进入第一发生器 1， 第一发生器 1产生的冷剂蒸汽分别提供给新增发生器 A和吸 收-发生器 16， 第一发生器 1的浓溶液经第一溶液热交换器 10进入新增发生器 A; 冷剂蒸汽 流经新增发生器八、 加热进入其内的溶液释放并向第一冷凝器 4提供冷剂蒸汽， 新增发生器 A的浓溶液经第一溶液泵 7和第一溶液热交换器 10之后再流经吸收-发生器 16、 吸热部分汽 化进入分汽室 17，流经新增发生器 A的冷剂蒸汽放热成冷剂液、再经新增节流阀 C节流进入 第一冷凝器 4， 形成单效 -回热式双效第三类吸收式热泵。  2 In the process, the dilute solution of the absorber 3 is cooled down by the third solution heat exchanger 15 to enter the absorption-generator 16, absorbs the refrigerant vapor from the first generator 1, and radiates heat through the absorption-generator The solution of 16 , the dilute solution of the absorption-generator 16 directly enters the first generator 1, and the refrigerant vapor generated by the first generator 1 is supplied to the new generator A and the absorption-generator 16, respectively, the first generator 1 The concentrated solution enters the new generator A through the first solution heat exchanger 10; the refrigerant vapor flows through the newly added generator 8. The solution heated into the solution is released and supplies the refrigerant vapor to the first condenser 4, adding The concentrated solution of the generator A passes through the first solution pump 7 and the first solution heat exchanger 10 and then flows through the absorption-generator 16 to vaporize the heat absorption portion into the steam separation chamber 17, and flows through the refrigerant of the newly added generator A. The steam is exothermic into a refrigerant liquid, and then throttled into the first condenser 4 through a new throttle valve C to form a single-effect-recovery double-effect third-class absorption heat pump.
图 27所示的单效 -回热式双效第三类吸收式热泵是这样实现的：  The single-effect-recovery double-effect third-class absorption heat pump shown in Figure 27 is implemented as follows:
①结构上， 在图 4所示的第三类吸收式热泵中， 取消吸收-发生器 16与外部连通的被加 热介质管路， 增加新增发生器、 新增溶液热交换器、 新增节流阀和新增溶液泵， 将吸收 -发生 器 16有稀溶液管路经第一溶液热交换器 10与第一发生器 1连通调整为吸收-发生器 16有稀 溶液管路第一溶液热交换器 10和新增溶液热交换器 B与新增发生器 A连通，新增发生器 A还 有浓溶液管路经新增溶液泵 D和新增溶液热交换器 B与第一发生器 1连通， 将第一发生器 1 有冷剂蒸汽通道与第一冷凝器 4连通调整为第一发生器 1有冷剂蒸汽通道与新增发生器 A连 通后新增发生器 A再有冷剂液管路经新增节流阀 C与第一冷凝器 4连通， 新增发生器 A还有 冷剂蒸汽通道与第一冷凝器 4连通。  1Structurally, in the third type of absorption heat pump shown in FIG. 4, the heated medium line in which the absorption-generator 16 communicates with the outside is cancelled, the new generator, the new solution heat exchanger, and the new section are added. Flow valve and new solution pump, the absorption-generator 16 has a dilute solution line connected to the first generator 1 through the first solution heat exchanger 10 to adjust to absorption - the generator 16 has a dilute solution line first solution heat The exchanger 10 and the newly added solution heat exchanger B are in communication with the newly added generator A, and the new generator A and the concentrated solution pipeline are added to the new solution pump D and the new solution heat exchanger B and the first generator 1 Connected, the first generator 1 has a refrigerant vapor passage connected to the first condenser 4 to be adjusted to be the first generator 1 has a refrigerant vapor passage connected with the newly added generator A, and then adds the generator A and then the refrigerant liquid The pipeline is connected to the first condenser 4 via a new throttle valve C, and a new generator A and a refrigerant vapor passage are connected to the first condenser 4.
②流程上，吸收-发生器 16的稀溶液经第一溶液热交换器 10和新增溶液热交换器 B进入 新增发生器 A， 第一发生器 1产生的冷剂蒸汽提供给新增发生器 A作驱动热介质， 冷剂蒸汽 流经新增发生器八、 加热进入其内的溶液释放并向第一冷凝器 4提供冷剂蒸汽， 新增发生器 A的浓溶液经新增溶液泵 D和新增溶液热交换器 B进入第一发生器 1， 流经新增发生器 A的 冷剂蒸汽放热成冷剂液、 再经新增节流阀 C节流进入第一冷凝器 4， 形成单效-回热式双效第 三类吸收式热泵。 2 In the process, the dilute solution of the absorption-generator 16 enters the newly added generator A through the first solution heat exchanger 10 and the newly added solution heat exchanger B, and the refrigerant vapor generated by the first generator 1 is supplied to the newly generated one. The device A acts as a driving heat medium, and the refrigerant vapor flows through the newly added generator. 8. The solution heated into the solution is released and the refrigerant vapor is supplied to the first condenser 4, and the concentrated solution of the generator A is newly added through the new solution pump. D and the new solution heat exchanger B enter the first generator 1, flowing through the new generator A The refrigerant vapor is exothermic into a refrigerant liquid, and then throttled into the first condenser 4 by a new throttle valve C to form a single-effect-recovery double-effect third-type absorption heat pump.
图 28所示的单效 -回热式双效第三类吸收式热泵是这样实现的：  The single-effect-recovery double-effect third-class absorption heat pump shown in Figure 28 is implemented as follows:
①结构上， 在图 4所示的第三类吸收式热泵中， 取消吸收-发生器 16与外部连通的被加 热介质管路， 取消第三溶液泵， 吸收器 3有稀溶液管路经第三溶液热交换器 15与吸收 -发生 器 16连通； 增加新增发生器、 新增溶液节流阀和新增节流阀， 将第一发生器 1有浓溶液管路 经第一溶液泵 7、 第一溶液热交换器 10和吸收-发生器 16与分汽室 17连通调整为第一发生 器 1有浓溶液管路经新增溶液节流阀 J和吸收-发生器 16与分汽室 17连通， 将吸收-发生器 16有稀溶液管路经第一溶液热交换器 10与第一发生器 1连通调整为吸收-发生器 16有稀溶 液管路第一溶液热交换器 10与新增发生器 A连通，新增发生器 A还有浓溶液管路经第一溶液 泵 7和第一溶液热交换器 10与第一发生器 1连通，将第一发生器 1有冷剂蒸汽通道与第一冷 凝器 4连通调整为第一发生器 1有冷剂蒸汽通道与新增发生器 A连通后新增发生器 A再有冷 剂液管路经新增节流阀 C与第一冷凝器 4连通， 新增发生器 A还有冷剂蒸汽通道与第一冷凝 器 4连通； 取消蒸发器 6与吸收-发生器 16连通的冷剂蒸汽通道， 第一发生器 1增设冷剂蒸 汽通道与吸收-发生器 16连通。  1Structurally, in the third type of absorption heat pump shown in FIG. 4, the heated medium line in which the absorption-generator 16 communicates with the outside is canceled, the third solution pump is canceled, and the absorber 3 has a dilute solution line through the first The three-solution heat exchanger 15 is in communication with the absorption-generator 16; an additional generator, a new solution throttle valve, and a new throttle valve are added, and the first generator 1 has a concentrated solution line through the first solution pump 7 The first solution heat exchanger 10 and the absorption-generator 16 are connected to the steam distribution chamber 17 to be adjusted so that the first generator 1 has a concentrated solution line through the newly added solution throttle valve J and the absorption-generator 16 and the steam distribution chamber. 17 connected, the absorption-generator 16 has a dilute solution line connected to the first generator 1 through the first solution heat exchanger 10 to adjust to absorption - the generator 16 has a dilute solution line first solution heat exchanger 10 and new The generator A is connected, the new generator A and the concentrated solution pipeline are connected to the first generator 1 via the first solution pump 7 and the first solution heat exchanger 10, and the first generator 1 has a refrigerant vapor passage. Connected with the first condenser 4 to adjust the first generator 1 to have a refrigerant vapor pass After connecting with the newly added generator A, the generator A is newly added, and then the refrigerant liquid pipeline is connected with the first condenser 4 through the newly added throttle valve C, and the new generator A is also provided with the refrigerant vapor passage and the first condensation. The device 4 is connected; the refrigerant vapor passage of the evaporator 6 and the absorption-generator 16 is eliminated, and the first generator 1 is provided with a refrigerant vapor passage communicating with the absorption-generator 16.
②流程上， 吸收器 3的稀溶液经第三溶液热交换器 15降温降压后进入吸收-发生器 16、 吸收来自第一发生器 1的冷剂蒸汽并放热于流经吸收-发生器 16的溶液； 吸收器 3的稀溶液 经第一溶液热交换器 10进入新增发生器 A,第一发生器 1产生的冷剂蒸汽分别提供给新增发 生器 A和吸收-发生器 16， 冷剂蒸汽流经新增发生器 A、 加热进入其内的溶液释放并向第一 冷凝器 4提供冷剂蒸汽， 新增发生器 A的浓溶液经第一溶液泵 7和第一溶液热交换器 10进 入第一发生器 1， 第一发生器 1的浓溶液经新增节流阀 J节流之后再流经吸收-发生器 16、 吸 热部分汽化进入分汽室 17， 流经新增发生器 A的冷剂蒸汽放热成冷剂液、 再经新增节流阀 C 节流进入第一冷凝器 4， 形成单效 -回热式双效第三类吸收式热泵。  2 In the process, the dilute solution of the absorber 3 is cooled down by the third solution heat exchanger 15 to enter the absorption-generator 16, absorbs the refrigerant vapor from the first generator 1, and radiates heat through the absorption-generator The solution of 16; the dilute solution of the absorber 3 enters the new generator A through the first solution heat exchanger 10, and the refrigerant vapor generated by the first generator 1 is supplied to the new generator A and the absorption-generator 16, respectively. The refrigerant vapor flows through the newly added generator A, the solution heated into the solution is released, and the refrigerant vapor is supplied to the first condenser 4, and the concentrated solution of the newly added generator A is exchanged with the first solution pump 7 and the first solution. The device 10 enters the first generator 1, and the concentrated solution of the first generator 1 is throttled by the new throttle valve J, and then flows through the absorption-generator 16 and the heat absorption portion is vaporized into the steam distribution chamber 17, and flows through The refrigerant vapor of the generator A is radiated into a refrigerant liquid, and then throttled into the first condenser 4 through a new throttle valve C to form a single-effect-recovery double-effect third-class absorption heat pump.
图 29所示的单效 -回热式三效第三类吸收式热泵是这样实现的：  The single-effect-recovery three-effect third-class absorption heat pump shown in Figure 29 is implemented as follows:
①结构上， 在图 19所示的第三类吸收式热泵中， 增加新增第二发生器、 新增第二溶液热 交换器和新增第二节流阀，第二溶液泵 14增设稀溶液管路经新增第二溶液热交换器 F与新增 第二发生器 E连通， 新增第二发生器 E还有浓溶液管路经新增第二溶液热交换器 F与第三发 生器 12连通，将新增第一发生器 A有冷剂蒸汽通道与第一冷凝器 4连通调整为新增第一发生 器 A有冷剂蒸汽通道与新增第二发生器 E连通后新增第二发生器 E再有冷剂液管路经新增第 二节流阀 G与第一冷凝器 4连通，新增第二发生器 E还有冷剂蒸汽通道与第一冷凝器 4连通。  1Structurally, in the third type of absorption heat pump shown in FIG. 19, a new second generator is added, a second solution heat exchanger is added, and a second throttle valve is added, and the second solution pump 14 is added with a thinner The solution line is connected to the newly added second generator E by adding the second solution heat exchanger F, and the second generator E and the concentrated solution line are newly added to the second solution heat exchanger F and the third generation occurs. The device 12 is connected, and the newly added first generator A has a refrigerant vapor channel connected to the first condenser 4 to be adjusted to add a new first generator A. The refrigerant vapor channel is connected with the newly added second generator E. The second generator E further has a refrigerant liquid pipeline connected to the first condenser 4 via a new second throttle valve G, and a second generator E and a refrigerant vapor passage are connected to the first condenser 4.
②流程上， 第二吸收器 13的部分稀溶液经第二溶液泵 14和新增第二溶液热交换器 F进 入新增第二发生器 E， 新增第一发生器 A产生的冷剂蒸汽提供给新增第二发生器 E作驱动热 介质， 冷剂蒸汽流经新增第二发生器 E、 加热进入其内的溶液释放并向第一冷凝器 4提供冷 剂蒸汽， 新增第二发生器 E的浓溶液经新增第二溶液热交换器 F进入第三发生器 12， 流经新 增第二发生器 E的冷剂蒸汽放热成冷剂液、 再经新增第二节流阀 G节流进入第一冷凝器 4， 形成单效 -回热式三效第三类吸收式热泵。  2 In the process, a part of the dilute solution of the second absorber 13 enters the newly added second generator E via the second solution pump 14 and the newly added second solution heat exchanger F, and the refrigerant vapor generated by the first generator A is newly added. Providing a new second generator E for driving the heat medium, the refrigerant vapor flowing through the newly added second generator E, releasing the solution into which it is heated, and supplying the refrigerant vapor to the first condenser 4, adding a second The concentrated solution of the generator E is added to the third generator 12 by adding the second solution heat exchanger F, and the refrigerant vapor flowing through the newly added second generator E is radiated into the refrigerant liquid, and then the second section is added. The flow valve G is throttled into the first condenser 4 to form a single-effect-recovery three-effect third-type absorption heat pump.
图 30所示的单效 -回热式三效第三类吸收式热泵是这样实现的：  The single-effect-recovery three-effect third-class absorption heat pump shown in Figure 30 is implemented as follows:
①结构上， 在图 20所示的第三类吸收式热泵中， 增加新增第二发生器、 新增第二溶液热 交换器和新增第二节流阀，将第二溶液泵 14有稀溶液管路经新增第一溶液热交换器 B和第三 溶液热交换器 15与第一发生器 1连通调整为第二溶液泵 14有稀溶液管路经新增第二溶液热 交换器 F、 新增第一溶液热交换器 B和第三溶液热交换器 15与第一发生器 1连通， 将新增第 一发生器 A有浓溶液管路经新增第一溶液热交换器 B与第三发生器 12连通调整为新增第一发 生器 A有浓溶液管路经新增第一溶液热交换器 B与新增第二发生器 E连通， 新增第二发生器 E还有浓溶液管路经新增第二溶液热交换器 F与第三发生器 12连通， 将新增第一发生器 A有 冷剂蒸汽通道与第一冷凝器 4连通调整为新增第一发生器 A有冷剂蒸汽通道与新增第二发生 器 E连通后新增第二发生器 E再有冷剂液管路经新增第二节流阀 G与第一冷凝器 4连通， 新 增第二发生器 E还有冷剂蒸汽通道与第一冷凝器 4连通；取消第三发生器 12与外部连通的余 热介质管路， 增加新增第三节流阀， 新增第一发生器 A增设冷剂蒸汽通道与第三发生器 12连 通后第三发生器 12再有冷剂液管路经新增第三节流阀与第一冷凝器 4连通。 1Structurally, in the third type of absorption heat pump shown in FIG. 20, a new second generator is added, a second solution heat exchanger is added, and a second throttle valve is added, and the second solution pump 14 is provided. The dilute solution pipeline is connected to the first generator 1 via the newly added first solution heat exchanger B and the third solution heat exchanger 15 to be adjusted to be the second solution pump 14 having a dilute solution pipeline by adding a second solution heat The exchanger F, the newly added first solution heat exchanger B and the third solution heat exchanger 15 are in communication with the first generator 1, and the newly added first generator A has a concentrated solution pipeline through the newly added first solution heat exchange The B is connected to the third generator 12 to be adjusted to add a first generator A. The concentrated solution pipeline is connected to the newly added second generator E by adding the first solution heat exchanger B, and the second generator E is newly added. Further, the concentrated solution pipeline is connected to the third generator 12 via the newly added second solution heat exchanger F, and the newly added first generator A has a refrigerant vapor passage connected to the first condenser 4 to be newly added first. The generator A has a refrigerant vapor passage connected with the newly added second generator E, and then a second generator E is added, and then the refrigerant liquid pipeline is connected to the first condenser 4 via the addition of the second throttle valve G, The second generator E is further connected with the refrigerant vapor passage to communicate with the first condenser 4; the waste heat medium pipeline connecting the third generator 12 with the outside is cancelled, the third throttle valve is added, and the first generator is added. A additional refrigerant vapor passage is connected with the third generator 12, and then the third generator 12 has a refrigerant liquid pipeline via a new third throttle valve and the first The condenser 4 is connected.
②流程上， 新增第一发生器 A产生的冷剂蒸汽分别提供给新增第二发生器 E和第三发生 器 12作驱动热介质， 新增第一发生器 A的浓溶液经新增第一溶液热交换器 B进入新增第二 发生器 E， 冷剂蒸汽流经新增第二发生器 E、 加热进入其内的溶液释放并向第一冷凝器 4提 供冷剂蒸汽， 流经新增第二发生器 E的冷剂蒸汽放热成冷剂液、 再经新增第二节流阀 G进入 第一冷凝器 4; 新增第二发生器 E的浓溶液经新增第二溶液热交换器 F进入第三发生器 12， 冷剂蒸汽流经第三发生器 12、 加热进入其内的溶液释放并向第二吸收器 13提供冷剂蒸汽流 经，流经第三发生器 12的冷剂蒸汽放热成冷剂液、再经新增第三节流阀 I进入第一冷凝器 4; 第二吸收器 13的稀溶液经第二溶液泵 14、新增第二溶液热交换器？、新增第一溶液热交换器 B和第三溶液热交换器 15进入第一发生器 1， 形成单效 -回热式三效第三类吸收式热泵。  2 In the process, the newly added refrigerant vapor generated by the first generator A is separately supplied to the newly added second generator E and the third generator 12 as the driving heat medium, and the concentrated solution of the first generator A is newly added. The first solution heat exchanger B enters a new second generator E, and the refrigerant vapor flows through the newly added second generator E, and the solution heated therein is released and supplies the refrigerant vapor to the first condenser 4, flowing through The refrigerant vapor of the second generator E is newly added into a refrigerant liquid, and then the second throttle valve G is added to enter the first condenser 4; the concentrated solution of the second generator E is newly added by the second The solution heat exchanger F enters the third generator 12, and the refrigerant vapor flows through the third generator 12, and the solution heated therein is released and supplies the refrigerant vapor to the second absorber 13 to flow through the third generator. The refrigerant vapor of 12 is exothermed into a refrigerant liquid, and then added to the first condenser 4 by adding a third throttle valve I; the dilute solution of the second absorber 13 is passed through the second solution pump 14, and the second solution heat is added. Switch? The first solution heat exchanger B and the third solution heat exchanger 15 are added to the first generator 1, and a single-effect-recovery three-effect type III absorption heat pump is formed.
图 31所示的单效 -回热式三效第三类吸收式热泵是这样实现的- The single-effect - regenerative three-effect third-class absorption heat pump shown in Figure 31 is implemented in this way -
①结构上， 在图 22所示的第三类吸收式热泵中， 增加新增第二发生器、 新增第二溶液热 交换器、新增第二节流阀和新增第二溶液泵， 将第二溶液泵 14有稀溶液管路经第三溶液热交 换器 15与新增第一发生器 A连通调整为第二溶液泵 14有稀溶液管路经第三溶液热交换器 15 与新增第二发生器 E连通， 新增第二发生器 E还有浓溶液管路经新增第二溶液泵 H和新增第 二溶液热交换器 F与新增第一发生器 A连通， 将第一发生器 1有浓溶液管路经新增第一溶液 热交换器 B和第三溶液热交换器 15与第三发生器 12连通调整为第二发生器 2有浓溶液管路 经新增第一溶液热交换器 B、 新增第二溶液热交换器 F和第三溶液热交换器 15与第三发生器 12连通， 将新增第一发生器 A有冷剂蒸汽通道与第一冷凝器 4连通调整为新增第一发生器 A 有冷剂蒸汽通道与新增第二发生器 E连通后新增第二发生器 E再有冷剂液管路经新增第二节 流阔 G与第一冷凝器 4连通， 新增第二发生器 E还有冷剂蒸汽通道与第一冷凝器 4连通； 取 消第三发生器 12与外部连通的余热介质管路， 增加新增第三节流阔，第一发生器 1增设冷剂 蒸汽通道与第三发生器 12连通后第三发生器 12再有冷剂液管路经新增第三节流阀 I与第一 冷凝器 4连通。 1Structurally, in the third type of absorption heat pump shown in FIG. 22, adding a second generator, adding a second solution heat exchanger, adding a second throttle valve, and adding a second solution pump, The second solution pump 14 has a dilute solution line connected to the newly added first generator A via the third solution heat exchanger 15 to adjust the second solution pump 14 to have a dilute solution line through the third solution heat exchanger 15 and the new The second generator E is connected, the second generator E and the concentrated solution pipeline are connected to the newly added first generator A by adding the second solution pump H and the newly added second solution heat exchanger F, The first generator 1 has a concentrated solution pipeline connected to the third generator 12 via the newly added first solution heat exchanger B and the third solution heat exchanger 15 to be adjusted to be the second generator 2 The first solution heat exchanger B, the newly added second solution heat exchanger F and the third solution heat exchanger 15 are in communication with the third generator 12, and the first generator A is added with the refrigerant vapor passage and the first condensation. 4 is connected to adjust the new first generator A with a refrigerant vapor channel and a new second generator E After the addition of the second generator E, the refrigerant liquid pipeline is connected to the first condenser 4 via the addition of the second section flow G, and the second generator E is further provided with the refrigerant vapor passage and the first condenser. 4 communicating; canceling the residual heat medium pipeline of the third generator 12 and the outside, adding a new third section of the flow, the first generator 1 is connected with the third generator 12 after the refrigerant vapor passage is connected with the third generator 12 Further, the refrigerant liquid line is connected to the first condenser 4 via the addition of the third throttle valve I.
②流程上，第二吸收器 13的稀溶液经第二溶液泵 14和第三溶液热交换器 15进入新增第 二发生器 E， 新增第一发生器 A产生的冷剂蒸汽提供给新增第二发生器 E作驱动热介质， 冷 剂蒸汽流经新增第二发生器 E、 加热进入其内的溶液释放并向第一冷凝器 4提供冷剂蒸汽， 流经新增第二发生器 E的冷剂蒸汽放热成冷剂液、再经新增第二节流阀 G进入第一冷凝器 4， 新增第二发生器 E的浓溶液经新增第二溶液泵 H和新增第二溶液热交换器 E进入新增第一发 生器 A; 第一发生器 1的浓溶液经新增第一溶液热交换器 B、 新增第二溶液热交换器 F和第 三溶液热交换器 15进入第三发生器 12， 第一发生器 1产生的冷剂蒸汽分别提供给新增第一 发生器 A和第三发生器 12作驱动热介质， 冷剂蒸汽流经第三发生器 12、 加热进入其内的溶 液释放并向第二吸收器 13提供冷剂蒸汽流经，流经第三发生器 12的冷剂蒸汽放热成冷剂液、 再经新增第三节流阀 I进入第一冷凝器 4， 形成单效 -回热式三效第三类吸收式热泵。 2 In the process, the dilute solution of the second absorber 13 enters the newly added second generator E through the second solution pump 14 and the third solution heat exchanger 15 to add the refrigerant vapor generated by the first generator A to the new The second generator E is added to drive the heat medium, and the refrigerant vapor flows through the newly added second generator E, and the solution heated into the liquid is released and supplies the refrigerant vapor to the first condenser 4, and flows through the second generation. The refrigerant vapor of the device E is radiated into a refrigerant liquid, and then the second throttle valve G is added to the first condenser 4, and the concentrated solution of the second generator E is newly added by adding the second solution pump H and the new The second solution heat exchanger E is added to the newly added first generator A; the concentrated solution of the first generator 1 is added with the first solution heat exchanger B, the second solution heat exchanger F and the third solution heat are added. The exchanger 15 enters the third generator 12, and the refrigerant vapor generated by the first generator 1 is supplied to the newly added first generator A and the third generator 12 as driving heat medium, and the refrigerant vapor flows through the third generator. 12, heating into the solution The liquid releases and supplies the refrigerant vapor to the second absorber 13 to flow through, and the refrigerant vapor flowing through the third generator 12 releases the refrigerant liquid into the first condenser 4 through the addition of the third throttle valve I. , forming a single-effect-recovery three-effect third-class absorption heat pump.
图 32所示的单效 -回热式三效第三类吸收式热泵是这样实现的：  The single-effect-recovery three-effect third-class absorption heat pump shown in Figure 32 is implemented as follows:
①结构上， 在图 23所示的第三类吸收式热泵中， 增加新增第二发生器、新增第二溶液热 交换器和新增第二节流阀， 将新增第一发生器 A有浓溶液管路经第一溶液泵 7和新增第一溶 液热交换器 B之后与第一发生器 1经第一溶液热交换器 10之后的浓溶液管路汇合调整为新增 第一发生器 A有浓溶液管路经新增第一溶液热交换器 B之后与第一发生器 1经第一溶液热交 换器 10之后的浓溶液管路汇合， 吸收-发生器 16增设稀溶液管路经新增第二溶液热交换器 F 与新增第二发生器 E连通， 新增第二发生器 E还有浓溶液管路经第一溶液泵 7和新增第二溶 液热交换器 F之后与第一发生器 1经第一溶液热交换器 10之后的浓溶液管路汇合，将新增第 一发生器 A有冷剂蒸汽通道与第一冷凝器 4连通调整为新增第一发生器 A有冷剂蒸汽通道与 新增第二发生器 E连通后新增第二发生器 E再有冷剂液管路经新增第二节流阀 G与第一冷凝 器 4连通， 新增第二发生器 E还有冷剂蒸汽通道与第一冷凝器 4连通。  1Structurally, in the third type of absorption heat pump shown in Fig. 23, the addition of the second generator, the addition of the second solution heat exchanger and the addition of the second throttle valve will be added, and the first generator will be added. The concentrated solution line of A is merged with the concentrated solution line after the first solution heat exchanger 10 is passed through the first solution pump 7 and the first solution heat exchanger B, and is added to the first step. The generator A has a concentrated solution line which is merged with the concentrated solution line after the first solution 1 passes through the first solution heat exchanger 10 after adding the first solution heat exchanger B, and the absorption-generator 16 adds a dilute solution tube. The second solution heat exchanger F is newly connected with the newly added second generator E, and the second generator E and the concentrated solution pipeline are added through the first solution pump 7 and the second solution heat exchanger F. Thereafter, the first generator 1 is merged with the concentrated solution pipeline after the first solution heat exchanger 10, and the newly added first generator A has a refrigerant vapor passage connected to the first condenser 4 to be adjusted to be newly added. A has a refrigerant vapor channel connected to the new second generator E to add a second occurrence E and then the refrigerant liquid pipe of the second throttle valve G communicates with the new first condenser 4, as well as new second generator E passage communicating with the first refrigerant vapor condenser 4.
②流程上， 吸收-发生器 16的部分稀溶液经新增第二溶液热交换器 F进入新增第二发生 器 E， 新增第一发生器 A产生的冷剂蒸汽提供给新增第二发生器 E作驱动热介质， 冷剂蒸汽 流经新增第二发生器 E、 加热进入其内的溶液释放并向第一冷凝器 4提供冷剂蒸汽， 新增第 二发生器 E的浓溶液经第一溶液泵 7和新增第二溶液热交换器 F之后再流经吸收-发生器 16、 吸热部分汽化进入分汽室 17， 流经新增第二发生器 E的冷剂蒸汽放热成冷剂液、 再经新增第 二节流阀 G进入第一冷凝器 4;新增第一发生器 A的浓溶液经新增第一溶液热交换器 B后再 流经吸收-发生器 16、吸热部分汽化进入分汽室 17，形成单效 -回热式三效第三类吸收式热泵。  2 In the process, a part of the dilute solution of the absorption-generator 16 is added to the second solution heat exchanger F to enter the newly added second generator E, and the refrigerant vapor generated by the first generator A is newly added to the second The generator E serves as a driving heat medium, and the refrigerant vapor flows through the newly added second generator E, the solution heated into the solution is released, and the refrigerant vapor is supplied to the first condenser 4, and the concentrated solution of the second generator E is newly added. After passing through the first solution pump 7 and adding the second solution heat exchanger F, it flows through the absorption-generator 16 and the heat absorption portion is vaporized into the steam separation chamber 17, and flows through the refrigerant vapor of the newly added second generator E. The hot refrigerant liquid is added to the first condenser 4 by adding a second throttle valve G; the concentrated solution of the first generator A is added after the first solution heat exchanger B is added, and then flows through the absorption-occurrence The heat absorbing portion is vaporized into the steam dividing chamber 17 to form a single-effect-recovery three-effect third-class absorption heat pump.
图 33所示的单效 -回热式三效第三类吸收式热泵是这样实现的：  The single-effect-recovery three-effect third-class absorption heat pump shown in Figure 33 is implemented as follows:
①结构上， 在图 24所示的第三类吸收式热泵中， 增加新增第二发生器、新增溶液热交换 器和新增第二节流阀， 将新增第一发生器 A有浓溶液管路经第一溶液泵 7和第一溶液热交换 器 10与第一发生器 1经新增溶液节流阀 J之后的浓溶液管路汇合调整为新增第一发生器 A有 浓溶液管路经第一溶液热交换器 10之后与第一发生器 1经新增溶液节流阔 J之后的浓溶液管 路汇合， 吸收-发生器 16增设稀溶液管路经新增溶液热交换器 B与新增第二发生器 E连通， 新增第二发生器 E还有浓溶液管路经第一溶液泵 7和新增溶液热交换器 B之后与第一发生器 1经新增溶液节流阀 J之后的浓溶液管路汇合， 将新增第一发生器 A有冷剂蒸汽通道与第一 冷凝器 4连通调整为新增第一发生器 A有冷剂蒸汽通道与新增第二发生器 E连通后新增第二 发生器 E再有冷剂液管路经新增第二节流阀 G与第一冷凝器 4连通， 新增第二发生器 E还有 冷剂蒸汽通道与第一冷凝器 4连通。  1Structurally, in the third type of absorption heat pump shown in Fig. 24, the addition of the second generator, the new solution heat exchanger and the addition of the second throttle valve will be added, and the first generator A will be added. The concentrated solution pipeline is adjusted by the first solution pump 7 and the first solution heat exchanger 10 and the concentrated solution pipeline after the first generator 1 is added by the new solution throttle valve J to be newly added. After the solution line passes through the first solution heat exchanger 10, it merges with the concentrated solution line after the first generator 1 is throttled by the new solution, and the absorption-generator 16 adds a dilute solution line through the new solution heat exchange. The B is connected to the newly added second generator E, and the second generator E and the concentrated solution pipeline are added to the first generator 1 through the first solution pump 7 and the new solution heat exchanger B. The concentrated solution pipeline after the throttle valve J merges, and the newly added first generator A has a refrigerant vapor passage and communicates with the first condenser 4 to adjust the newly added first generator A to have a refrigerant vapor passage and a new addition After the second generator E is connected, the second generator E is added, and then the refrigerant liquid pipeline is added with the second throttle. G in communication with the first condenser 4, as well as new second generator E passage communicating with the first refrigerant vapor condenser 4.
②流程上， 新增第一发生器 A产生的冷剂蒸汽提供给新增第二发生器 E作驱动热介质， 新增第一发生器 A的浓溶液经第一溶液热交换器 10之后再流经吸收-发生器 16、吸热部分汽 化后进入分汽室 17; 吸收-发生器 16的部分稀溶液经新增第二溶液热交换器 F进入新增第二 发生器 E， 冷剂蒸汽流经新增第二发生器 E、 加热进入其内的溶液释放并向第一冷凝器 4提 供冷剂蒸汽， 新增第二发生器 E的浓溶液经第一溶液泵 7和新增溶液热交换器 B之后再流经 吸收-发生器 16、 吸热部分汽化进入分汽室 17， 流经新增第二发生器 E的冷剂蒸汽放热成冷 剂液、 再经新增第二节流阀 G进入第一冷凝器 4， 形成单效 -回热式三效第三类吸收式热泵。  2 In the process, the refrigerant coolant generated by the first generator A is newly supplied to the second generator E to drive the heat medium, and the concentrated solution of the first generator A is added after passing through the first solution heat exchanger 10. Flowing through the absorption-generator 16 and vaporizing the heat-absorbing portion into the steam dividing chamber 17; part of the dilute solution of the absorption-generator 16 is added to the second solution heat exchanger F to enter the newly added second generator E, the refrigerant vapor Flowing through the addition of the second generator E, heating the solution into which it is released and supplying the refrigerant vapor to the first condenser 4, adding the concentrated solution of the second generator E to the first solution pump 7 and adding the solution heat After the exchanger B flows through the absorption-generator 16, the heat absorption portion is vaporized into the steam separation chamber 17, and the refrigerant vapor flowing through the newly added second generator E is radiated into a refrigerant liquid, and then the second section is added. The flow valve G enters the first condenser 4 to form a single-effect-recovery three-effect third-type absorption heat pump.
图 34所示的单效 -回热式三效第三类吸收式热泵是这样实现的：  The single-effect-recovery three-effect third-class absorption heat pump shown in Figure 34 is implemented as follows:
①结构上， 在图 33所示的第三类吸收式热泵中， 将吸收-发生器 16有稀溶液管路直接与 第一发生器 1连通调整为吸收-发生器 16有稀溶液管路经第一溶液热交换器 10与第一发生器 1连通， 将第一发生器 1有浓溶液管路经新增溶液节流阀 J和吸收-发生器 16与分汽室 17连 通调整为第一发生器 1有浓溶液管路经第一溶液热交换器 10和吸收-发生器 16与分汽室 17 连通，将吸收-发生器 16有稀溶液管路经第一溶液热交换器 10与新增第一发生器 A连通调整 为吸收-发生器 16有稀溶液管路直接与新增第一发生器 A连通， 将新增第一发生器 A有浓溶 液管路经第一溶液热交换器 10和吸收-发生器 16与分汽室 17连通调整为新增第一发生器 A 有浓溶液管路经新增溶液节流阀 J和吸收-发生器 16与分汽室 17连通，将第一发生器 1有冷 剂蒸汽通道与吸收-发生器 16连通调整为新增第一发生器 A有冷剂蒸汽通道与吸收-发生器 16连通。 1 Structurally, in the third type of absorption heat pump shown in Fig. 33, the absorption-generator 16 has a dilute solution line directly The first generator 1 is connected and adjusted to be an absorption-generator 16 having a dilute solution line connected to the first generator 1 via the first solution heat exchanger 10, and the first generator 1 has a concentrated solution line through the newly added solution section. The flow valve J and the absorption-generator 16 are connected to the steam distribution chamber 17 to be adjusted so that the first generator 1 has a concentrated solution line connected to the steam distribution chamber 17 via the first solution heat exchanger 10 and the absorption-generator 16 to absorb - the generator 16 has a dilute solution line connected to the newly added first generator A via the first solution heat exchanger 10 to be adjusted to absorb - the generator 16 has a dilute solution line directly connected to the newly added first generator A, The first first generator A has a concentrated solution pipeline connected to the steam distribution chamber 17 through the first solution heat exchanger 10 and the absorption-generator 16 to be newly added to the first generator A. The concentrated solution pipeline has a new solution. The throttle valve J and the absorption-generator 16 are in communication with the steam dividing chamber 17, and the first generator 1 has a refrigerant vapor passage communicating with the absorption-generator 16 to adjust the newly added first generator A to have a refrigerant vapor passage and The absorption-generator 16 is in communication.
②流程上， 吸收-发生器 16的稀溶液分成三路——第一路经第一溶液热交换器 10进入第 一发生器 1， 第二路直接进入新增第一发生器 A， 第三路经新增溶液热交换器 B进入新增第 二发生器 E;新增第一发生器 A产生的冷剂蒸汽分别提供给新增第二发生器 E和吸收-发生器 16, 冷剂蒸汽流经新增第二发生器 E、 加热进入其内的溶液释放并向第一冷凝器 4提供冷剂 蒸汽， 流经新增第二发生器 E的冷剂蒸汽放热成冷剂液、 再经新增第二节流阀 G进入第一冷 凝器 4; 第一发生器 1的浓溶液经第一溶液热交换器 10之后再流经吸收-发生器 16、 吸热部 分汽化后进入分汽室 17， 新增第一发生器 A的浓溶液经新增溶液节流阀 J之后再流经吸收- 发生器 16、 吸热部分汽化后进入分汽室 17， 形成单效 -回热式三效第三类吸收式热泵。  2 In the process, the dilute solution of the absorption-generator 16 is divided into three paths - the first path enters the first generator 1 via the first solution heat exchanger 10, and the second path directly enters the newly added first generator A, the third The newly added solution heat exchanger B enters the newly added second generator E; the newly added refrigerant vapor generated by the first generator A is separately supplied to the newly added second generator E and the absorption-generator 16, the refrigerant vapor Flowing through the newly added second generator E, releasing the solution into which it is heated and supplying the refrigerant vapor to the first condenser 4, and flowing the refrigerant vapor flowing through the second generator E to release the refrigerant liquid, and then The second throttle valve G is added to enter the first condenser 4; the concentrated solution of the first generator 1 passes through the first solution heat exchanger 10 and then flows through the absorption-generator 16 to vaporize the heat absorption portion and enter the steam separation portion. Room 17, the new concentrated solution of the first generator A is added to the absorption-generator 16 after the addition of the solution throttle valve J, and the heat absorption portion is vaporized and then enters the steam separation chamber 17, forming a single-effect-recovery type III The third type of absorption heat pump.
图 35所示的单效 -回热式三效第三类吸收式热泵是这样实现的：  The single-effect-recovery three-effect third-class absorption heat pump shown in Figure 35 is implemented as follows:
①结构上， 在图 25所示的第三类吸收式热泵中， 增加新增第二发生器、 新增第二溶液热 交换器和新增第二节流阀， 将新增第一发生器 A有浓溶液管路经第一溶液泵 7和新增第一溶 液热交换器 B与第一溶液热交换器 10连通调整为新增第一发生器 A有浓溶液管路经新增第二 溶液热交换器 F与新增第二发生器 E连通， 新增第二发生器 E还有浓溶液管路经第一溶液泵 7、 新增第二溶液热交换器 F和新增第一溶液热交换器 B与第一溶液热交换器 10连通， 将新 增第一发生器 A有冷剂蒸汽通道与第一冷凝器 4连通调整为新增第一发生器 A有冷剂蒸汽通 道与新增第二发生器 E连通后新增第二发生器 E再有冷剂液管路经新增第二节流阀 G与第一 冷凝器 4连通， 新增第二发生器 E还有冷剂蒸汽通道与第一冷凝器 4连通。  1Structurally, in the third type of absorption heat pump shown in Fig. 25, the addition of the second generator, the addition of the second solution heat exchanger and the addition of the second throttle valve will add a first generator. A concentrated solution pipeline is connected to the first solution heat exchanger 10 via the first solution pump 7 and the newly added first solution heat exchanger B to be newly added, the first generator A has a concentrated solution pipeline, and the second is added. The solution heat exchanger F is connected to the newly added second generator E, and the second generator E and the concentrated solution line are added through the first solution pump 7, the second solution heat exchanger F is added, and the first solution is added. The heat exchanger B is in communication with the first solution heat exchanger 10, and the newly added first generator A has a refrigerant vapor passage communicating with the first condenser 4 to adjust the new first generator A to have a refrigerant vapor passage and a new one. After the second generator E is connected, the second generator E is newly added, and then the refrigerant liquid pipeline is connected with the first condenser 4 through the addition of the second throttle valve G, and the second generator E is added with the refrigerant. The steam passage is in communication with the first condenser 4.
②流程上， 新增第一发生器 A的浓溶液经新增第二溶液热交换器 F进入新增第二发生器 E, 新增第一发生器 A产生的冷剂蒸汽提供给新增第二发生器 E作驱动热介质， 冷剂蒸汽流 经新增第二发生器 E、 加热进入其内的溶液释放并向第一冷凝器 4提供冷剂蒸汽， 新增第二 发生器 E的浓溶液经第一溶液泵 7、 新增第二溶液热交换器？、 新增第一溶液热交换器 B和 第一溶液热交换器 10之后再流经吸收-发生器 16、 吸热部分汽化后进入分汽室 17， 流经新增 第二发生器 E的冷剂蒸汽放热成冷剂液、 再经新增第二节流阀 G进入第一冷凝器 4, 形成单 效 -回热式三效第三类吸收式热泵。  2 In the process, the concentrated solution of the first generator A is newly added to the second solution E by adding the second solution heat exchanger F, and the refrigerant vapor generated by the first generator A is newly added to the new one. The second generator E serves as a driving heat medium, and the refrigerant vapor flows through the newly added second generator E, the solution heated into the solution is released, and the refrigerant vapor is supplied to the first condenser 4, and the second generator E is added. The solution is passed through the first solution pump 7, and the second solution heat exchanger is added. Adding the first solution heat exchanger B and the first solution heat exchanger 10, then flowing through the absorption-generator 16, vaporizing the heat absorption portion, and entering the steam separation chamber 17, flowing through the cold of the second generator E. The agent steam exotherms into a refrigerant liquid, and then enters the first condenser 4 by adding a second throttle valve G to form a single-effect-recovery three-effect third-type absorption heat pump.
图 36所示的单效 -回热式三效第三类吸收式热泵是这样实现的：  The single-effect-recovery three-effect third-class absorption heat pump shown in Figure 36 is implemented as follows:
①结构上， 在图 26所示的第三类吸收式热泵中， 增加新增第二发生器、 新增溶液热交换 器和新增第二节流阀， 将新增第一发生器 A有浓溶液管路经第一溶液泵 7与第一溶液热交换 器 10连通调整为新增第一发生器 A有浓溶液管路经新增溶液热交换器 B与新增第二发生器 E 连通， 新增第二发生器 E还有浓溶液管路经第一溶液泵 7和新增溶液热交换器 B与第一溶液 热交换器 10连通，将新增第一发生器 A有冷剂蒸汽通道与第一冷凝器 4连通调整为新增第一 发生器 A有冷剂蒸汽通道与新增第二发生器 E连通后新增第二发生器 E再有冷剂液管路经新 增第二节流阀 G与第一冷凝器 4连通， 新增第二发生器 E还有冷剂蒸汽通道与第一冷凝器 4 连通。 1Structurally, in the third type of absorption heat pump shown in Fig. 26, the addition of the second generator, the new solution heat exchanger and the addition of the second throttle valve will be added, and the first generator A will be added. The concentrated solution pipeline is connected to the first solution heat exchanger 10 via the first solution pump 7 to be newly added to the first generator A. The concentrated solution pipeline is connected to the newly added second generator E via the new solution heat exchanger B. The second generator E and the concentrated solution pipeline are connected to the first solution heat exchanger 10 via the first solution pump 7 and the new solution heat exchanger B, and the first generator A is added with refrigerant vapor. The passage is connected with the first condenser 4 to adjust to add a new first generator A. The refrigerant vapor passage is connected with the newly added second generator E, and then the second generator E is added and the refrigerant liquid pipeline is newly added. The second throttle valve G is connected to the first condenser 4, and the second generator E and the refrigerant vapor passage are connected to the first condenser 4.
②流程上， 新增第一发生器 A的浓溶液经新增溶液热交换器 B进入新增第二发生器 E， 新增第一发生器 A产生的冷剂蒸汽提供给新增第二发生器 E作驱动热介质， 冷剂蒸汽流经新 增第二发生器 E、 加热进入其内的溶液释放并向第一冷凝器 4提供冷剂蒸汽， 新增第二发生 器 E的浓溶液经第一溶液泵 7、新增溶液热交换器 B和第一溶液热交换器 10之后再流经吸收 -发生器 16、 吸热部分汽化后进入分汽室 17， 流经新增第二发生器 E的冷剂蒸汽放热成冷剂 液、 再经新增第二节流阀 G进入第一冷凝器 4， 形成单效 -回热式三效第三类吸收式热泵。  2 In the process, the concentrated solution of the first generator A is newly added to the newly added second heat exchanger B through the new solution heat exchanger B, and the new refrigerant generated by the first generator A is newly supplied to the second generation. The device E serves as a driving heat medium, and the refrigerant vapor flows through the newly added second generator E, the solution heated into the solution is released, and the refrigerant vapor is supplied to the first condenser 4, and the concentrated solution of the second generator E is newly added. The first solution pump 7, the new solution heat exchanger B and the first solution heat exchanger 10 are then passed through the absorption-generator 16, and the heat absorption portion is vaporized and then enters the steam separation chamber 17, and flows through the new second generator. The refrigerant vapor of E is exothermic into a refrigerant liquid, and then added to the second throttle valve G to enter the first condenser 4 to form a single-effect-recovery three-effect third-type absorption heat pump.
图 37所示的单效 -回热式三效第三类吸收式热泵是这样实现的：  The single-effect-recovery three-effect third-class absorption heat pump shown in Figure 37 is implemented as follows:
①结构上， 在图 36所示的第三类吸收式热泵中， 增加新增溶液泵， 将吸收-发生器 16有 稀溶液管路直接与第一发生器 1连通调整为吸收-发生器 16有稀溶液管路经新增溶液泵 D和 第一溶液热交换器 10与第一发生器 1连通，将新增第二发生器 E有浓溶液管路经第一溶液泵 7和新增溶液热交换器 B与第一溶液热交换器 10连通调整为新增第二发生器 E有浓溶液管路 经第一溶液泵 7和新增溶液热交换器 B与吸收-发生器 16连通， 将第一发生器 1有冷剂蒸汽 通道与吸收-发生器 16连通调整为新增第一发生器 A有冷剂蒸汽通道与吸收-发生器 16连通。  1Structurally, in the third type of absorption heat pump shown in FIG. 36, a new solution pump is added, and the absorption-generator 16 has a dilute solution line directly connected to the first generator 1 and adjusted to an absorption-generator 16 The dilute solution pipeline is connected to the first generator 1 via the new solution pump D and the first solution heat exchanger 10, and the second generator E has a concentrated solution pipeline through the first solution pump 7 and the newly added solution. The heat exchanger B is connected to the first solution heat exchanger 10 to be adjusted to add a second generator E. The concentrated solution line is connected to the absorption-generator 16 via the first solution pump 7 and the new solution heat exchanger B. The first generator 1 has a refrigerant vapor passage communicating with the absorption-generator 16 to adjust to add a first generator A having a refrigerant vapor passage in communication with the absorption-generator 16.
②流程上，吸收-发生器 16的稀溶液经新增溶液泵 D和第一溶液热交换器 10进入第一发 生器 1， 新增第一发生器 A产生的冷剂蒸汽分别提供给新增第二发生器 E和吸收-发生器 16， 新增第二发生器 E的浓溶液经第一溶液泵 7和新增溶液热交换器 B之后再流经吸收-发生器 16、 吸热部分汽化后进入分汽室 17， 形成单效 -回热式三效第三类吸收式热泵。  2 In the process, the dilute solution of the absorption-generator 16 enters the first generator 1 via the new solution pump D and the first solution heat exchanger 10, and the newly added refrigerant vapor generated by the first generator A is separately supplied to the new generator The second generator E and the absorption-generator 16 add a concentrated solution of the second generator E through the first solution pump 7 and the newly added solution heat exchanger B, and then flow through the absorption-generator 16 to vaporize the endothermic portion. After entering the steam dividing chamber 17, a single-effect-recovery three-effect third-class absorption heat pump is formed.
图 38所示的单效 -回热式三效第三类吸收式热泵是这样实现的- The single-effect-recovery three-effect third-class absorption heat pump shown in Figure 38 is realized in this way -
①结构上， 在图 27所示的第三类吸收式热泵中， 增加新增第二发生器、 新增第二溶液热 交换器、 新增第二节流阀和新增第二溶液泵， 将吸收-发生器 16有稀溶液管路经第一溶液热 交换器 10和新增第一溶液热交换器 B与新增第一发生器 A连通调整为吸收-发生器 16有稀溶 液管路经第一溶液热交换器 10、 新增第一溶液热交换器 B和新增第二溶液热交换器 F与新增 第二发生器 E连通， 新增第二发生器 E还有浓溶液管路经新增第二溶液泵 H和新增第二溶液 热交换器 F与新增第一发生器 A连通， 将新增第一发生器 A有冷剂蒸汽通道与第一冷凝器 4 连通调整为新增第一发生器 A有冷剂蒸汽通道与新增第二发生器 E连通后新增第二发生器 E 再有冷剂液管路经新增第二节流阀 G与第一冷凝器 4连通， 新增第二发生器 E还有冷剂蒸汽 通道与第一冷凝器 4连通。 1Structurally, in the third type of absorption heat pump shown in FIG. 27, adding a second generator, adding a second solution heat exchanger, adding a second throttle valve, and adding a second solution pump, Adjusting the absorption-generator 16 having a dilute solution line through the first solution heat exchanger 10 and the newly added first solution heat exchanger B to the newly added first generator A to adjust to the absorption-generator 16 having a dilute solution line The first solution heat exchanger 10, the newly added first solution heat exchanger B and the newly added second solution heat exchanger F are connected to the newly added second generator E, and the second generator E and the concentrated solution tube are newly added. The second new solution pump H and the newly added second solution heat exchanger F are connected to the newly added first generator A, and the newly added first generator A has a refrigerant vapor passage connected to the first condenser 4 to be adjusted. In order to add the first generator A, the refrigerant vapor channel is connected with the newly added second generator E, and then the second generator E is added, and then the refrigerant liquid pipeline is added with the second throttle valve G and the first condensation. The device 4 is connected, and a second generator E and a refrigerant vapor passage are connected to communicate with the first condenser 4.
②流程上， 吸收-发生器 16的浓溶液经第一溶液热交换器 10、 新增第一溶液热交换器 B 和新增第二溶液热交换器 F进入新增第二发生器 E， 新增第一发生器 A产生的冷剂蒸汽提供 给新增第二发生器 E作驱动热介质， 冷剂蒸汽流经新增第二发生器 E、 加热进入其内的溶液 释放并向第一冷凝器 4提供冷剂蒸汽， 流经新增第二发生器 E的冷剂蒸汽放热成冷剂液、 再 经新增第二节流阔 G进入第一冷凝器 4， 新增第二发生器 E的浓溶液经新增第二溶液泵 H和 新增第二溶液热交换器 F进入新增第一发生器 A， 形成单效 -回热式三效第三类吸收式热泵。  2 In the process, the concentrated solution of the absorption-generator 16 enters the newly added second generator E through the first solution heat exchanger 10, the newly added first solution heat exchanger B, and the newly added second solution heat exchanger F, Increasing the refrigerant vapor generated by the first generator A is supplied to the newly added second generator E as a driving heat medium, and the refrigerant vapor flows through the newly added second generator E, and the solution heated into the liquid is released and discharged to the first condensation The device 4 supplies the refrigerant vapor, and the refrigerant vapor flowing through the second generator E is dissipated into a refrigerant liquid, and then the second section G is added to the first condenser 4, and the second generator is added. The concentrated solution of E is added to the first first generator A by adding a second solution pump H and a new second solution heat exchanger F to form a single-effect-recovery three-effect third-type absorption heat pump.
图 39所示的单效 -回热式三效第三类吸收式热泵是这样实现的- The single-effect-recovery three-effect third-class absorption heat pump shown in Figure 39 is realized in this way -
①结构上， 在图 28所示的第三类吸收式热泵中， 增加新增第二发生器、 新增溶液热交换 器、新增第二节流阔和新增溶液泵， 将吸收-发生器 16有稀溶液管路第一溶液热交换器 10与 新增第一发生器 A连通调整为吸收-发生器 16有稀溶液管路经第一溶液热交换器 10和新增溶 液热交换器 B与新增第二发生器 E连通， 新增第二发生器 E还有浓溶液管路经新增溶液泵 D 和新增溶液热交换器 B与新增第一发生器 A连通， 将新增第一发生器 A有冷剂蒸汽通道与第 一冷凝器 4连通调整为新增第一发生器 A有冷剂蒸汽通道与新增第二发生器 E连通后新增第 二发生器 E再有冷剂液管路经新增第二节流阀 G与第一冷凝器 4连通， 新增第二发生器 E还 有冷剂蒸汽通道与第一冷凝器 4连通。 1Structurally, in the third type of absorption heat pump shown in Fig. 28, the addition of the second generator, the new solution heat exchanger, the addition of the second section of the flow and the new solution pump will be absorbed-occurring. The first solution heat exchanger 10 has a dilute solution line and is connected to the newly added first generator A to adjust the absorption-generator 16 with a dilute solution line through the first solution heat exchanger 10 and the new solution heat exchanger. B is connected with the newly added second generator E, and the second generator E and the concentrated solution pipeline are added through the new solution pump D. And the newly added solution heat exchanger B is connected with the newly added first generator A, and the newly added first generator A has a refrigerant vapor passage and communicates with the first condenser 4 to adjust the newly added first generator A to have a refrigerant. After the steam passage is connected with the newly added second generator E, the second generator E is newly added, and the refrigerant liquid pipeline is connected with the first condenser 4 through the addition of the second throttle valve G, and the second generator E is newly added. There is also a refrigerant vapor passage that communicates with the first condenser 4.
②流程上，吸收-发生器 16的浓溶液经第一溶液热交换器 10和新增溶液热交换器 B进入 新增第二发生器 E， 新增第一发生器 A产生的冷剂蒸汽提供给新增第二发生器 E作驱动热介 质， 冷剂蒸汽流经新增第二发生器 E、 加热进入其内的溶液释放并向第一冷凝器 4提供冷剂 蒸汽， 流经新增第二发生器 E的冷剂蒸汽放热成冷剂液、 再经新增第二节流阀 G进入第一冷 凝器 4， 新增第二发生器 E的浓溶液经新增溶液泵 D和新增溶液热交换器 B进入新增第一发 生器 A， 形成单效 -回热式三效第三类吸收式热泵。  2 In the process, the concentrated solution of the absorption-generator 16 enters the newly added second generator E through the first solution heat exchanger 10 and the newly added solution heat exchanger B, and the refrigerant vapor generated by the first generator A is newly supplied. The second generator E is added to drive the heat medium, and the refrigerant vapor flows through the newly added second generator E, and the solution heated into the solution is released and supplies the refrigerant vapor to the first condenser 4, and flows through the new section. The refrigerant vapor of the second generator E is radiated into a refrigerant liquid, and then the second throttle valve G is added to enter the first condenser 4, and the concentrated solution of the second generator E is newly added by the new solution pump D and new The solubilizing solution heat exchanger B enters the newly added first generator A to form a single-effect-recovery three-effect third-class absorption heat pump.
图 40所示的单效 -回热式三效第三类吸收式热泵是这样实现的：  The single-effect-recovery three-effect third-class absorption heat pump shown in Figure 40 is implemented as follows:
①结构上， 在图 39所示的第三类吸收式热泵中， 取消新增溶液节流阀， 将第一发生器 1 有浓溶液管路经新增溶液节流阀 J和吸收-发生器 16与分汽室 17连通调整为第一发生器 1有 浓溶液管路经第一溶液热交换器 10和吸收-发生器 16与分汽室 17连通， 将吸收-发生器 16 有稀溶液管路经第一溶液热交换器 10和新增溶液热交换器 B与新增第二发生器 E连通调整为 吸收-发生器 16有稀溶液管路经新增溶液热交换器 B与新增第二发生器 E连通， 将第一发生 器 1有冷剂蒸汽通道与吸收-发生器 16连通调整为新增第一发生器 A增设冷剂蒸汽通道与吸 收-发生器 16连通。  1Structurally, in the third type of absorption heat pump shown in FIG. 39, the new solution throttle valve is cancelled, and the first generator 1 has a concentrated solution line through the newly added solution throttle valve J and the absorption-generator 16 is connected to the steam dividing chamber 17 to be adjusted so that the first generator 1 has a concentrated solution line connected to the steam dividing chamber 17 via the first solution heat exchanger 10 and the absorption-generator 16 , and the absorption-generator 16 has a dilute solution tube The first solution heat exchanger 10 and the new solution heat exchanger B are connected to the newly added second generator E to be adjusted to absorb-the generator 16 has a dilute solution line through the new solution heat exchanger B and the new addition The two generators E are connected, and the first generator 1 has a refrigerant vapor passage connected to the absorption-generator 16 to be adjusted to add a first generator A. The additional refrigerant vapor passage is in communication with the absorption-generator 16.
②流程上， 吸收-发生器 16的稀溶液经新增溶液热交换器 B进入新增第二发生器 E， 新 增第一发生器 A产生的冷剂蒸汽分别提供给新增第二发生器 E和吸收-发生器 16， 第一发生 器 1的浓溶液经第一溶液热交换器 10之后再流经吸收-发生器 16、 吸热部分汽化后进入分汽 室 17， 形成单效 -回热式三效第三类吸收式热泵。  2 In the process, the dilute solution of the absorption-generator 16 enters the newly added second generator E through the newly added solution heat exchanger B, and the newly added refrigerant vapor generated by the first generator A is separately supplied to the newly added second generator. E and the absorption-generator 16, the concentrated solution of the first generator 1 passes through the first solution heat exchanger 10 and then flows through the absorption-generator 16, and the endothermic portion is vaporized and then enters the steam separation chamber 17, forming a single-effect-return Thermal three-effect third-class absorption heat pump.
图 41所示的单效 -1. 5级第三类吸收式热泵是这样实现的：  The single-effect -1. 5 third-class absorption heat pump shown in Figure 41 is implemented as follows:
①结构上， 在图 1所示的第三类吸收式热泵中， 增加新增溶液热交换器、 新增吸收 -蒸发 器和新增冷剂液泵，将吸收器 3有稀溶液管路经第一溶液热交换器 10与第一发生器 1连通调 整为吸收器 3有稀溶液管路经新增溶液热交换器 B与新增吸收-蒸发器 K连通， 新增吸收-蒸 发器 K还有稀溶液管路经第一溶液热交换器 10与第一发生器 1连通，将第一发生器 1有浓溶 液管路经第一溶液泵 7和第一溶液热交换器 10与第二溶液热交换器 11连通调整为第一发生 器 1有浓溶液管路经第一溶液泵 7、 第一溶液热交换器 10和新增溶液热交换器 B与第二溶液 热交换器 11连通，将蒸发器 6有冷剂蒸汽通道与吸收器 3连通调整为蒸发器 6有冷剂蒸汽通 道与新增吸收-蒸发器 K连通， 第一冷凝器 4增设冷剂液管路经新增冷剂液泵 L与新增吸收- 蒸发器 K连通后新增吸收-蒸发器 K再有冷剂蒸汽通道与吸收器 3连通。  1Structurally, in the third type of absorption heat pump shown in Fig. 1, a new solution heat exchanger, a new absorption-evaporator and a new refrigerant liquid pump are added, and the absorber 3 has a dilute solution line. The first solution heat exchanger 10 is connected to the first generator 1 to be adjusted so that the absorber 3 has a dilute solution line connected to the newly added absorption-evaporator K via the newly added solution heat exchanger B, and the new absorption-evaporator K is further added. The dilute solution line is connected to the first generator 1 via the first solution heat exchanger 10, and the first generator 1 has a concentrated solution line through the first solution pump 7 and the first solution heat exchanger 10 and the second solution The heat exchanger 11 is connected to be adjusted so that the first generator 1 has a concentrated solution line connected to the second solution heat exchanger 11 via the first solution pump 7, the first solution heat exchanger 10, and the new solution heat exchanger B, The evaporator 6 has a refrigerant vapor passage communicating with the absorber 3 to adjust the evaporator 6 to have a refrigerant vapor passage communicating with the newly added absorption-evaporator K, and the first condenser 4 is provided with a refrigerant liquid pipeline through the newly added refrigerant liquid. Pump L is connected to the new absorption-evaporator K and then added absorption-evaporator K and then cold Steam passage 3 communicating with the absorber.
②流程上， 吸收器 3的稀溶液经新增溶液热交换器 B进入新增吸收 -蒸发器 K、吸收来自 蒸发器 6的冷剂蒸汽并放热于流经新增吸收-蒸发器 Κ的冷剂液， 新增吸收-蒸发器 Κ的稀溶 液经第一溶液热交换器 10进入第一发生器 1， 第一发生器 1的浓溶液经溶液泵 7、 第一溶液 热交换器 10、 新增溶液热交换器 Β和第二溶液热交换器 11进入第二发生器 2; 第一冷凝器 4 的冷剂液分成两路——第一路经冷剂液泵 8加压进入蒸发器 6， 第二路经新增冷剂液泵 L加 压后再流经新增吸收 -蒸发器 、吸热成冷剂蒸汽并向吸收器 3提供，形成单效 -1. 5级第三类 吸收式热泵。  2 In the process, the dilute solution of the absorber 3 enters the new absorption-evaporator K through the newly added solution heat exchanger B, absorbs the refrigerant vapor from the evaporator 6, and radiates heat through the new absorption-evaporator. a refrigerant solution, a dilute solution of the new absorption-evaporator 经 enters the first generator 1 through the first solution heat exchanger 10, and the concentrated solution of the first generator 1 passes through the solution pump 7, the first solution heat exchanger 10, The new solution heat exchanger Β and the second solution heat exchanger 11 enter the second generator 2; the refrigerant liquid of the first condenser 4 is divided into two paths - the first passage is pressurized by the refrigerant liquid pump 8 into the evaporator 6, the second way is added by the new refrigerant liquid pump L and then flows through the new absorption-evaporator, the heat is absorbed into the refrigerant vapor and is supplied to the absorber 3, forming a single effect - 1. 5 level third class Absorption heat pump.
图 42所示的单效- 1. 5级第三类吸收式热泵是这样实现的： ①结构上， 在图 1所示的第三类吸收式热泵中， 增加新增溶液热交换器、 新增溶液泵、 新增吸收 -蒸发器和新增冷剂液泵， 将第二发生器 2有浓溶液管路经第二溶液热交换器 11与 吸收器 3连通调整为第二发生器 2有浓溶液管路经第二溶液热交换器 11和新增溶液热交换器 B与新增吸收-蒸发器 K连通， 新增吸收-蒸发器 K还有稀溶液管路经新增溶液泵 D和新增溶 液热交换器 B与吸收器 3连通， 将蒸发器 6有冷剂蒸汽通道与吸收器 3连通调整为蒸发器 6 有冷剂蒸汽通道与新增吸收-蒸发器 K连通，蒸发器 6增设冷剂液管路经新增冷剂液泵 L与新 增吸收-蒸发器 K连通后新增吸收-蒸发器 K再有冷剂蒸汽通道与吸收器 3连通。 The single-effect - 1. 5 third-class absorption heat pump shown in Figure 42 is implemented as follows: 1Structure, in the third type of absorption heat pump shown in Figure 1, adding a new solution heat exchanger, a new solution pump, a new absorption-evaporator and a new refrigerant liquid pump, the second generator 2 The concentrated solution pipeline is connected to the absorber 3 through the second solution heat exchanger 11 to be adjusted to be the second generator 2 having the concentrated solution pipeline passing through the second solution heat exchanger 11 and the newly added solution heat exchanger B and adding The absorption-evaporator K is connected, the new absorption-evaporator K and the dilute solution line are connected to the absorber 3 via the new solution pump D and the new solution heat exchanger B, and the evaporator 6 has a refrigerant vapor channel and The absorber 3 is connected to the evaporator 6 and has a refrigerant vapor passage communicating with the newly added absorption-evaporator K. The evaporator 6 is provided with a refrigerant liquid pipeline connected to the newly added absorption liquid evaporator L through the newly added refrigerant liquid pump L. After that, the absorption-evaporator K is added and the refrigerant vapor passage is connected to the absorber 3.
②流程上，第二发生器 2的浓溶液经第二溶液热交换器 11和新增溶液热交换器 B进入新 增吸收-蒸发器 K、吸收来自蒸发器 6的冷剂蒸汽并放热于流经新增吸收-蒸发器 Κ的冷剂液， 新增吸收-蒸发器 Κ的稀溶液经新增溶液泵 D和新增溶液热交换器 Β进入吸收器 3、 吸收来 自新增吸收-蒸发器 Κ的冷剂蒸汽并放热于被加热介质；蒸发器 6的冷剂液分成两路——第一 路吸收余热成冷剂蒸汽并向新增吸收-蒸发器 Κ提供， 第二路经新增冷剂液泵 L加压后再流 经新增吸收-蒸发器 Κ、吸热成冷剂蒸汽并向吸收器 3提供， 形成单效 -1. 5级第三类吸收式热 泵。  2 In the process, the concentrated solution of the second generator 2 enters the new absorption-evaporator K through the second solution heat exchanger 11 and the new solution heat exchanger B, absorbs the refrigerant vapor from the evaporator 6, and radiates heat. Flow through the new absorption-evaporator enthalpy solution, add a new absorption-evaporator 稀 dilute solution through the new solution pump D and the new solution heat exchanger Β into the absorber 3, absorption from the new absorption-evaporation The refrigerant vapor of the crucible is exothered in the heated medium; the refrigerant liquid of the evaporator 6 is divided into two paths - the first passage absorbs the residual heat into the refrigerant vapor and supplies it to the newly added absorption-evaporator, the second passage The new refrigerant liquid pump L is pressurized and then flows through the new absorption-evaporator Κ, the heat is absorbed into the refrigerant vapor, and is supplied to the absorber 3 to form a single-effect-1. 5 third-class absorption heat pump.
图 43所示的单效 -1. 5级第三类吸收式热泵是这样实现的：  The single-effect -1. 5 third-class absorption heat pump shown in Figure 43 is implemented as follows:
①结构上， 在图 1所示的第三类吸收式热泵中， 增加新增溶液热交换器、 新增溶液泵、 新增吸收 -蒸发器和新增冷剂液泵，将第一发生器 1有浓溶液管路经第一溶液泵 7和第一溶液 热交换器 10与第二溶液热交换器 11连通调整为第一发生器 1有浓溶液管路经第一溶液泵 7、 第一溶液热交换器 10和新增溶液热交换器 Β与新增吸收-蒸发器 Κ连通， 新增吸收-蒸发器 Κ 还有稀溶液管路经新增溶液泵 D和新增溶液热交换器 Β与第二溶液热交换器 11连通，将蒸发 器 6有冷剂蒸汽通道与吸收器 3连通调整为蒸发器 6有冷剂蒸汽通道与新增吸收-蒸发器 Κ连 通， 蒸发器 6增设冷剂液管路经新增冷剂液泵 L与新增吸收-蒸发器 Κ连通后新增吸收-蒸发 器 Κ再有冷剂蒸汽通道与吸收器 3连通。  1Structure, in the third type of absorption heat pump shown in Figure 1, adding a new solution heat exchanger, a new solution pump, a new absorption-evaporator and a new refrigerant liquid pump, the first generator 1 has a concentrated solution pipeline through the first solution pump 7 and the first solution heat exchanger 10 and the second solution heat exchanger 11 connected to adjust to the first generator 1 has a concentrated solution pipeline through the first solution pump 7, first The solution heat exchanger 10 and the new solution heat exchanger Κ are connected to the new absorption-evaporator, and the absorption-evaporator 新增 is added, and the dilute solution line is added to the new solution pump D and the new solution heat exchanger. Communicating with the second solution heat exchanger 11 to connect the evaporator 6 with the refrigerant vapor passage and the absorber 3 to adjust the evaporator 6 to have a refrigerant vapor passage communicating with the newly added absorption-evaporator, and the evaporator 6 is provided with a refrigerant. The liquid pipeline is connected to the absorber 3 by adding a new refrigerant liquid pump L and a new absorption-evaporator 后, and then a refrigerant vapor channel is connected to the absorber 3.
②流程上， 第一发生器 1的浓溶液经溶液泵 7、 第一溶液热交换器 10和新增溶液热交换 器 Β进入新增吸收-蒸发器 ：、吸收来自蒸发器 6的冷剂蒸汽并放热于流经新增吸收-蒸发器 Κ 的冷剂液， 新增吸收-蒸发器 Κ的稀溶液经新增溶液泵 D、 新增溶液热交换器 B和第二溶液 热交换器 11进入第二发生器 2，第二发生器 2的浓溶液经第二溶液热交换器 11进入吸收器 3、 吸收来自新增吸收-蒸发器 K的冷剂蒸汽并加热被加热介质；蒸发器 6的冷剂液分成两路—— 第一路吸收余热成冷剂蒸汽并向新增吸收-蒸发器 K提供， 第二路经新增冷剂液泵 L加压后 再流经新增吸收-蒸发器 K、吸热成冷剂蒸汽并向吸收器 3提供，形成单效 -1. 5级第三类吸收 式热泵。  2 In the process, the concentrated solution of the first generator 1 enters the new absorption-evaporator through the solution pump 7, the first solution heat exchanger 10 and the newly added solution heat exchanger: absorbs the refrigerant vapor from the evaporator 6. And exothermic to the refrigerant liquid flowing through the new absorption-evaporator ,, adding a dilute solution of the absorption-evaporator 经 to the new solution pump D, the new solution heat exchanger B and the second solution heat exchanger 11 Entering the second generator 2, the concentrated solution of the second generator 2 enters the absorber 3 through the second solution heat exchanger 11, absorbs the refrigerant vapor from the newly added absorption-evaporator K, and heats the heated medium; the evaporator 6 The refrigerant liquid is divided into two paths - the first path absorbs the waste heat into the refrigerant vapor and supplies it to the new absorption-evaporator K, and the second channel is pressurized by the newly added refrigerant liquid pump L and then flows through the newly absorbed - The evaporator K, which absorbs heat into a refrigerant vapor and supplies it to the absorber 3 to form a single-effect-1. 5 third-class absorption heat pump.
图 44所示的单效-回热式 1. 5级第三类吸收式热泵是这样实现的- The single-effect-recovery type shown in Figure 44. The fifth-class absorption heat pump of the fifth-class is realized in this way -
①结构上， 在图 2所示的第三类吸收式热泵中， 增加新增溶液热交换器、 新增吸收 -蒸发 器和新增冷剂液泵， 将吸收器 3有稀溶液管路经第一溶液热交换器 10与第二吸收器 13连通 调整为吸收器 3有稀溶液管路经新增溶液热交换器 Β与新增吸收-蒸发器 Κ连通， 新增吸收- 蒸发器 Κ还有稀溶液管路经第一溶液热交换器 10与第二吸收器 13连通，将第三发生器 12有 浓溶液管路经第一溶液泵 7和第一溶液热交换器 10与第二溶液热交换器 11连通调整为第三 发生器 12有浓溶液管路经第一溶液泵 7、 第一溶液热交换器 10和新增溶液热交换器 Β与第 二溶液热交换器 11连通，将蒸发器 6有冷剂蒸汽通道与吸收器 3连通调整为蒸发器 6有冷剂 蒸汽通道与新增吸收-蒸发器 Κ连通，蒸发器 6增设冷剂液管路经新增冷剂液泵 L与新增吸收 -蒸发器 K连通后新增吸收-蒸发器 K再有冷剂蒸汽通道与吸收器 3连通。 1Structurally, in the third type of absorption heat pump shown in Fig. 2, a new solution heat exchanger, a new absorption-evaporator and a new refrigerant liquid pump are added, and the absorber 3 has a dilute solution line. The first solution heat exchanger 10 is connected to the second absorber 13 to be adjusted so that the absorber 3 has a dilute solution line through the new solution heat exchanger and is connected to the new absorption-evaporator, and the absorption-evaporator is added. The dilute solution line is connected to the second absorber 13 via the first solution heat exchanger 10, and the third generator 12 has a concentrated solution line through the first solution pump 7 and the first solution heat exchanger 10 and the second solution. The heat exchanger 11 is connected to be adjusted so that the third generator 12 has a concentrated solution line connected to the second solution heat exchanger 11 via the first solution pump 7, the first solution heat exchanger 10, and the new solution heat exchanger ,, The evaporator 6 has a refrigerant vapor passage connected to the absorber 3 to be adjusted so that the evaporator 6 has a refrigerant vapor passage connected to the newly added absorption-evaporator, and the evaporator 6 adds a refrigerant liquid pipeline through the newly added refrigerant liquid pump L. With new absorption - After the evaporator K is connected, an absorption-evaporator K is added and then a refrigerant vapor passage is connected to the absorber 3.
②流程上， 吸收器 3的稀溶液经新增溶液热交换器 B进入新增吸收 -蒸发器 、吸收来自 蒸发器 6的冷剂蒸汽并放热于流经新增吸收-蒸发器 K的冷剂液， 新增吸收-蒸发器 K的稀溶 液经第一溶液热交换器 10进入第二吸收器 13; 蒸发器 6的冷剂液分成两路——第一路吸收 余热成冷剂蒸汽并向新增吸收-蒸发器 K提供， 第二路经新增冷剂液泵 L加压后再流经新增 吸收-蒸发器 K、吸热成冷剂蒸汽并向吸收器 3提供;第三发生器 12的浓溶液经第一溶液泵 7、 第一溶液热交换器 10、新增溶液热交换器 Β和第二溶液热交换器 11进入第二发生器 2，形成 单效-回热式 1. 5级第三类吸收式热泵。  2 In the process, the dilute solution of the absorber 3 is introduced into the new absorption-evaporator via the newly added solution heat exchanger B, absorbs the refrigerant vapor from the evaporator 6, and radiates heat to the cold flowing through the new absorption-evaporator K. The liquid solution, the dilute solution of the new absorption-evaporator K is introduced into the second absorber 13 through the first solution heat exchanger 10; the refrigerant liquid of the evaporator 6 is divided into two paths - the first path absorbs the residual heat into the refrigerant vapor and Provided to the newly added absorption-evaporator K, the second passage is pressurized by the newly added refrigerant liquid pump L, then flows through the new absorption-evaporator K, absorbs heat into the refrigerant vapor, and supplies it to the absorber 3; The concentrated solution of the generator 12 enters the second generator 2 via the first solution pump 7, the first solution heat exchanger 10, the new solution heat exchanger Β and the second solution heat exchanger 11 to form a single-effect-recovery type 1. Class 5 third type absorption heat pump.
图 45所示的单效-回热式 1. 5级第三类吸收式热泵是这样实现的：  The single-effect-recovery type shown in Figure 45. The fifth-stage type III absorption heat pump is realized as follows:
①结构上， 在图 2所示的第三类吸收式热泵中， 增加新增溶液热交换器、 新增溶液泵、 新增吸收 -蒸发器和新增冷剂液泵， 将第二发生器 2有浓溶液管路经第二溶液热交换器 11与 吸收器 3连通调整为第二发生器 2有浓溶液管路经第二溶液热交换器 11和新增溶液热交换器 Β与新增吸收-蒸发器 Κ连通， 新增吸收-蒸发器 Κ还有稀溶液管路经新增溶液泵 D和新增溶 液热交换器 Β与吸收器 3连通， 将蒸发器 6有冷剂蒸汽通道与吸收器 3连通调整为蒸发器 6 有冷剂蒸汽通道与新增吸收-蒸发器 Κ连通，蒸发器 6增设冷剂液管路经新增冷剂液泵 L与新 增吸收-蒸发器 Κ连通后新增吸收-蒸发器 Κ再有冷剂蒸汽通道与吸收器 3连通。  1Structurally, in the third type of absorption heat pump shown in Figure 2, adding a new solution heat exchanger, a new solution pump, a new absorption-evaporator and a new refrigerant liquid pump, the second generator 2 The concentrated solution pipeline is connected to the absorber 3 through the second solution heat exchanger 11 to be adjusted to be the second generator 2, the concentrated solution pipeline is passed through the second solution heat exchanger 11 and the new solution heat exchanger, and newly added The absorption-evaporator is connected, the new absorption-evaporator and the dilute solution line are connected to the absorber 3 via the new solution pump D and the new solution heat exchanger, and the evaporator 6 has a refrigerant vapor channel and The absorber 3 is connected and adjusted to the evaporator 6 with a refrigerant vapor passage connected to the newly added absorption-evaporator, and the evaporator 6 is provided with a refrigerant liquid pipeline connected to the newly added absorption-evaporator via the newly added refrigerant liquid pump L. After that, an absorption-evaporator is added, and then a refrigerant vapor passage is connected to the absorber 3.
②流程上，第二发生器 2的浓溶液经第二溶液热交换器 11和新增溶液热交换器 Β进入新 增吸收-蒸发器 Κ、吸收来自蒸发器 6的冷剂蒸汽并放热于流经新增吸收-蒸发器 Κ的冷剂液， 新增吸收-蒸发器 Κ的稀溶液经新增溶液泵 D和新增溶液热交换器 Β进入吸收器 3、 吸收来 自新增吸收-蒸发器 Κ的冷剂蒸汽并放热于被加热介质；蒸发器 6的冷剂液分成两路——第一 路吸收余热成冷剂蒸汽并向新增吸收-蒸发器 Κ提供， 第二路经新增冷剂液泵 L加压后再流 经新增吸收-蒸发器 Κ、 吸热成冷剂蒸汽并向吸收器 3提供， 形成单效-回热式 1. 5级第三类 吸收式热泵。  2 In the process, the concentrated solution of the second generator 2 passes through the second solution heat exchanger 11 and the newly added solution heat exchanger, enters the new absorption-evaporator, absorbs the refrigerant vapor from the evaporator 6, and radiates heat. Flow through the new absorption-evaporator enthalpy solution, add a new absorption-evaporator 稀 dilute solution through the new solution pump D and the new solution heat exchanger Β into the absorber 3, absorption from the new absorption-evaporation The refrigerant vapor of the crucible is exothered in the heated medium; the refrigerant liquid of the evaporator 6 is divided into two paths - the first passage absorbs the residual heat into the refrigerant vapor and supplies it to the newly added absorption-evaporator, the second passage The new refrigerant liquid pump L is pressurized and then flows through the new absorption-evaporator Κ, the heat is absorbed into the refrigerant vapor, and is supplied to the absorber 3 to form a single-effect-recovery type 1. Heat pump.
图 46所示的单效-回热式 1. 5级第三类吸收式热泵是这样实现的：  The single-effect-recovery type shown in Figure 46. The fifth-stage type III absorption heat pump is realized as follows:
①结构上， 在图 2所示的第三类吸收式热泵中， 增加新增溶液热交换器、 新增溶液泵、 新增吸收 -蒸发器和新增冷剂液泵， 将第三发生器 12有浓溶液管路经第一溶液泵 7和第一溶 液热交换器 10与第二溶液热交换器 11连通调整为第三发生器 12有浓溶液管路经第一溶液泵 7、 第一溶液热交换器 10和新增溶液热交换器 Β与新增吸收-蒸发器 Κ连通， 新增吸收 -蒸发 器 Κ还有稀溶液管路经新增溶液泵 D和新增溶液热交换器 Β与第二溶液热交换器 11连通，将 蒸发器 6有冷剂蒸汽通道与吸收器 3连通调整为蒸发器 6有冷剂蒸汽通道与新增吸收-蒸发器 Κ连通， 蒸发器 6增设冷剂液管路经新增冷剂液泵 L与新增吸收-蒸发器 Κ连通后新增吸收- 蒸发器 Κ再有冷剂蒸汽通道与吸收器 3连通。  1Structurally, in the third type of absorption heat pump shown in Figure 2, adding a new solution heat exchanger, a new solution pump, a new absorption-evaporator and a new refrigerant liquid pump, the third generator 12 has a concentrated solution pipeline through the first solution pump 7 and the first solution heat exchanger 10 and the second solution heat exchanger 11 communicated to adjust the third generator 12 has a concentrated solution pipeline through the first solution pump 7, first The solution heat exchanger 10 and the new solution heat exchanger Κ are connected to the new absorption-evaporator, and the new absorption-evaporator and the dilute solution line are added to the new solution pump D and the new solution heat exchanger. Communicating with the second solution heat exchanger 11 to connect the evaporator 6 with the refrigerant vapor passage and the absorber 3 to adjust the evaporator 6 to have a refrigerant vapor passage communicating with the newly added absorption-evaporator, and the evaporator 6 is provided with a refrigerant. The liquid pipeline is connected to the absorber 3 by adding a new refrigerant liquid pump L to the new absorption-evaporator and then adding an absorption-evaporator and then a refrigerant vapor passage.
②流程上， 第三发生器 12的浓溶液经溶液泵 7、 第一溶液热交换器 10和新增溶液热交 换器 Β进入新增吸收-蒸发器 Κ、 吸收来自蒸发器 6的冷剂蒸汽并放热于流经新增吸收 -蒸发 器 Κ的冷剂液， 新增吸收-蒸发器 Κ的稀溶液经新增溶液泵 D、 新增溶液热交换器 B和第二 溶液热交换器 11进入第二发生器 2， 第二发生器 2的浓溶液经第二溶液热交换器 11进入吸 收器 3、 吸收来自新增吸收-蒸发器 K的冷剂蒸汽并放热于被加热介质； 蒸发器 6的冷剂液分 成两路——第一路吸收余热成冷剂蒸汽并向新增吸收-蒸发器 K提供，第二路经新增冷剂液泵 L加压后再流经新增吸收-蒸发器 K、 吸热成冷剂蒸汽并向吸收器 3提供， 形成单效-回热式 1. 5级第三类吸收式热泵。 图 47所示的单效-回热式 1. 5级第三类吸收式热泵是这样实现的： 2 In the process, the concentrated solution of the third generator 12 passes through the solution pump 7, the first solution heat exchanger 10 and the newly added solution heat exchanger, enters the new absorption-evaporator, and absorbs the refrigerant vapor from the evaporator 6. And exothermic to the cold liquid flowing through the new absorption-evaporator, adding a dilute solution of the absorption-evaporator 经 through the new solution pump D, the new solution heat exchanger B and the second solution heat exchanger 11 Entering the second generator 2, the concentrated solution of the second generator 2 enters the absorber 3 through the second solution heat exchanger 11, absorbs the refrigerant vapor from the newly added absorption-evaporator K, and releases the heat to the heated medium; The refrigerant liquid of the device 6 is divided into two paths - the first path absorbs the residual heat into the refrigerant vapor and is supplied to the newly added absorption-evaporator K, and the second path is pressurized by the newly added refrigerant liquid pump L, and then flows through the new The absorption-evaporator K, the heat-absorbing refrigerant vapor is supplied to the absorber 3 to form a single-effect-recovery type 1.5 third-class absorption heat pump. The single-effect-recovery type 1.5 third-class absorption heat pump shown in Fig. 47 is realized as follows:
①结构上， 在图 5所示的第三类吸收式热泵中， 取消第三溶液泵 21， 吸收器 3有稀溶液 管路经第三溶液热交换器 15与吸收-发生器 16连通； 增加新增冷剂液泵， 取消蒸发器 6与吸 收器 3连通的冷剂蒸汽通道，第一冷凝器 4增设冷剂液管路经新增冷剂液泵 L与吸收-发生器 16连通后吸收-发生器 16还有冷剂蒸汽通道与吸收器 3连通。  1 structurally, in the third type of absorption heat pump shown in FIG. 5, the third solution pump 21 is cancelled, and the diluted solution line of the absorber 3 is connected to the absorption-generator 16 via the third solution heat exchanger 15; The refrigerant liquid pump is newly added, and the refrigerant vapor passage connecting the evaporator 6 and the absorber 3 is canceled, and the refrigerant line of the first condenser 4 is added by the newly added refrigerant liquid pump L and the absorption-generator 16 is connected and absorbed. The generator 16 also has a refrigerant vapor passage in communication with the absorber 3.
②流程上， 吸收器 3的稀溶液经第三溶液热交换器 15进入吸收-发生器 16、 吸收来自蒸 发器 6的冷剂蒸汽并分别放热于流经吸收-发生器 16的溶液和冷剂液； 第一冷凝器 4的冷剂 液分成两路——第一路经冷剂液泵 8加压进入蒸发器 6， 第二路经新增冷剂液泵 L加压后再 流经新增吸收-蒸发器 K、 吸热成冷剂蒸汽并向吸收器 3提供， 形成单效-回热式 1. 5级第三 类吸收式热泵。  2 In the process, the dilute solution of the absorber 3 enters the absorption-generator 16 through the third solution heat exchanger 15, absorbs the refrigerant vapor from the evaporator 6, and respectively releases the solution flowing through the absorption-generator 16 and is cooled. The liquid of the first condenser 4 is divided into two paths - the first passage is pressurized by the refrigerant liquid pump 8 into the evaporator 6, and the second passage is pressurized by the newly added refrigerant liquid pump L and then flows through The absorption-evaporator K and the heat-absorbing refrigerant vapor are added to the absorber 3 to form a single-effect-recovery type 1.5 third-class absorption heat pump.
图 48所示的单效-回热式 1. 5级第三类吸收式热泵是这样实现的：  The single-effect-recovery type shown in Figure 48. The fifth-class type III absorption heat pump is realized as follows:
①结构上， 在图 5所示的第三类吸收式热泵中， 取消第三溶液泵 21， 吸收器 3有稀溶液 管路经第三溶液热交换器 15与吸收-发生器 16连通；增加新增吸收 -蒸发器和新增冷剂液泵， 将吸收-发生器 16有稀溶液管路经第一溶液热交换器 10与第一发生器 1连通调整为吸收-发 生器 16有稀溶液管路直接与新增吸收-蒸发器 Κ连通，新增吸收-蒸发器 Κ还有稀溶液管路经 第一溶液热交换器 10与第一发生器 1连通，将第一蒸发器 6有冷剂蒸汽通道与吸收器 3连通 调整为第一蒸发器 6有冷剂蒸汽通道与新增吸收-蒸发器 Κ连通，第一冷凝器 4增设冷剂液管 路经新增冷剂液泵 L与吸收-发生器 16连通后吸收-发生器 16还有冷剂蒸汽通道与吸收器 3 连通。  1 structurally, in the third type of absorption heat pump shown in FIG. 5, the third solution pump 21 is eliminated, and the absorber 3 has a dilute solution line connected to the absorption-generator 16 via the third solution heat exchanger 15; A new absorption-evaporator and a new refrigerant liquid pump are added, and the absorption-generator 16 has a dilute solution line connected to the first generator 1 via the first solution heat exchanger 10 to be adjusted to absorb-the generator 16 has a dilute solution. The pipeline is directly connected to the new absorption-evaporator, and the new absorption-evaporator and the dilute solution pipeline are connected to the first generator 1 via the first solution heat exchanger 10, and the first evaporator 6 is cooled. The vapor passage of the agent is connected to the absorber 3 to be adjusted so that the first evaporator 6 has a refrigerant vapor passage connected to the newly added absorption-evaporator, and the first condenser 4 adds a refrigerant liquid pipeline through the newly added refrigerant liquid pump L and After the absorption-generator 16 is connected, the absorption-generator 16 and the refrigerant vapor passage are in communication with the absorber 3.
②流程上， 吸收器 3的稀溶液经第三溶液热交换器 15降温降压进入吸收-发生器 16, 吸 收-发生器 16的稀溶液进入新增吸收-蒸发器 Κ、 吸收来自蒸发器 6的冷剂蒸汽并放热于流经 吸收-发生器 16的冷剂液， 新增吸收-蒸发器 Κ的稀溶液经第一溶液热交换器 10进入第一发 生器 1 ; 第一冷凝器 4的冷剂液分成两路——第一路经冷剂液泵 8加压进入蒸发器 6， 第二路 经新增冷剂液泵 L加压后再流经新增吸收-蒸发器 Κ、 吸热成冷剂蒸汽并向吸收器 3提供， 形 成单效-回热式 1. 5级第三类吸收式热泵。  2 In the process, the dilute solution of the absorber 3 is cooled down by the third solution heat exchanger 15 into the absorption-generator 16, the dilute solution of the absorption-generator 16 enters the new absorption-evaporator, and the absorption is from the evaporator 6. The refrigerant vapor is exothermic to the refrigerant liquid flowing through the absorption-generator 16, and the dilute solution of the new absorption-evaporator 新增 is introduced into the first generator 1 through the first solution heat exchanger 10; the first condenser 4 The refrigerant liquid is divided into two paths - the first passage is pressurized into the evaporator 6 by the refrigerant liquid pump 8, and the second passage is pressurized by the newly added refrigerant liquid pump L, and then flows through the new absorption-evaporator, The heat is cooled to a refrigerant vapor and supplied to the absorber 3 to form a single-effect-recovery type 1.5 third-stage absorption heat pump.
图 49所示的单效-回热式 1. 5级第三类吸收式热泵是这样实现的：  The single-effect-recovery type shown in Figure 49. The fifth-stage type III absorption heat pump is implemented as follows:
①结构上， 在图 3所示的第三类吸收式热泵中， 增加新增溶液热交换器、 新增溶液泵、 新增吸收-蒸发器和新增节流阀， 将第二发生器 2有浓溶液管路经第二溶液热交换器 11与吸 收器 3连通调整为第二发生器 2有浓溶液管路经第二溶液热交换器 11和新增溶液热交换器 Β 与新增吸收-蒸发器 Κ连通， 新增吸收-蒸发器 Κ还有稀溶液管路经新增溶液泵 D和新增溶液 热交换器 Β与吸收器 3连通， 将第一蒸发器 6有冷剂蒸汽通道与吸收器 3连通调整为第一蒸 发器 6有冷剂蒸汽通道与新增吸收-蒸发器 Κ连通，第二冷凝器 5增设冷剂液管路经新增节流 阀 C与新增吸收-蒸发器 Κ连通后新增吸收-蒸发器 Κ再有冷剂蒸汽通道与吸收器 3连通。  1Structurally, in the third type of absorption heat pump shown in Fig. 3, adding a new solution heat exchanger, a new solution pump, a new absorption-evaporator and a new throttle valve, the second generator 2 The concentrated solution line is connected to the absorber 3 via the second solution heat exchanger 11 to be adjusted to the second generator 2, the concentrated solution line is passed through the second solution heat exchanger 11 and the new solution heat exchanger, and the new absorption is performed. - The evaporator is connected, the new absorption-evaporator and the dilute solution line are connected to the absorber 3 via the new solution pump D and the new solution heat exchanger, and the first evaporator 6 has a refrigerant vapor channel. The communication with the absorber 3 is adjusted so that the first evaporator 6 has a refrigerant vapor passage connected to the newly added absorption-evaporator, and the second condenser 5 adds a refrigerant liquid pipeline through the newly added throttle valve C and newly absorbed - After the evaporator is connected, an absorption-evaporator is added, and then a refrigerant vapor passage is connected to the absorber 3.
②流程上，第二发生器 2的浓溶液经第二溶液热交换器 11和新增溶液热交换器 Β进入新 增吸收-蒸发器 Κ、 吸收来自第一蒸发器 6的冷剂蒸汽并放热于流经新增吸收-蒸发器 Κ的冷 剂液， 新增吸收-蒸发器 Κ的稀溶液经新增溶液泵 D和新增溶液热交换器 Β进入吸收器 3、 吸收来自新增吸收-蒸发器 Κ的冷剂蒸汽并放热于被加热介质；第二冷凝器 5的冷剂液分成两 路——第一路经节流阀 9进入第一蒸发器 6， 第二路经新增节流阀 C节流后再流经新增吸收- 蒸发器 Κ、 吸热成冷剂蒸汽并向吸收器 3提供， 形成单效-回热式 1. 5级第三类吸收式热泵。  2 In the process, the concentrated solution of the second generator 2 passes through the second solution heat exchanger 11 and the newly added solution heat exchanger, enters the new absorption-evaporator, absorbs the refrigerant vapor from the first evaporator 6, and puts The hot liquid flows through the new absorption-evaporator ,, and the dilute solution of the new absorption-evaporator 新增 is added to the absorber through the new solution pump D and the new solution heat exchanger, and the absorption is from the new absorption. - the refrigerant vapor of the evaporator 并 is radiated to the heated medium; the refrigerant liquid of the second condenser 5 is divided into two paths - the first passage enters the first evaporator 6 via the throttle valve 9, the second passage is new After the throttle valve C is throttled, it flows through the new absorption-evaporator Κ, absorbs the refrigerant vapor, and supplies it to the absorber 3 to form a single-effect-recovery type 1.5 third-class absorption heat pump.
这里要说明的是， 在特定情况下， 第二冷凝器 5的冷剂液全部经新增节流阀 C节流后再 流经新增吸收-蒸发器 K, 此时没有冷剂液经节流阀 9向第一蒸发器 6提供。 It should be noted here that, in a specific case, the refrigerant liquid of the second condenser 5 is all throttled by the newly added throttle valve C. Flow through the new absorption-evaporator K, at which time no refrigerant liquid is supplied to the first evaporator 6 via the throttle valve 9.
图 50所示的单效-回热式 1. 5级第三类吸收式热泵是这样实现的：  The single-effect-recovery type shown in Figure 50. The fifth-stage type III absorption heat pump is realized as follows:
①结构上， 在图 3所示的第三类吸收式热泵中， 增加新增溶液热交换器、 新增溶液泵、 新增吸收 -蒸发器和新增冷剂液泵，将分汽室 17有浓溶液管路经第二溶液泵 14和第三溶液热 交换器 15与第二溶液热交换器 11连通调整为分汽室 17有浓溶液管路经第二溶液泵 14、 第 三溶液热交换器 15和新增溶液热交换器 B与新增吸收-蒸发器 K连通，新增吸收-蒸发器 K还 有稀溶液管路经新增溶液泵 D和新增溶液热交换器 B与第二溶液热交换器 11连通，取消第一 蒸发器 6与吸收器 3连通的冷剂蒸汽通道， 蒸发器 6增设冷剂液管路经新增冷剂液泵 L与新 增吸收-蒸发器 K连通后新增吸收-蒸发器 K再有冷剂蒸汽通道与吸收器 3连通。  1Structurally, in the third type of absorption heat pump shown in Fig. 3, a new solution heat exchanger, a new solution pump, a new absorption-evaporator and a new refrigerant liquid pump are added, and the steam separation chamber 17 is added. The concentrated solution line is connected to the second solution heat exchanger 11 via the second solution pump 14 and the third solution heat exchanger 15 to be adjusted to the steam dividing chamber 17 having the concentrated solution line passing through the second solution pump 14, the third solution heat The exchanger 15 and the new solution heat exchanger B are connected to the newly added absorption-evaporator K, and the new absorption-evaporator K and the dilute solution pipeline are added to the new solution pump D and the new solution heat exchanger B and the first The two solution heat exchanger 11 is connected to cancel the refrigerant vapor passage connecting the first evaporator 6 and the absorber 3, and the evaporator 6 is provided with a refrigerant liquid pipeline via the newly added refrigerant liquid pump L and the newly added absorption-evaporator K. After the connection, the absorption-evaporator K is added and the refrigerant vapor channel is connected to the absorber 3.
②流程上， 分汽室 17的浓溶液经第二溶液泵 14、 第三溶液热交换器 15和新增溶液热交 换器 B进入新增吸收-蒸发器 K、 吸收来自第一蒸发器 6的冷剂蒸汽并放热于流经新增吸收- 蒸发器 Κ的冷剂液， 新增吸收-蒸发器 Κ的稀溶液经新增溶液泵 D、 新增溶液热交换器 B和 第二溶液热交换器 11进入第二发生器 2， 第二发生器 2的浓溶液经第二溶液热交换器 11进 入吸收器 3、 吸收来自新增吸收-蒸发器 K的冷剂蒸汽并放热于被加热介质； 第一蒸发器 6的 冷剂液分成两路——第一路吸收余热成冷剂蒸汽并向新增吸收-蒸发器 K提供，第二路经新增 冷剂液泵 L加压后再流经新增吸收-蒸发器 K、 吸热成冷剂蒸汽并向吸收器 3提供， 形成单效 -回热式 1. 5级第三类吸收式热泵。  2 In the process, the concentrated solution of the steam separation chamber 17 enters the new absorption-evaporator K through the second solution pump 14, the third solution heat exchanger 15 and the new solution heat exchanger B, and absorbs the absorption from the first evaporator 6. The refrigerant vapor is exothermic to the refrigerant liquid flowing through the new absorption-evaporator, and the dilute solution of the absorption-evaporator is added to the new solution pump D, the new solution heat exchanger B and the second solution heat. The exchanger 11 enters the second generator 2, and the concentrated solution of the second generator 2 enters the absorber 3 via the second solution heat exchanger 11, absorbs the refrigerant vapor from the newly added absorption-evaporator K, and radiates heat to be heated. The medium; the refrigerant liquid of the first evaporator 6 is divided into two paths - the first path absorbs the residual heat into the refrigerant vapor and is supplied to the newly added absorption-evaporator K, and the second path is pressurized by the newly added refrigerant liquid pump L. Then, a new type of absorption-evaporator K, an endothermic refrigerant vapor is supplied to the absorber 3 to form a single-effect-recovery type 1.
图 51所示的单效-回热式 1. 5级第三类吸收式热泵是这样实现的：  The single-effect-recovery type shown in Figure 51. The fifth-class third-class absorption heat pump is realized as follows:
①结构上， 在图 6所示的第三类吸收式热泵中， 增加新增溶液热交换器、 新增吸收-蒸发 器和新增冷剂液泵，将吸收器 3有稀溶液管路经第三溶液热交换器 15和吸收-发生器 16与分 汽室 17连通调整为吸收器 3有稀溶液管路经新增溶液热交换器 Β与新增吸收-蒸发器 Κ连通， 新增吸收-蒸发器 Κ还有稀溶液管路经第三溶液热交换器 15和吸收-发生器 16与分汽室 17连 通，将第二溶液泵 14有浓溶液管路经第三溶液热交换器 15与第二溶液热交换器 11连通调整 为第二溶液泵 14有浓溶液管路经第三溶液热交换器 15和新增溶液热交换器 Β与第二溶液热 交换器 11连通，将第二蒸发器 19有冷剂蒸汽通道与吸收器 3连通调整为第二蒸发器 19有冷 剂蒸汽通道与新增吸收-蒸发器 Κ连通， 第二蒸发器 19增设冷剂液管路经新增冷剂液泵 L与 新增吸收-蒸发器 Κ连通后新增吸收-蒸发器 Κ再有冷剂蒸汽通道与吸收器 3连通。  1Structurally, in the third type of absorption heat pump shown in Fig. 6, the new solution heat exchanger, the new absorption-evaporator and the newly added refrigerant liquid pump are added, and the absorber 3 has a dilute solution line. The third solution heat exchanger 15 and the absorption-generator 16 are connected to the steam distribution chamber 17 to be adjusted so that the absorber 3 has a dilute solution line and is connected to the new absorption-evaporator via the new solution heat exchanger, and newly absorbed. - the evaporator Κ and the dilute solution line are in communication with the steam dividing chamber 17 via the third solution heat exchanger 15 and the absorption-generator 16 , and the second solution pump 14 has a concentrated solution line through the third solution heat exchanger 15 Connected with the second solution heat exchanger 11 to adjust the second solution pump 14 to have a concentrated solution line connected to the second solution heat exchanger 11 via the third solution heat exchanger 15 and the new solution heat exchanger ,, the second The evaporator 19 has a refrigerant vapor passage connected to the absorber 3 to be adjusted so that the second evaporator 19 has a refrigerant vapor passage connected to the newly added absorption-evaporator, and the second evaporator 19 adds a refrigerant liquid line through the newly added cold. Adding absorption-evaporation after the agent liquid pump L is connected to the new absorption-evaporator Further Κ refrigerant vapor passage 3 communicating with the absorber.
②流程上， 吸收器 3的稀溶液经新增溶液热交换器 Β进入新增吸收 -蒸发器{、 吸收来自 第二蒸发器 19的冷剂蒸汽并放热于流经新增吸收-蒸发器 Κ的冷剂液，新增吸收-蒸发器 Κ的 稀溶液经第三溶液热交换器 15之后再流经吸收-发生器 16、 吸热部分汽化进入分汽室 17， 分 汽室 17的浓溶液经第二溶液泵 14、 第三溶液热交换器 15、 新增溶液热交换器 Β和第二溶液 热交换器 11进入第二发生器 2，第二发生器 2的浓溶液经第二溶液热交换器 11进入吸收器 3、 吸收来自新增吸收-蒸发器 Κ的冷剂蒸汽并放热于被加热介质； 第二蒸发器 19的冷剂液分成 两路——第一路吸收余热成冷剂蒸汽并向新增吸收-蒸发器 Κ提供，第二路经新增冷剂液泵 L 加压后再流经新增吸收-蒸发器 Κ、吸热成冷剂蒸汽并向吸收器 3提供，形成单效-回热式 1. 5 级第三类吸收式热泵。  2 In the process, the dilute solution of the absorber 3 is passed through a new solution heat exchanger to enter a new absorption-evaporator {, absorbing the refrigerant vapor from the second evaporator 19 and radiating heat through the new absorption-evaporator The cold refrigerant liquid of the crucible, the dilute solution of the absorption-evaporator 新增 is added to the absorption-generator 16 through the third solution heat exchanger 15, and the endothermic portion is vaporized into the separation chamber 17, and the concentration of the separation chamber 17 is concentrated. The solution enters the second generator 2 through the second solution pump 14, the third solution heat exchanger 15, the new solution heat exchanger Β and the second solution heat exchanger 11, and the concentrated solution of the second generator 2 passes through the second solution The heat exchanger 11 enters the absorber 3, absorbs the refrigerant vapor from the newly added absorption-evaporator and releases the heat to the heated medium; the refrigerant liquid of the second evaporator 19 is divided into two paths - the first path absorbs the residual heat into The refrigerant vapor is supplied to the newly added absorption-evaporator, and the second passage is pressurized by the newly added refrigerant liquid pump L, and then flows through the new absorption-evaporator, the heat is absorbed into the refrigerant vapor, and is directed to the absorber 3. Provided to form a single-effect-recovery type 1. Class 5 absorption heat pump.
图 52所示的单效-回热式 1. 5级第三类吸收式热泵是这样实现的：  The single-effect-recovery type shown in Figure 52. The fifth-class third-class absorption heat pump is realized as follows:
①结构上， 在图 6所示的第三类吸收式热泵中， 增加新增溶液热交换器、 新增溶液泵、 新增吸收-蒸发器和新增冷剂液泵， 将第二溶液热交换器 11有浓溶液管路与吸收器 3连通调 整为第二溶液热交换器 11有浓溶液管路经新增溶液热交换器 Β与新增吸收-蒸发器 Κ连通， 新增吸收-蒸发器 K还有稀溶液管路经新增溶液泵 D和新增溶液热交换器 B与吸收器 3连通， 将第二蒸发器 19有冷剂蒸汽通道与吸收器 3连通调整为第二蒸发器 19有冷剂蒸汽通道与新 增吸收-蒸发器 K连通，第三冷凝器 18增设冷剂液管路经新增冷剂液泵 L与新增吸收-蒸发器 K连通后新增吸收-蒸发器 K再有冷剂蒸汽通道与吸收器 3连通。 1Structurally, in the third type of absorption heat pump shown in Fig. 6, adding a new solution heat exchanger, a new solution pump, a new absorption-evaporator and a new refrigerant liquid pump, and the second solution heat The exchanger 11 has a concentrated solution line connected to the absorber 3 and is adjusted to be a second solution heat exchanger 11 having a concentrated solution line connected to the new absorption-evaporator via a new solution heat exchanger. The new absorption-evaporator K and the dilute solution pipeline are connected to the absorber 3 via the new solution pump D and the new solution heat exchanger B, and the second evaporator 19 has a refrigerant vapor passage connected to the absorber 3 to adjust The second evaporator 19 has a refrigerant vapor passage communicating with the newly added absorption-evaporator K, and the third condenser 18 adds a refrigerant liquid pipeline through the newly added refrigerant liquid pump L to communicate with the newly added absorption-evaporator K. A new absorption-evaporator K is added and a refrigerant vapor passage is connected to the absorber 3.
②流程上，第二发生器 2的浓溶液经第二溶液热交换器 11和新增溶液热交换器 B进入新 增吸收-蒸发器 K、吸收来自第二蒸发器 19的冷剂蒸汽并放热于流经新增吸收-蒸发器 Κ的冷 剂液， 新增吸收-蒸发器 Κ的稀溶液经新增溶液泵 D和新增溶液热交换器 Β进入吸收器 3、 吸收来自新增吸收-蒸发器 Κ的冷剂蒸汽并放热于被加热介质； 第三冷凝器 18的冷剂液分成 两路——第一路经第二冷剂液泵 20加压进入第二蒸发器 19， 第二路经新增冷剂液泵 L加压 后再流经新增吸收-蒸发器 Κ、 吸热成冷剂蒸汽并向吸收器 3提供， 形成单效-回热式 1. 5级 第三类吸收式热泵。  2 In the process, the concentrated solution of the second generator 2 enters the new absorption-evaporator K through the second solution heat exchanger 11 and the new solution heat exchanger B, absorbs the refrigerant vapor from the second evaporator 19, and discharges The hot liquid flows through the new absorption-evaporator ,, and the dilute solution of the new absorption-evaporator 新增 is added to the absorber through the new solution pump D and the new solution heat exchanger, and the absorption is from the new absorption. - the refrigerant vapor of the evaporator is vented and exothermic to the heated medium; the refrigerant liquid of the third condenser 18 is split into two paths - the first passage is pressurized by the second refrigerant liquid pump 20 into the second evaporator 19, The second pass is pressurized by a new refrigerant liquid pump L and then flows through a new absorption-evaporator Κ, which absorbs heat into a refrigerant vapor and supplies it to the absorber 3 to form a single-effect-recovery type 1. Three types of absorption heat pumps.
图 53所示的单效-回热式 1. 5级第三类吸收式热泵是这样实现的- Single-effect-recovery type shown in Figure 53. Class 5 third-class absorption heat pump is realized like this -
①结构上， 在图 6所示的第三类吸收式热泵中， 增加新增溶液热交换器、 新增溶液泵、 新增吸收 -蒸发器和新增冷剂液泵，将分汽室 17有浓溶液管路经第二溶液泵 14和第三溶液热 交换器 15与第二溶液热交换器 11连通调整为分汽室 17有浓溶液管路经第二溶液泵 14、 第 三溶液热交换器 15和新增溶液热交换器 Β与新增吸收-蒸发器 Κ连通，新增吸收-蒸发器 Κ还 有稀溶液管路经新增溶液泵 D和新增溶液热交换器 Β与第二溶液热交换器 11连通，将第二蒸 发器 19有冷剂蒸汽通道与吸收器 3连通调整为第二蒸发器 19有冷剂蒸汽通道与新增吸收- 蒸发器 Κ连通， 第二蒸发器 19增设冷剂液管路经新增冷剂液泵 L与新增吸收-蒸发器 Κ连通 后新增吸收-蒸发器 Κ再有冷剂蒸汽通道与吸收器 3连通。 1Structally, in the third type of absorption heat pump shown in Fig. 6, adding a new solution heat exchanger, a new solution pump, a new absorption-evaporator and a new refrigerant liquid pump, the steam separation chamber 17 The concentrated solution line is connected to the second solution heat exchanger 11 via the second solution pump 14 and the third solution heat exchanger 15 to be adjusted to the steam dividing chamber 17 having the concentrated solution line passing through the second solution pump 14, the third solution heat The exchanger 15 and the new solution heat exchanger Κ are connected to the new absorption-evaporator, and the new absorption-evaporator and the dilute solution line are added to the new solution pump D and the new solution heat exchanger. The two solution heat exchanger 11 is in communication, and the second evaporator 19 has a refrigerant vapor passage connected to the absorber 3 to be adjusted to be a second evaporator 19 having a refrigerant vapor passage communicating with the newly added absorption-evaporator, the second evaporator 19 Adding a refrigerant liquid pipeline is connected with the new absorption-evaporator by adding a new refrigerant liquid pump L, and then adding an absorption-evaporator, and then a refrigerant vapor passage is connected to the absorber 3.
②流程上， 分汽室 17的浓溶液经第二溶液泵 14、 第三溶液热交换器 15和新增溶液热交 换器 Β进入新增吸收 -蒸发器！^吸收来自第二蒸发器 19的冷剂蒸汽并放热于流经新增吸收- 蒸发器 Κ的冷剂液， 新增吸收-蒸发器 Κ的稀溶液经新增溶液泵 D、 新增溶液热交换器 B和 第二溶液热交换器 11进入第二发生器 2， 第二发生器 2的浓溶液经第二溶液热交换器 11进 入吸收器 3、 吸收来自新增吸收-蒸发器 K的冷剂蒸汽并放热于被加热介质； 第二蒸发器 19 的冷剂液分成两路——第一路吸收余热成冷剂蒸汽并向新增吸收-蒸发器 K提供，第二路经新 增冷剂液泵 L加压后再流经新增吸收-蒸发器 K、 吸热成冷剂蒸汽并向吸收器 3提供， 形成单 效-回热式 1. 5级第三类吸收式热泵。  2 In the process, the concentrated solution of the steam separation chamber 17 passes through the second solution pump 14, the third solution heat exchanger 15 and the newly added solution heat exchanger Β into the new absorption-evaporator! ^ Absorbing the refrigerant vapor from the second evaporator 19 and radiating heat to the refrigerant liquid flowing through the new absorption-evaporator, adding a dilute solution of the absorption-evaporator 经 to the new solution pump D, adding a new solution The heat exchanger B and the second solution heat exchanger 11 enter the second generator 2, and the concentrated solution of the second generator 2 enters the absorber 3 through the second solution heat exchanger 11 to absorb the absorption from the new absorption-evaporator K. The refrigerant vapor is exothermic to the heated medium; the refrigerant liquid of the second evaporator 19 is divided into two paths - the first passage absorbs the residual heat into the refrigerant vapor and supplies it to the newly added absorption-evaporator K, and the second passage is new The fifth-stage absorption heat pump is a single-effect-recovery type 1. Class 5 third-stage absorption heat pump. The refrigerant is pumped through the new absorption-evaporator K and the heat-absorbing refrigerant vapor is supplied to the absorber 3. .
图 54所示的单效-回热式 1. 5级第三类吸收式热泵是这样实现的：  The single-effect-recovery type shown in Figure 54. The fifth-class third-class absorption heat pump is realized as follows:
①结构上， 在图 6所示的第三类吸收式热泵中， 增加新增溶液热交换器、 新增吸收 -蒸发 器和新增冷剂液泵， 将吸收-发生器 16有稀溶液管路经第一溶液热交换器 10与第一发生器 1 连通调整为吸收-发生器 16有稀溶液管路经第一溶液热交换器 10与新增吸收-蒸发器 Κ连通， 新增吸收-蒸发器 Κ还有稀溶液管路经新增溶液热交换器 Β与第一发生器 1连通，将第一发生 器 1有浓溶液管路经第一溶液泵 7和第一溶液热交换器 10与吸收-发生器 16连通调整为第一 发生器 1有浓溶液管路经第一溶液泵 7、 新增溶液热交换器 Β和第一溶液热交换器 10与吸收 -发生器 16连通， 将第一蒸发器 6有冷剂蒸汽通道与吸收-发生器 16连通调整为第一蒸发器 6有冷剂蒸汽通道与新增吸收-蒸发器 Κ连通， 第一冷凝器 4增设冷剂液管路经新增吸收-蒸 发器 Κ连通后新增吸收-蒸发器 Κ还有冷剂蒸汽通道与吸收-发生器 16连通。  1Structally, in the third type of absorption heat pump shown in Fig. 6, a new solution heat exchanger, a new absorption-evaporator and a new refrigerant liquid pump are added, and the absorption-generator 16 has a dilute solution tube. The first solution heat exchanger 10 is connected to the first generator 1 to be adjusted to be an absorption-generator 16 having a dilute solution line connected to the new absorption-evaporator via the first solution heat exchanger 10, and newly absorbed- The evaporator Κ and the dilute solution line are connected to the first generator 1 via the new solution heat exchanger, and the first generator 1 has a concentrated solution line through the first solution pump 7 and the first solution heat exchanger 10 Connected to the absorption-generator 16 to adjust to the first generator 1 having a concentrated solution line connected to the absorption-generator 16 via the first solution pump 7, the new solution heat exchanger, and the first solution heat exchanger 10, The first evaporator 6 has a refrigerant vapor passage connected to the absorption-generator 16 to be adjusted so that the first evaporator 6 has a refrigerant vapor passage communicating with the newly added absorption-evaporator, and the first condenser 4 is provided with a refrigerant liquid pipeline. Adding an absorption-evaporator after adding a new absorption-evaporator The refrigerant vapor passage is in communication with the absorption-generator 16.
②流程上，第一发生器 1的浓溶液经新增溶液热交换器 Β和第一溶液热交换器 10进入吸 收-发生器 16、吸收来自新增吸收-蒸发器 Κ的冷剂蒸汽并放热于流经吸收-发生器 16的溶液， 吸收-发生器 16的稀溶液经第一溶液热交换器 10进入新增吸收-蒸发器 K、吸收来自第一蒸发 器 6的冷剂蒸汽并放热于流经新增吸收-蒸发器 K的冷剂液， 新增吸收-蒸发器 K的稀溶液经 新增溶液热交换器 B进入第一发生器 1 ; 第一冷凝器 4的冷剂液分成两路——第一路经第一 冷剂液泵 8加压进入第一蒸发器 6、 吸收余热成冷剂蒸汽并向新增吸收-蒸发器 K提供， 第二 路经新增冷剂液泵 L加压后再流经新增吸收-蒸发器 K、 吸热成冷剂蒸汽并向吸收-发生器 16 提供， 形成单效-回热式 1. 5级第三类吸收式热泵。 2 In the process, the concentrated solution of the first generator 1 is introduced into the absorption-generator 16 via the newly added solution heat exchanger Β and the first solution heat exchanger 10, and the refrigerant vapor from the newly added absorption-evaporator is absorbed and discharged. Hot to the solution flowing through the absorption-generator 16 The dilute solution of the absorption-generator 16 enters the new absorption-evaporator K via the first solution heat exchanger 10, absorbs the refrigerant vapor from the first evaporator 6, and radiates heat through the new absorption-evaporator K. The refrigerant liquid, the dilute solution of the new absorption-evaporator K is added to the first generator 1 through the new solution heat exchanger B; the refrigerant liquid of the first condenser 4 is divided into two paths - the first pass through the first cold The liquid medium pump 8 is pressurized into the first evaporator 6, absorbs waste heat into refrigerant vapor and is supplied to the newly added absorption-evaporator K, and the second passage is pressurized by the newly added refrigerant liquid pump L, and then flows through the newly absorbed - The third type of absorption heat pump of the fifth stage is formed by the evaporator K, the endothermic refrigerant vapor, and supplied to the absorption-generator 16.
图 55所示的单效-回热式 1. 5级第三类吸收式热泵是这样实现的：  The single-effect-recovery type shown in Figure 55. The fifth-stage type III absorption heat pump is implemented as follows:
①结构上， 在图 6所示的第三类吸收式热泵中， 增加新增溶液热交换器、 新增溶液泵、 新增吸收 -蒸发器和新增冷剂液泵，将第一发生器 1有浓溶液管路经第一溶液泵 7和第一溶液 热交换器 10与吸收-发生器 16连通调整为第一发生器 1有浓溶液管路经第一溶液泵 7和第一 溶液热交换器 10与新增吸收-蒸发器 Κ连通，新增吸收-蒸发器 Κ还有稀溶液管路经新增溶液 泵 D和新增溶液热交换器 Β与吸收-发生器 16连通， 将吸收-发生器 16有稀溶液管路经第一 溶液热交换器 10与第一发生器 1连通调整为吸收-发生器 16有稀溶液管路经新增溶液热交换 器 Β和第一溶液热交换器 10与第一发生器 1连通， 将第一蒸发器 6有冷剂蒸汽通道与吸收- 发生器 16连通调整为第一蒸发器 6有冷剂蒸汽通道与新增吸收-蒸发器 Κ连通， 第一冷凝器 4增设冷剂液管路经新增吸收-蒸发器 Κ连通后新增吸收-蒸发器 Κ还有冷剂蒸汽通道与吸收- 发生器 16连通。  1Structure, in the third type of absorption heat pump shown in Figure 6, adding a new solution heat exchanger, a new solution pump, a new absorption-evaporator and a new refrigerant liquid pump, the first generator 1 The concentrated solution line is connected to the absorption-generator 16 via the first solution pump 7 and the first solution heat exchanger 10 to be adjusted to be the first generator 1 having the concentrated solution line passing through the first solution pump 7 and the first solution heat The exchanger 10 is connected to the newly added absorption-evaporator, and the new absorption-evaporator and the dilute solution line are connected to the absorption-generator 16 via the new solution pump D and the new solution heat exchanger, and will absorb - the generator 16 has a dilute solution line connected to the first generator 1 via the first solution heat exchanger 10 to be adjusted to absorb - the generator 16 has a dilute solution line through the new solution heat exchanger and the first solution is heat exchanged The device 10 is in communication with the first generator 1, and the first evaporator 6 has a refrigerant vapor passage connected to the absorption-generator 16 to be adjusted so that the first evaporator 6 has a refrigerant vapor passage connected to the new absorption-evaporator. The first condenser 4 adds a refrigerant liquid pipeline through a new absorption-evaporator After the addition, an absorption-evaporator is added, and a refrigerant vapor passage is connected to the absorption-generator 16.
②流程上，第一发生器 1的浓溶液经第一溶液泵 7和第一溶液热交换器 10进入新增吸收 -蒸发器 Κ、 吸收来自第一蒸发器 6的冷剂蒸汽并放热于流经新增吸收-蒸发器 Κ的冷剂液， 新增吸收-蒸发器 Κ的稀溶液经新增溶液泵 D和新增溶液热交换器 Β进入吸收-发生器 16、吸 收来自新增吸收-蒸发器 Κ的冷剂蒸汽并放热于流经吸收-发生器 16的溶液， 吸收-发生器 16 的稀溶液经新增溶液热交换器 Β和第一溶液热交换器 10进入第一发生器 1；第一冷凝器 4的 冷剂液分成两路——第一路经第一冷剂液泵 8加压进入第一蒸发器 6、 吸收余热成冷剂蒸汽 并向新增吸收-蒸发器 Κ提供， 第二路经新增冷剂液泵 L加压后再流经新增吸收-蒸发器 Κ、 吸热成冷剂蒸汽并向吸收-发生器 16提供， 形成单效-回热式 1. 5级第三类吸收式热泵。  2 In the process, the concentrated solution of the first generator 1 enters the new absorption-evaporator 经 via the first solution pump 7 and the first solution heat exchanger 10, absorbs the refrigerant vapor from the first evaporator 6, and radiates heat. Flow through the new absorption-evaporator 冷 coolant solution, add the absorption-evaporator 稀 dilute solution through the new solution pump D and the new solution heat exchanger Β into the absorption-generator 16 and absorb from the new absorption - the refrigerant vapor of the evaporator 并 and exothermic to the solution flowing through the absorption-generator 16, the dilute solution of the absorption-generator 16 is passed through the new solution heat exchanger Β and the first solution heat exchanger 10 into the first occurrence The refrigerant liquid of the first condenser 4 is divided into two paths - the first passage is pressurized by the first refrigerant liquid pump 8 into the first evaporator 6, and the residual heat is absorbed into the refrigerant vapor and is added to the absorption-evaporation Provided by the device, the second channel is pressurized by the newly added refrigerant liquid pump L, and then flows through the new absorption-evaporator, the heat is absorbed into the refrigerant vapor, and is supplied to the absorption-generator 16 to form a single-effect heat. Equation 1. Class 5 third type absorption heat pump.
本发明技术可以实现的效果——本发明所提出的第三类吸收式热泵， 具有如下的效果和 优势：  The effect that can be achieved by the technique of the present invention - the third type of absorption heat pump proposed by the present invention has the following effects and advantages:
1. 提出的第三类吸收式热泵， 丰富了低温余热用于溶液第一阶段发生过程、 高温驱动热 用于溶液第二阶段发生过程的第三类吸收式热泵， 可更好地实现热泵供热与用户需求之间的 相互匹配。  1. The proposed third type of absorption heat pump enriches the third type of absorption heat pump which is used for the first stage of the solution and the high temperature drive heat for the second stage of the solution, which can better realize the heat pump supply. The match between heat and user needs.
2. 提出的第三类吸收式热泵， 当驱动热介质与被加热介质之间温差较大时， 有利于发挥 高温驱动热的作用或降低对高温驱动热的温度要求。  2. The proposed third type of absorption heat pump, when the temperature difference between the driving heat medium and the heated medium is large, is beneficial to play the role of high temperature driving heat or reduce the temperature requirement for high temperature driving heat.
3. 利用本发明的第三类吸收式热泵， 在余热资源较为丰富、 尤其是存在以潜热为主的丰 富余热资源时， 可实现余热温度的进一步提升。  3. By using the third type of absorption heat pump of the present invention, the residual heat temperature can be further improved when the waste heat resources are abundant, especially when there is abundant waste heat resources mainly based on latent heat.
4. 能够适应多种工况， 扩大了吸收式热泵的温度工作区间， 扩展和丰富了吸收式热泵的 应用范围。  4. It can adapt to a variety of working conditions, expand the temperature working range of the absorption heat pump, and expand and enrich the application range of the absorption heat pump.

Claims

权 利 要 求 书 ― WO 2013/003982 PCT/CN2011/001118 Claims - WO 2013/003982 PCT/CN2011/001118
1. 第三类吸收式热泵， 是在由第一发生器、 第二发生器、 吸收器、 第一冷凝器、 第二 冷凝器、 蒸发器、 溶液泵、 冷剂液泵、 节流阀、 第一溶液热交换器和第二溶液热交换器组成 1. The third type of absorption heat pump is composed of a first generator, a second generator, an absorber, a first condenser, a second condenser, an evaporator, a solution pump, a refrigerant pump, a throttle valve, First solution heat exchanger and second solution heat exchanger
——第一发生器（1 )有浓溶液管路经溶液泵（7)、 第一溶液热交换器（10)和第二溶液热交 换器 （11 ) 与第二发生器 （2) 连通， 第二发生器 （2) 还有浓溶液管路经第二溶液热交换器- the first generator (1) has a concentrated solution line connected to the second generator (2) via the solution pump (7), the first solution heat exchanger (10) and the second solution heat exchanger (11), The second generator (2) also has a concentrated solution line through the second solution heat exchanger
( 11 ) 与吸收器 （3 ) 连通， 吸收器 （3) 还有稀溶液管路经第一溶液热交换器 （10) 与第一 发生器 （1 )连通， 第一发生器（1 )还有冷剂蒸汽通道与第一冷凝器（4)连通， 第一冷凝器(11) communicating with the absorber (3), the absorber (3) and the dilute solution line are connected to the first generator (1) via the first solution heat exchanger (10), and the first generator (1) is further a refrigerant vapor passage communicating with the first condenser (4), the first condenser
(4) 还有冷剂液管路经冷剂液泵 （8) 与蒸发器 （6) 连通， 第二发生器 （2) 还有冷剂蒸汽 通道与第二冷凝器（5 )连通， 第二冷凝器（5) 还有冷剂液管路经节流阀 （9 ) 与蒸发器（6) 连通， 蒸发器 （6) 还有冷剂蒸汽通道与吸收器 （3 ) 连通， 第一发生器 （1 ) 和蒸发器 （6) 还分别有余热介质管路与外部连通， 第二发生器（2 )还有驱动热介质管路与外部连通， 吸收 器（3)和第二冷凝器（5)还分别有被加热介质管路与外部连通， 第一冷凝器（4)还有冷却 介质管路与外部连通——的单效-单效第三类吸收式热泵中， 增加第三发生器、 第二吸收器、 第二溶液泵和第三溶液热交换器， 将吸收器（3)有稀溶液管路经第一溶液热交换器（10) 与 第一发生器 （1 ) 连通调整为吸收器 （3 ) 有稀溶液管路经第一溶液热交换器 （10) 与第二吸 收器 （13) 连通， 第二吸收器 （13 ) 还有稀溶液管路经第二溶液泵 （14) 和第三溶液热交换 器 （15) 与第一发生器 （1 ) 连通， 将第一发生器 （1 ) 有浓溶液管路经第一溶液泵 （7 )、 第 一溶液热交换器（10)和第二溶液热交换器（11 ) 与第二发生器（2 )连通调整为第一发生器(4) The coolant liquid line is connected to the evaporator (6) via the refrigerant liquid pump (8), and the second generator (2) and the refrigerant vapor passage are connected to the second condenser (5), The second condenser (5) and the refrigerant liquid pipeline are connected to the evaporator (6) via a throttle valve (9), and the evaporator (6) and the refrigerant vapor passage are connected to the absorber (3), the first occurrence occurs. The evaporator (1) and the evaporator (6) respectively have a residual heat medium line communicating with the outside, and the second generator (2) also drives the heat medium line to communicate with the outside, the absorber (3) and the second condenser ( 5) There is also a single-effect-single-effect third-class absorption heat pump in which the heated medium pipe is connected to the outside, and the first condenser (4) and the cooling medium pipe are connected to the outside, and the third occurrence occurs. , a second absorber, a second solution pump and a third solution heat exchanger, wherein the absorber (3) has a dilute solution line connected to the first generator (1) via the first solution heat exchanger (10) a dilute solution line for the absorber (3) is connected to the second absorber (13) via the first solution heat exchanger (10), the second absorption (13) further, the dilute solution line is connected to the first generator (1) via the second solution pump (14) and the third solution heat exchanger (15), and the first generator (1) has a concentrated solution line Adjusted to the first generator via the first solution pump (7), the first solution heat exchanger (10), and the second solution heat exchanger (11) in communication with the second generator (2)
( 1 ) 有浓溶液管路经第三溶液热交换器 （15) 与第三发生器 （12) 连通， 第三发生器 （12 ) 还有浓溶液管路经第一溶液泵 （7 )、 第一溶液热交换器 （10) 和第二溶液热交换器 （11 ) 与 第二发生器（2)连通， 第三发生器（12 )还分别有冷剂蒸汽通道与第二吸收器（13)连通和 有余热介质管路与外部连通， 第二吸收器 （13 ) 还有冷却介质管路与外部连通， 形成单效- 回热式单效第三类吸收式热泵。 (1) The concentrated solution line is connected to the third generator (12) via the third solution heat exchanger (15), and the third generator (12) and the concentrated solution line are passed through the first solution pump (7), The first solution heat exchanger (10) and the second solution heat exchanger (11) are in communication with the second generator (2), and the third generator (12) further has a refrigerant vapor channel and a second absorber (13) The communicating and residual heat medium pipeline communicates with the outside, and the second absorber (13) and the cooling medium pipeline communicate with the outside to form a single-effect-recovery single-effect third-class absorption heat pump.
2. 第三类吸收式热泵， 是在权利要求 1所提及的单效-单效第三类吸收式热泵中， 增加 第二溶液泵、 第三溶液热交换器、 吸收-发生器、 分汽室、 第三冷凝器、 第二蒸发器、 第二冷 剂液泵和第三冷剂液泵， 将吸收器（3)有稀溶液管路经第一溶液热交换器（10)与第一发生 器（1 )连通调整为吸收器（3)有稀溶液管路经第三溶液热交换器（15 )与吸收-发生器（16) 连通， 吸收-发生器 （16) 还有稀溶液管路经第一溶液热交换器 （10) 与第一发生器 （1 ) 连 通， 将第一发生器（1 )有浓溶液管路经第一溶液泵（7)、 第一溶液热交换器（10)和第二溶 液热交换器 （11 ) 与第二发生器 （2) 连通调整为第一发生器 （1 ) 有浓溶液管路经第一溶液 泵 （7)、 第一溶液热交换器 （10) 和吸收-发生器 （16) 与分汽室 （17) 连通， 分汽室 （17 ) 还有浓溶液管路经第二溶液泵（14)、 第三溶液热交换器（15)和第二溶液热交换器（11 )与 第二发生器（2 )连通， 吸收-发生器 （16)或还有被加热介质管路与外部连通， 分汽室 （17 ) 还有冷剂蒸汽通道与第三冷凝器 （18) 连通， 第三冷凝器 （18 ) 还有冷剂液管路经第二冷剂 液泵（20)与第二蒸发器（19 )连通， 第一冷凝器（4)增设冷剂液管路经第三冷剂液泵与第 二蒸发器 （19)连通， 第二蒸发器（19)还有冷剂蒸汽通道与吸收-发生器 （16)连通， 第三 冷凝器 （18) 还有冷却介质管路与外部连通， 第二蒸发器 （19 ) 还有余热介质管路与外部连 通， 形成单效 -回热式单效第三类吸收式热泵； 其中， 吸收 -发生器无被加热介质管路与外部 连通时， 可取消第一冷凝器经第三冷剂液泵与第二蒸发器 （19 ) 连通的冷剂液管路。  2. The third type of absorption heat pump is a single-effect-single-effect third-type absorption heat pump as claimed in claim 1, adding a second solution pump, a third solution heat exchanger, an absorption-generator, and a minute a steam chamber, a third condenser, a second evaporator, a second refrigerant liquid pump, and a third refrigerant liquid pump, and the absorber (3) has a dilute solution line through the first solution heat exchanger (10) and A generator (1) is connected to the absorber (3) has a dilute solution line connected to the absorption-generator (16) via the third solution heat exchanger (15), and the absorption-generator (16) and the dilute solution The pipeline is connected to the first generator (1) via the first solution heat exchanger (10), and the first generator (1) has a concentrated solution pipeline through the first solution pump (7), the first solution heat exchanger (10) and the second solution heat exchanger (11) is connected to the second generator (2) to be adjusted to be the first generator (1) having a concentrated solution line through the first solution pump (7), the first solution heat exchange The (10) and absorption-generator (16) are in communication with the steam distribution chamber (17), the steam distribution chamber (17) and the concentrated solution line are passed through the second solution pump (14). The third solution heat exchanger (15) and the second solution heat exchanger (11) are in communication with the second generator (2), and the absorption-generator (16) or the heated medium line is in communication with the outside. The steam dividing chamber (17) further has a refrigerant vapor passage communicating with the third condenser (18), and the third condenser (18) and the refrigerant liquid pipeline passing through the second refrigerant liquid pump (20) and the second evaporation The first condenser (4) is provided with a refrigerant liquid pipeline connected to the second evaporator (19) via a third refrigerant liquid pump, and the second evaporator (19) has a refrigerant vapor passage and The absorption-generator (16) is connected, the third condenser (18) and the cooling medium line are connected to the outside, and the second evaporator (19) and the residual heat medium line are connected to the outside to form a single-effect-recovery type. Single-effect third-type absorption heat pump; wherein, when the absorption-generator is not connected to the outside by the heating medium pipeline, the cold connection between the first condenser and the second evaporator (19) may be cancelled Liquid line.
3. 第三类吸收式热泵， 是在权利要求 1所提及的单效-单效第三类吸收式热泵中， 增加 第二溶液泵、 第三溶液热交换器、 吸收-发生器、 分汽室、 第三冷凝器、 第二冷剂液泵和第三 权 利 要 求 书 3. The third type of absorption heat pump is a single-effect-single-effect third-type absorption heat pump as claimed in claim 1, adding a second solution pump, a third solution heat exchanger, an absorption-generator, and a minute Steam chamber, third condenser, second refrigerant pump and third Claim
― W0 2013/003982 PCT/CN2011/001118 溶液泵， 将吸收器 （3) 有稀溶液管路经第一溶液热交换器 （10) 与第一发生器 （1 ) 连通调 整为吸收器 （3) 有稀溶液管路经第三溶液泵 （21 ) 和第三溶液热交换器 （15) 与吸收 -发生 器（16)连通， 吸收-发生器（16)还有稀溶液管路经第一溶液热交换器 （10) 与第一发生器 ― W0 2013/003982 PCT/CN2011/001118 solution pump, adjusting the absorber (3) dilute solution line through the first solution heat exchanger (10) to the first generator (1) to adjust to the absorber (3) The dilute solution line is connected to the absorption-generator (16) via the third solution pump (21) and the third solution heat exchanger (15), and the absorption-generator (16) and the dilute solution line are passed through the first solution. Heat exchanger (10) and first generator
( I ) 连通， 将第一发生器 （1 ) 有浓溶液管路经第一溶液泵 （7 )、 第一溶液热交换器 （10) 和第二溶液热交换器 （11 ) 与第二发生器 （2) 连通调整为第一发生器 （1 ) 有浓溶液管路经 第一溶液泵 （7)、 第一溶液热交换器（10)和吸收-发生器 （16) 与分汽室 （17)连通， 分汽 室（17)还有浓溶液管路经第二溶液泵（14)、 第三溶液热交换器（15)和第二溶液热交换器(I) communicating, the first generator (1) has a concentrated solution line through the first solution pump (7), the first solution heat exchanger (10) and the second solution heat exchanger (11) and the second occurrence (2) Connected to the first generator (1) with a concentrated solution line through the first solution pump (7), the first solution heat exchanger (10) and the absorption-generator (16) and the steam distribution chamber ( 17) connected, the steam dividing chamber (17) and the concentrated solution pipeline pass through the second solution pump (14), the third solution heat exchanger (15) and the second solution heat exchanger
( I I ) 与第二发生器 （2 ) 连通， 吸收-发生器 （16) 或还有被加热介质管路与外部连通， 分 汽室 （17) 还有冷剂蒸汽通道与第三冷凝器 （18) 连通， 第三冷凝器 （18) 还有冷剂液管路 经第二冷剂液泵（20)与蒸发器（6)连通，蒸发器（6)增设冷剂蒸汽通道与吸收-发生器（16) 连通， 第三冷凝器（18)还有冷却介质管路与外部连通， 形成单效 -回热式单效第三类吸收式 热泵。 (II) in communication with the second generator (2), the absorption-generator (16) or the heated medium line is in communication with the outside, and the steam distribution chamber (17) has a refrigerant vapor passage and a third condenser ( 18) Connected, the third condenser (18) and the refrigerant liquid line are connected to the evaporator (6) via the second refrigerant liquid pump (20), and the evaporator (6) is provided with a refrigerant vapor channel and absorption-occurrence The (16) is connected, and the third condenser (18) and the cooling medium line communicate with the outside to form a single-effect-recovery single-effect third-type absorption heat pump.
4. 第三类吸收式热泵， 是在权利要求 1所提及的单效-单效第三类吸收式热泵中， 增加 第二溶液泵、 第三溶液热交换器、 吸收-发生器、 分汽室、 第三冷凝器、 第二蒸发器、 第二冷 剂液泵或第二节流阀， 将第一发生器（1 )有浓溶液管路经第一溶液泵（7)、 第一溶液热交换 器 （10) 和第二溶液热交换器 （11 ) 与第二发生器 （2) 连通调整为第一发生器 （1 ) 有浓溶 液管路经第一溶液泵 （7)和第一溶液热交换器（10) 与吸收-发生器（16)连通， 吸收 -发生 器（16)还有稀溶液管路经第一溶液热交换器（10) 与第一发生器 （1 ) 连通， 将吸收器 （3) 有稀溶液管路经第一溶液热交换器 （10) 与第一发生器 （1 ) 连通调整为吸收器 （3) 有稀溶 液管路经第三溶液热交换器 （15) 和吸收-发生器 （16) 与分汽室 （17 ) 连通， 分汽室 （17) 还有浓溶液管路经第二溶液泵（14 )、 第三溶液热交换器（15 )和第二溶液热交换器（11 ) 与 第二发生器（2)连通， 将第一冷凝器（4) 有冷剂液管路经第一冷剂液泵 （8 ) 与第一蒸发器 4. The third type of absorption heat pump is a single-effect-single-effect third-type absorption heat pump as claimed in claim 1, adding a second solution pump, a third solution heat exchanger, an absorption-generator, and a minute a steam chamber, a third condenser, a second evaporator, a second refrigerant liquid pump or a second throttle valve, the first generator (1) has a concentrated solution line through the first solution pump (7), the first The solution heat exchanger (10) and the second solution heat exchanger (11) are connected to the second generator (2) to be adjusted to be the first generator (1) having a concentrated solution line through the first solution pump (7) and a solution heat exchanger (10) is in communication with the absorption-generator (16), and the absorption-generator (16) and the dilute solution line are connected to the first generator (1) via the first solution heat exchanger (10) , the absorber (3) has a dilute solution line connected to the first generator (1) through the first solution heat exchanger (10) to adjust the absorber (3) has a dilute solution line through the third solution heat exchanger (15) and the absorption-generator (16) is in communication with the steam distribution chamber (17), the steam distribution chamber (17) and the concentrated solution line are passed through the second solution pump 14), the third solution heat exchanger (15) and the second solution heat exchanger (11) are in communication with the second generator (2), and the first condenser (4) has a refrigerant liquid line through the first cold Liquid liquid pump (8) and first evaporator
(6)连通调整为第一冷凝器（4 )有冷剂液管路经第一冷剂液泵（8 ) 与第二蒸发器（19)连 通， 第二蒸发器 （19)还有冷剂蒸汽通道与吸收-发生器 （16) 连通， 分汽室 （17)还有冷剂 蒸汽通道与第三冷凝器（18)连通， 第三冷凝器（18 )还有冷剂液管路经第二冷剂液泵（20) 与第一蒸发器（6)连通、 或第三冷凝器（18)还有冷剂液管路经第二节流阀 （22) 与第一冷 凝器 （4) 连通， 吸收-发生器 （16) 或还有被加热介质管路与外部连通， 第三冷凝器 （18) 还有冷却介质管路与外部连通， 第二蒸发器（19)还有余热介质管路与外部连通， 形成单效- 回热式单效第三类吸收式热泵； 其中， ①无第二蒸发器时， 第一冷凝器（4)有冷剂液管路经 第一冷剂液泵 （8) 与第一蒸发器 （6) 连通， 第一蒸发器 （6) 增设冷剂蒸汽通道与吸收-发 生器（16)连通； ②无第三冷凝器时， 分汽室（17)有冷剂蒸汽通道与第一冷凝器（4)连通， 第一冷凝器 （4) 增设冷剂液管路经第二冷剂液泵 （20) 与第一蒸发器 （6 ) 连通。 (6) The communication is adjusted to be that the first condenser (4) has a refrigerant liquid pipeline connected to the second evaporator (19) via the first refrigerant liquid pump (8), and the second evaporator (19) has a refrigerant. The steam passage is connected to the absorption-generator (16), the steam distribution chamber (17) and the refrigerant vapor passage are in communication with the third condenser (18), and the third condenser (18) and the refrigerant liquid pipeline are The second refrigerant liquid pump (20) is in communication with the first evaporator (6), or the third condenser (18) and the refrigerant liquid line are passed through the second throttle valve (22) and the first condenser (4) Connected, the absorption-generator (16) or the heated medium line is in communication with the outside, the third condenser (18) and the cooling medium line are in communication with the outside, and the second evaporator (19) and the residual heat medium tube The road is connected to the outside to form a single-effect-recovery single-effect third-type absorption heat pump; wherein, when there is no second evaporator, the first condenser (4) has a refrigerant liquid pipeline through the first refrigerant liquid The pump (8) is in communication with the first evaporator (6), the first evaporator (6) is provided with a refrigerant vapor passage communicating with the absorption-generator (16); 2 when there is no third condenser, The steam chamber (17) has a refrigerant vapor passage communicating with the first condenser (4), and the first condenser (4) is provided with a refrigerant liquid pipeline via the second refrigerant liquid pump (20) and the first evaporator (6) ) Connected.
5. 第三类吸收式热泵， 是在权利要求 1所提及的单效-单效第三类吸收式热泵中， 增加 第三发生器、 第三溶液热交换器和第二节流阀， 第一发生器 （1 ) 经第一溶液泵 （7 ) 和第一 溶液热交换器（10)之后增设浓溶液管路并再经第三溶液热交换器（15 )与第三发生器（12) 连通， 第三发生器 （12)还有浓溶液管路经第三溶液热交换器 （15) 与吸收器（3)连通， 将 第二发生器（2)有冷剂蒸汽通道与第二冷凝器（5)连通调整为第二发生器（2)有冷剂蒸汽 通道与第三发生器 （12) 连通后第三发生器 （12) 再有冷剂液管路经第二节流阀 （22 ) 与第 二冷凝器（5)连通——第二发生器产生的冷剂蒸汽作为第三发生器的驱动热介质， 第三发生 器 （12) 还有冷剂蒸汽通道与第二冷凝器 （5 ) 连通， 形成双效 -单效第三类吸收式热泵。 权 利 要 求 书 5. A third type of absorption heat pump, in the single-effect-single-effect third-type absorption heat pump mentioned in claim 1, adding a third generator, a third solution heat exchanger and a second throttle valve, The first generator (1) is further provided with a concentrated solution line after passing through the first solution pump (7) and the first solution heat exchanger (10) and then through the third solution heat exchanger (15) and the third generator (12) Connected, the third generator (12) and the concentrated solution line communicate with the absorber (3) via the third solution heat exchanger (15), and the second generator (2) has a refrigerant vapor channel and a second The condenser (5) is adjusted to be connected to the second generator (2), the refrigerant vapor passage is connected to the third generator (12), and the third generator (12) is further provided with the refrigerant liquid pipeline through the second throttle valve. (22) communicating with the second condenser (5) - the refrigerant vapor generated by the second generator acts as a driving heat medium for the third generator, and the third generator (12) also has a refrigerant vapor passage and a second condensation The device (5) is connected to form a double-effect-single-effect third-type absorption heat pump. Claim
― WO 2013/003982 PCT/CN2011/001118  ― WO 2013/003982 PCT/CN2011/001118
6. 第三类吸收式热泵， 是在权利要求 1所提及的单效-单效第三类吸收式热泵中， 增加 第三发生器、第三溶液热交换器和第二节流阀，将第一发生器（1)有浓溶液管路经溶液泵（7)、 第一溶液热交换器 （10)和第二溶液热交换器（11) 与第二发生器（2)连通调整为第一发生 器 （1) 有浓溶液管路经溶液泵 （7)、 第一溶液热交换器 （10)、 第二溶液热交换器 （11) 和 第三溶液热交换器 （15) 与第二发生器 （2) 连通， 将第二发生器 （2) 有浓溶液管路经第二 溶液热交换器 （11) 与吸收器 （3) 连通调整为第二发生器 （2) 有浓溶液管路经第三溶液热 交换器 （15) 与第三发生器 （12) 连通， 第三发生器 （12) 还有浓溶液管路经第二溶液热交 换器（11) 与吸收器 （3)连通， 将第二发生器（2)有冷剂蒸汽通道与第二冷凝器（5)连通 调整为第二发生器 （2)有冷剂蒸汽通道与第三发生器（12)连通后第三发生器（12) 再有冷 剂液管路经第二节流阔 (22)与第二冷凝器（5)连通——第二发生器产生的冷剂蒸汽作为第 三发生器的驱动热介质， 第三发生器（12)还有冷剂蒸汽通道与第二冷凝器（5)连通， 形成 双效-单效第三类吸收式热泵。  6. A third type of absorption heat pump, in the single-effect-single-effect third-type absorption heat pump mentioned in claim 1, adding a third generator, a third solution heat exchanger and a second throttle valve, Adjusting the first generator (1) having a concentrated solution line through the solution pump (7), the first solution heat exchanger (10), and the second solution heat exchanger (11) to the second generator (2) The first generator (1) has a concentrated solution line through the solution pump (7), the first solution heat exchanger (10), the second solution heat exchanger (11), and the third solution heat exchanger (15) and The second generator (2) is connected, and the second generator (2) has a concentrated solution line connected to the absorber (3) through the second solution heat exchanger (11) to be adjusted to a second generator (2) having a concentrated solution The pipeline is connected to the third generator (12) via the third solution heat exchanger (15), and the third generator (12) and the concentrated solution pipeline are passed through the second solution heat exchanger (11) and the absorber (3) Connected, the second generator (2) has a refrigerant vapor passage connected to the second condenser (5) to be adjusted to a second generator (2) having a refrigerant vapor passage After communicating with the third generator (12), the third generator (12) has a refrigerant liquid line connected to the second condenser (5) via the second section (22) - the second generator The refrigerant vapor acts as a driving heat medium for the third generator, and the third generator (12) and the refrigerant vapor passage communicate with the second condenser (5) to form a double-effect-single-effect third-type absorption heat pump.
7. 第三类吸收式热泵， 是在权利要求 6所述的第三类吸收式热泵中， 增加溶液节流阔， 将第一发生器 （1) 有浓溶液管路经第一溶液泵 （7)、 第一溶液热交换器 （10)、 第二溶液热 交换器 （11) 和第三溶液热交换器 （15) 与第二发生器 （2) 连通调整为第一发生器 （1) 有 浓溶液管路经第一溶液泵（7)、 第一溶液热交换器（10)、 第二溶液热交换器（11)之后分别 再经溶液节流阀与第三发生器 （12) 连通和再经第三溶液热交换器 （15) 与第二发生器 （2) 连通， 形成双效 -单效第三类吸收式热泵。  7. A third type of absorption heat pump, which is characterized in that in the third type of absorption heat pump according to claim 6, the solution is increased in throttling, and the first generator (1) has a concentrated solution line through the first solution pump ( 7), the first solution heat exchanger (10), the second solution heat exchanger (11) and the third solution heat exchanger (15) are connected to the second generator (2) to be adjusted to the first generator (1) The concentrated solution pipeline is connected to the third generator (12) through the solution throttle valve through the first solution pump (7), the first solution heat exchanger (10), and the second solution heat exchanger (11), respectively. And communicating with the second generator (2) via the third solution heat exchanger (15) to form a double-effect-single-effect third type absorption heat pump.
8. 第三类吸收式热泵， 是在权利要求 1所提及的单效-单效第三类吸收式热泵中， 增加 第三发生器、 第三溶液热交换器、 第二溶液泵和第二节流阀， 将第一发生器（1)有浓溶液管 路经第一溶液泵（7)、第一溶液热交换器（10)和第二溶液热交换器（11)与第二发生器（2) 连通调整为第一发生器（1)有浓溶液管路经第一溶液泵（7)、 第一溶液热交换器（10)和第 二溶液热交换器 （11) 与第三发生器 （12) 连通， 第三发生器 （12) 还有浓溶液管路经第二 溶液泵 （14) 和第三溶液热交换器 （15) 与第二发生器 （2) 连通， 将第二发生器 （2) 有浓 溶液管路经第二溶液热交换器 （11) 与吸收器 （3) 连通调整为第二发生器 （2) 有浓溶液管 路经第三溶液热交换器（15)和第二溶液热交换器 （11) 与吸收器 （3)连通， 将第二发生器 8. A third type of absorption heat pump, which is a single-effect-single-effect third-type absorption heat pump as claimed in claim 1, adding a third generator, a third solution heat exchanger, a second solution pump, and a a two-way valve, the first generator (1) has a concentrated solution pipeline through the first solution pump (7), the first solution heat exchanger (10) and the second solution heat exchanger (11) and the second occurs (2) Connected to the first generator (1) with a concentrated solution line through the first solution pump (7), the first solution heat exchanger (10) and the second solution heat exchanger (11) and the third The generator (12) is connected, the third generator (12) and the concentrated solution line are connected to the second generator (2) via the second solution pump (14) and the third solution heat exchanger (15), The second generator (2) has a concentrated solution line connected to the absorber (3) via the second solution heat exchanger (11) to be adjusted to a second generator (2) having a concentrated solution line through the third solution heat exchanger ( 15) and the second solution heat exchanger (11) is in communication with the absorber (3), the second generator
(2)有冷剂蒸汽通道与第二冷凝器（5)连通调整为第二发生器（2)有冷剂蒸汽通道与第三 发生器（12)连通后第三发生器（12)再有冷剂液管路经第二节流阀（22)与第二冷凝器（5) 连通——第二发生器产生的冷剂蒸汽作为第三发生器的驱动热介质， 第三发生器 （12) 还有 冷剂蒸汽通道与第二冷凝器 （5) 连通， 形成双效 -单效第三类吸收式热泵。 (2) The refrigerant flow channel is connected to the second condenser (5) to be adjusted to be the second generator (2). The refrigerant flow channel is connected to the third generator (12), and the third generator (12) is further The refrigerant liquid line is connected to the second condenser (5) via the second throttle valve (22) - the refrigerant vapor generated by the second generator is used as the driving heat medium of the third generator, and the third generator (12) There is also a refrigerant vapor passage that communicates with the second condenser (5) to form a double-effect-single-effect third-type absorption heat pump.
9. 第三类吸收式热泵， 是在权利要求 8所述的第三类吸收式热泵中， 增加溶液节流阀， 将第一发生器（1)有浓溶液管路经第一溶液泵 （7)、 第一溶液热交换器（10)和第二溶液热 交换器（11)与第三发生器（12)连通调整为第一发生器（1)有浓溶液管路经第一溶液泵（7)、 第一溶液热交换器（10)和第二溶液热交换器（11)之后分别直接与第二发生器（2)连通和 再经溶液节流阀与第三发生器 （12) 连通， 形成双效 -单效第三类吸收式热泵。  9. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 8, wherein the solution throttle valve is added, and the first generator (1) has a concentrated solution line through the first solution pump ( 7), the first solution heat exchanger (10) and the second solution heat exchanger (11) are connected to the third generator (12) to be adjusted to be the first generator (1) having a concentrated solution line through the first solution pump (7), the first solution heat exchanger (10) and the second solution heat exchanger (11) are directly connected to the second generator (2) and then passed through the solution throttle valve and the third generator (12) Connected to form a double-effect-single-effect third-class absorption heat pump.
10. 第三类吸收式热泵，是在权利要求 5所述的第三类吸收式热泵中，增加第四发生器、 第四溶液热交换器和第三节流阀， 第一溶液热交换器 （10) 增设浓溶液管路经第四溶液热交 换器 （24) 与第四发生器 （23) 连通， 第四发生器 （23) 还有浓溶液管路经第四溶液热交换 器 （24) 与吸收器 （3) 连通， 将第三发生器 （12) 有冷剂蒸汽通道与第二冷凝器 （5) 连通 调整为第三发生器 （12) 有冷剂蒸汽通道与第四发生器 （23) 连通后第四发生器 （23) 再有 权 利 要 求 书 10. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 5, adding a fourth generator, a fourth solution heat exchanger and a third throttle valve, the first solution heat exchanger (10) The concentrated solution line is connected to the fourth generator (23) via the fourth solution heat exchanger (24), and the fourth generator (23) and the concentrated solution line are passed through the fourth solution heat exchanger (24). Connected to the absorber (3), the third generator (12) has a refrigerant vapor passage connected to the second condenser (5) to be adjusted to a third generator (12) having a refrigerant vapor passage and a fourth generator (23) After connecting, the fourth generator (23) Claim
― WO 2013/003982 PCT/CN2011/001118 冷剂液管路经第三节流阔 (25) 与第二冷凝器（5)连通， 第四发生器 （23)还有冷剂蒸汽通 道与第二冷凝器 （5) 连通， 形成三效 -单效第三类吸收式热泵。  ― WO 2013/003982 PCT/CN2011/001118 The refrigerant liquid line is connected to the second condenser (5) via the third section (25), and the fourth generator (23) also has the refrigerant vapor passage and the second The condenser (5) is connected to form a three-effect-single-effect third-type absorption heat pump.
11. 第三类吸收式热泵，是在权利要求 6所述的第三类吸收式热泵中，增加第四发生器、 第四溶液热交换器和第三节流阀， 将第二溶液热交换器 （11) 有浓溶液管路经第三溶液热交 换器（15) 与第二发生器（2)连通调整为第二溶液热交换器（11) 有浓溶液管路经第四溶液 热交换器 （24)和第三溶液热交换器 （15) 与第二发生器（2)连通， 将第三发生器 （12) 有 浓溶液管路经第二溶液热交换器（11) 与吸收器（3)连通调整为第三发生器（12)有浓溶液 管路经第第四溶液热交换器 （24) 与第四发生器 （23) 连通， 第四发生器 （23) 还有浓溶液 管路经第二溶液热交换器（11) 与吸收器（3)连通， 将第三发生器（12)有冷剂蒸汽通道与 第二冷凝器（5)连通调整为第三发生器（12)有冷剂蒸汽通道与第四发生器（23)连通后第 四发生器（23)再有冷剂液管路经第三节流阀（25)与第二冷凝器（5)连通，第四发生器（23) 还有冷剂蒸汽通道与第二冷凝器 （5) 连通， 形成三效-单效第三类吸收式热泵。  11. A third type of absorption heat pump, wherein in the third type of absorption heat pump according to claim 6, the fourth generator, the fourth solution heat exchanger and the third throttle valve are added, and the second solution is heat exchanged. The (11) concentrated solution line is connected to the second generator (2) via the third solution heat exchanger (15) to be adjusted to the second solution heat exchanger (11). The concentrated solution line is subjected to the fourth solution heat exchange. The second solution (24) and the third solution heat exchanger (15) are in communication with the second generator (2), and the third generator (12) has a concentrated solution line through the second solution heat exchanger (11) and the absorber (3) The communication is adjusted to be a third generator (12) having a concentrated solution line connected to the fourth generator (23) via the fourth solution heat exchanger (24), and the fourth generator (23) having a concentrated solution The pipeline is connected to the absorber (3) via the second solution heat exchanger (11), and the third generator (12) has a refrigerant vapor passage connected to the second condenser (5) to be adjusted to a third generator (12). After the refrigerant vapor passage is connected with the fourth generator (23), the fourth generator (23) has a refrigerant liquid pipeline through the third throttle valve (25) and (5) communicating two condensers, a fourth generator (23), the refrigerant vapor channel and a second condenser (5) communicating, forming three-way - a third single effect absorption heat pump.
12. 第三类吸收式热泵，是在权利要求 8所述的第三类吸收式热泵中，增加第四发生器、 第四溶液热交换器、 第三节流阀和第三溶液泵， 将第二溶液热交换器 （11) 有浓溶液管路与 第三发生器 （12) 连通调整为第二溶液热交换器 （11) 有浓溶液管路与第四发生器 （23) 连 通， 第四发生器 （23) 还有浓溶液管路经第三溶液泵 （21) 和第四溶液热交换器 （24) 与第 三发生器（12)连通， 将第二发生器（2)有浓溶液管路经第三溶液热交换器（15)和第二溶 液热交换器 （11) 与吸收器 （3) 连通调整为第二发生器 （2) 有浓溶液管路经第三溶液热交 换器 （15)、 第四溶液热交换器 （24) 和第二溶液热交换器 （11) 与吸收器 （3) 连通， 将第 三发生器（12)有冷剂蒸汽通道与第二冷凝器（5)连通调整为第三发生器（12)有冷剂蒸汽 通道与第四发生器 （23) 连通后第四发生器 （23) 再有冷剂液管路经第三节流阀 （25) 与第 二冷凝器 （5) 连通， 第四发生器 （23) 还有冷剂蒸汽通道与第二冷凝器 （5) 连通， 形成三 效 -单效第三类吸收式热泵。  12. The third type of absorption heat pump, in the third type of absorption heat pump according to claim 8, adding a fourth generator, a fourth solution heat exchanger, a third throttle valve and a third solution pump, The second solution heat exchanger (11) has a concentrated solution line connected to the third generator (12) and is adjusted to be a second solution heat exchanger (11). The concentrated solution line is connected to the fourth generator (23), The fourth generator (23) further has a concentrated solution line connected to the third generator (12) via the third solution pump (21) and the fourth solution heat exchanger (24), and the second generator (2) is thick The solution line is connected to the absorber (3) via the third solution heat exchanger (15) and the second solution heat exchanger (11) to be adjusted to the second generator (2). The concentrated solution line is subjected to the third solution heat exchange. The (15), the fourth solution heat exchanger (24) and the second solution heat exchanger (11) are in communication with the absorber (3), and the third generator (12) has a refrigerant vapor passage and a second condenser (5) The communication is adjusted to a third generator (12) having a refrigerant vapor passage connected to the fourth generator (23) and a fourth generator 23) The refrigerant liquid line is connected to the second condenser (5) via the third throttle valve (25), and the fourth generator (23) and the refrigerant vapor channel are connected to the second condenser (5). , forming a three-effect-single-effect third-class absorption heat pump.
13. 第三类吸收式热泵，是在权利要求 1所述的第三类吸收式热泵中，增加第四发生器、 第四溶液热交换器和第二节流阀， 第一发生器 （1) 经第一溶液泵 （7) 和第一溶液热交换器 13. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 1, wherein the fourth generator, the fourth solution heat exchanger and the second throttle valve are added, the first generator (1) Passing the first solution pump (7) and the first solution heat exchanger
(10) 之后增设浓溶液管路并再经第四溶液热交换器 （24) 与第四发生器 （23) 连通， 第四 发生器（23) 还有浓溶液管路经第四溶液热交换器（24) 与吸收器（3) 连通， 将第二发生器(10) After adding a concentrated solution line and communicating with the fourth generator (23) via the fourth solution heat exchanger (24), the fourth generator (23) and the concentrated solution line are subjected to the fourth solution heat exchange. (24) is connected to the absorber (3), and the second generator is
(2)有冷剂蒸汽通道与第二冷凝器（5)连通调整为第二发生器（2)有冷剂蒸汽通道与第四 发生器（23)连通后第四发生器（23)再有冷剂液管路经第二节流阀（22)与第二冷凝器（5) 连通——第二发生器产生的冷剂蒸汽作为第四发生器的驱动热介质， 第四发生器 （23) 还有 冷剂蒸汽通道与第二冷凝器 （5) 连通， 形成双效-回热式单效第三类吸收式热泵。 (2) The refrigerant having the refrigerant vapor passage and the second condenser (5) is adjusted to be the second generator (2), and the fourth generator (23) is further connected to the fourth generator (23). The refrigerant liquid line is connected to the second condenser (5) via the second throttle valve (22) - the refrigerant vapor generated by the second generator is used as the driving heat medium of the fourth generator, and the fourth generator (23) There is also a refrigerant vapor passage communicating with the second condenser (5) to form a double-effect regenerative single-effect third-stage absorption heat pump.
14. 第三类吸收式热泵，是在权利要求 1所述的第三类吸收式热泵中，增加第四发生器、 第四溶液热交换器和第二节流阀， 将第一发生器（1)有浓溶液管路经第一溶液泵（7)、 第一 溶液热交换器（10)和第二溶液热交换器（11)与第二发生器（2)连通调整为第一发生器（1) 有浓溶液管路经第一溶液泵（7)、 第一溶液热交换器（10)、 第二溶液热交换器（11)和第四 溶液热交换器 （24) 与第二发生器 （2) 连通， 将第二发生器 （2) 有浓溶液管路经第二溶液 热交换器 （11) 与吸收器 （3) 连通调整为第二发生器 （2) 有浓溶液管路经第四溶液热交换 器 （24) 与第四发生器 （23) 连通， 第四发生器 （23) 还有浓溶液管路经第二溶液热交换器 14. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 1, wherein the fourth generator, the fourth solution heat exchanger and the second throttle valve are added, and the first generator is 1) The concentrated solution line is connected to the second generator (2) via the first solution pump (7), the first solution heat exchanger (10) and the second solution heat exchanger (11) to be adjusted to the first generator (1) The concentrated solution line passes through the first solution pump (7), the first solution heat exchanger (10), the second solution heat exchanger (11), and the fourth solution heat exchanger (24) with the second occurrence The (2) is connected, and the second generator (2) has a concentrated solution line connected to the absorber (3) through the second solution heat exchanger (11) to be adjusted to a second generator (2) having a concentrated solution line The fourth solution heat exchanger (24) is in communication with the fourth generator (23), and the fourth generator (23) has a concentrated solution line through the second solution heat exchanger.
(11) 与吸收器 （3)连通， 将第二发生器（2)有冷剂蒸汽通道与第二冷凝器 （5)连通调整 为第二发生器（2)有冷剂蒸汽通道与第四发生器（23)连通后第四发生器（23)再有冷剂液 权 利 要 求 书 (11) communicating with the absorber (3), connecting the second generator (2) with the refrigerant vapor passage and the second condenser (5) to adjust to the second generator (2) having the refrigerant vapor passage and the fourth After the generator (23) is connected, the fourth generator (23) has a refrigerant liquid Claim
― WO 2013/003982 PCT/CN2011/001118 管路经第二节流阀 （22)与第二冷凝器（5)连通——第二发生器产生的冷剂蒸汽作为第四发 生器的驱动热介质， 第四发生器（24)还有冷剂蒸汽通道与第二冷凝器（5 )连通， 形成双效 -回热式单效第三类吸收式热泵。  ― WO 2013/003982 PCT/CN2011/001118 The pipeline is connected to the second condenser (5) via the second throttle valve (22) - the refrigerant vapor generated by the second generator acts as the driving heat medium for the fourth generator The fourth generator (24) also has a refrigerant vapor passage communicating with the second condenser (5) to form a double-effect-recovery single-effect third-type absorption heat pump.
15. 第三类吸收式热泵， 是在权利要求 14所述的第三类吸收式热泵中， 增加溶液节流 阀， 将第一发生器 （1 ) 有浓溶液管路经第一溶液泵 （7)、 第一溶液热交换器 （10)、 第二溶 液热交换器（11 )和第四溶液热交换器（24) 与第二发生器（2)连通调整为第一发生器（1 ) 有浓溶液管路经第一溶液泵 （7)、 第一溶液热交换器（10)、 第二溶液热交换器（11 )之后分 别再经溶液节流阀与第四发生器（23)连通和再经第四溶液热交换器（24)与第二发生器（2) 连通， 形成双效 -回热式单效第三类吸收式热泵。  15. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 14, wherein the solution throttle valve is added, and the first generator (1) has a concentrated solution line through the first solution pump ( 7), the first solution heat exchanger (10), the second solution heat exchanger (11), and the fourth solution heat exchanger (24) are connected to the second generator (2) to be adjusted to the first generator (1) The concentrated solution pipeline is connected to the fourth generator (23) via the solution throttle valve through the first solution pump (7), the first solution heat exchanger (10), and the second solution heat exchanger (11), respectively. And communicating with the second generator (2) via the fourth solution heat exchanger (24) to form a double-effect-recovery single-effect third-type absorption heat pump.
16. 第三类吸收式热泵，是在权利要求 1所述的第三类吸收式热泵中，增加第四发生器、 第四溶液热交换器、 第二节流阀和第三溶液泵， 将第一发生器（1 )有浓溶液管路经第一溶液 泵 （7 )、 第一溶液热交换器 （10)和第二溶液热交换器 （11 ) 与第二发生器（2)连通调整为 第一发生器（1 )有浓溶液管路经第一溶液泵 （7 )、 第一溶液热交换器 （10)和第二溶液热交 换器（11 ) 与第四发生器 （23 )连通， 第四发生器（23 ) 还有浓溶液管路经第三溶液泵 （21 ) 和第四溶液热交换器 （24) 与第二发生器 （2) 连通， 将第二发生器 （2) 有浓溶液管路经第 二溶液热交换器 （11 ) 与吸收器 （3 ) 连通调整为第二发生器 （2 ) 有浓溶液管路经第四溶液 热交换器 （24) 和第二溶液热交换器 （11 ) 与吸收器 （3 ) 连通， 将第二发生器 （2) 有冷剂 蒸汽通道与第二冷凝器（5)连通调整为第二发生器（2 )有冷剂蒸汽通道与第四发生器（23) 连通后第四发生器（23)再有冷剂液管路经第二节流阀 （22 ) 与第二冷凝器（5)连通——第 二发生器产生的冷剂蒸汽作为第四发生器的驱动热介质， 第四发生器 （23) 还有冷剂蒸汽通 道与第二冷凝器 （5 ) 连通， 形成双效-回热式单效第三类吸收式热泵。  16. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 1, wherein the fourth generator, the fourth solution heat exchanger, the second throttle valve and the third solution pump are added, The first generator (1) has a concentrated solution line connected to the second generator (2) via the first solution pump (7), the first solution heat exchanger (10) and the second solution heat exchanger (11) a concentrated solution line for the first generator (1) is connected to the fourth generator (23) via the first solution pump (7), the first solution heat exchanger (10) and the second solution heat exchanger (11) The fourth generator (23) and the concentrated solution line are connected to the second generator (2) via the third solution pump (21) and the fourth solution heat exchanger (24), and the second generator (2) The concentrated solution line is connected to the absorber (3) via the second solution heat exchanger (11) to be adjusted to the second generator (2). The concentrated solution line is passed through the fourth solution heat exchanger (24) and the second solution. The heat exchanger (11) is in communication with the absorber (3), and the second generator (2) has a refrigerant vapor passage and a second condenser (5) The second generator (23) is connected to the fourth generator (2), and the fourth generator (23) is further connected to the fourth generator (23) through the second throttle valve (22) and the second The second condenser (5) is connected - the refrigerant vapor generated by the second generator is used as the driving heat medium of the fourth generator, and the fourth generator (23) and the refrigerant vapor passage are connected to the second condenser (5) , forming a double-effect-recovery single-effect third-class absorption heat pump.
17. 第三类吸收式热泵， 是在权利要求 16所述的第三类吸收式热泵中， 增加溶液节流 阀， 将第一发生器（1 )有浓溶液管路经第一溶液泵 （7 )、 第一溶液热交换器（10)和第二溶 液热交换器（11 ) 与第四发生器（23)连通调整为第一发生器（1 )有浓溶液管路经第一溶液 泵（7)、 第一溶液热交换器（10)和第二溶液热交换器（11 )之后分别直接与第二发生器（2) 连通和再经溶液节流阀与第四发生器 （23) 连通， 形成双效 -单效第三类吸收式热泵。  17. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 16, wherein the solution throttle valve is added, and the first generator (1) has a concentrated solution line through the first solution pump ( 7), the first solution heat exchanger (10) and the second solution heat exchanger (11) are connected to the fourth generator (23) to be adjusted to be the first generator (1) having a concentrated solution line through the first solution pump (7), the first solution heat exchanger (10) and the second solution heat exchanger (11) are directly connected to the second generator (2) and then passed through the solution throttle valve and the fourth generator (23) Connected to form a double-effect-single-effect third-class absorption heat pump.
18. 第三类吸收式热泵， 是在权利要求 13所述的第三类吸收式热泵中， 增加第五发生 器、 第三节流阔和第五溶液热交换器， 第一溶液热交换器 （10) 增设浓溶液管路经第五溶液 热交换器与第五发生器连通， 第五发生器还有浓溶液管路经第五溶液热交换器与吸收器 （3) 连通， 将第四发生器 （23) 有冷剂蒸汽通道与第二冷凝器 （5) 连通调整为第四发生器 （23) 有冷剂蒸汽通道与第五发生器连通后第五发生器再有冷剂液管路经第三节流阀 （25) 与第二 冷凝器（5)连通， 第五发生器还有冷剂蒸汽通道与第二冷凝器（5 )连通， 形成三效-回热式 单效第三类吸收式热泵。  18. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 13, adding a fifth generator, a third section wide and a fifth solution heat exchanger, the first solution heat exchanger (10) The concentrated solution line is connected to the fifth generator via the fifth solution heat exchanger, and the fifth generator and the concentrated solution line are connected to the absorber (3) via the fifth solution heat exchanger, and the fourth The generator (23) has a refrigerant vapor passage connected to the second condenser (5) and is adjusted to be a fourth generator (23). The refrigerant vapor passage is connected to the fifth generator, and the fifth generator has a refrigerant liquid pipe. The third throttle valve (25) is in communication with the second condenser (5), and the fifth generator has a refrigerant vapor passage communicating with the second condenser (5) to form a three-effect-recovery type single effect Three types of absorption heat pumps.
19. 第三类吸收式热泵， 是在权利要求 14所述的第三类吸收式热泵中， 增加第五发生 器、 第三节流阀和第五溶液热交换器， 将第二溶液热交换器 （11 ) 有浓溶液管路经第四溶液 热交换器（24)与第二发生器（2)连通调整为第二溶液热交换器（11 )有浓溶液管路经第五 溶液热交换器和第四溶液热交换器（24) 与第二发生器（2)连通， 将第四发生器（23) 有浓 溶液管路经第二溶液热交换器（11 ) 与吸收器（3)连通调整为第四发生器（23 )有浓溶液管 路经第第五溶液热交换器与第五发生器连通， 第五发生器还有浓溶液管路经第二溶液热交换 器 （11 ) 与吸收器 （3) 连通， 将第四发生器 （23) 有冷剂蒸汽通道与第二冷凝器 （5 ) 连通 权 利 要 求 书 19. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 14, wherein the fifth generator, the third throttle valve and the fifth solution heat exchanger are added, and the second solution is heat exchanged The concentrated solution line is connected to the second generator (2) via the fourth solution heat exchanger (24) to be adjusted to the second solution heat exchanger (11), and the concentrated solution line is heat exchanged through the fifth solution. And the fourth solution heat exchanger (24) is in communication with the second generator (2), and the fourth generator (23) has a concentrated solution line through the second solution heat exchanger (11) and the absorber (3) The communication is adjusted to a fourth generator (23) having a concentrated solution line connected to the fifth generator via the fifth solution heat exchanger, and the fifth generator and the concentrated solution line passing through the second solution heat exchanger (11) Connected to the absorber (3) to connect the fourth generator (23) with a refrigerant vapor passage to the second condenser (5) Claim
_ WO 2013/003982 PCT/CN2011/001118 调整为第四发生器 （23) 有冷剂蒸汽通道与第五发生器连通后第五发生器再有冷剂液管路经 第三节流阀 （25) 与第二冷凝器（5)连通， 第五发生器还有冷剂蒸汽通道与第二冷凝器（5 ) 连通， 形成三效 -回热式单效第三类吸收式热泵。  _ WO 2013/003982 PCT/CN2011/001118 Adjusted to fourth generator (23) After the refrigerant vapor passage is connected to the fifth generator, the fifth generator has a refrigerant liquid line through the third throttle valve (25) ) communicating with the second condenser (5), the fifth generator and the refrigerant vapor passage are in communication with the second condenser (5) to form a three-effect-recovery single-effect third-type absorption heat pump.
20. 第三类吸收式热泵， 是在权利要求 16所述的第三类吸收式热泵中， 增加第五发生 器、 第三节流阀、 第四溶液泵和第五溶液热交换器， 将第二溶液热交换器 （11 ) 有浓溶液管 路与第四发生器（23)连通调整为第二溶液热交换器（11 )有浓溶液管路与第五发生器连通， 第五发生器还有浓溶液管路经第四溶液泵和第五溶液热交换器与第四发生器 （23 ) 连通， 将 第二发生器（2 )有浓溶液管路经第四溶液热交换器（24)和第二溶液热交换器（11 ) 与吸收 器（3)连通调整为第二发生器（2)有浓溶液管路经第四溶液热交换器（24)、 第五溶液热交 换器和第二溶液热交换器 （11 ) 与吸收器（3)连通， 将第四发生器（23)有冷剂蒸汽通道与 第二冷凝器（5)连通调整为第四发生器（23)有冷剂蒸汽通道与第五发生器连通后第五发生 器再有冷剂液管路经第三节流阀 （25)与第二冷凝器（5)连通， 第五发生器还有冷剂蒸汽通 道与第二冷凝器 （5) 连通， 形成三效 -回热式单效第三类吸收式热泵。  20. A third type of absorption heat pump, wherein in the third type of absorption heat pump according to claim 16, the fifth generator, the third throttle valve, the fourth solution pump, and the fifth solution heat exchanger are added, The second solution heat exchanger (11) has a concentrated solution line connected to the fourth generator (23) and is adjusted to be a second solution heat exchanger (11) having a concentrated solution line communicating with the fifth generator, the fifth generator Further, the concentrated solution line is connected to the fourth generator (23) via the fourth solution pump and the fifth solution heat exchanger, and the second generator (2) has the concentrated solution line through the fourth solution heat exchanger (24) And the second solution heat exchanger (11) is connected to the absorber (3) to be adjusted to a second generator (2) having a concentrated solution line through the fourth solution heat exchanger (24), the fifth solution heat exchanger and The second solution heat exchanger (11) is in communication with the absorber (3), and the fourth generator (23) has a refrigerant vapor passage connected to the second condenser (5) to be adjusted so that the fourth generator (23) is cold. After the agent vapor channel is in communication with the fifth generator, the fifth generator has a refrigerant liquid line through the third throttle valve (25) (5) communicating two condenser (5) communicating fifth steam generator, the refrigerant passage and the second condenser to form a three-way - a third heat recovery single effect absorption heat pump.
21. 第三类吸收式热泵，是在权利要求 2-3内任一权利要求所述的第三类吸收式热泵中， 增加第三发生器、 第四溶液热交换器和第二节流阔， 第二溶液泵 （14) 经第三溶液热交换器 21. A third type of absorption heat pump, which is a third type of absorption heat pump according to any of claims 2-3, wherein the third generator, the fourth solution heat exchanger and the second section are widened , the second solution pump (14) passes through the third solution heat exchanger
( 15) 增设浓溶液管路并再经第四溶液热交换器 （24) 与第三发生器 （12) 连通， 第三发生 器（12)还有浓溶液管路经第四溶液热交换器 （24) 与吸收器 （3)连通， 将第二发生器 （2 ) 有冷剂蒸汽通道与第二冷凝器 （5) 连通调整为第二发生器 （2) 有冷剂蒸汽通道与第三发生 器（12 )连通后第三发生器（12) 再有冷剂液管路经第二节流阀 （22) 与第二冷凝器（5)连 通——第二发生器产生的冷剂蒸汽作为第三发生器的驱动热介质， 第三发生器 （12) 还有冷 剂蒸汽通道与第二冷凝器 （5) 连通， 形成双效 -回热式单效第三类吸收式热泵。 (15) Adding a concentrated solution line and communicating with the third generator (12) via the fourth solution heat exchanger (24), the third generator (12) and the concentrated solution line passing through the fourth solution heat exchanger (24) communicating with the absorber (3), connecting the second generator (2) with the refrigerant vapor passage and the second condenser (5) to the second generator (2) having the refrigerant vapor passage and the third After the generator (12) is connected, the third generator (12) has a refrigerant liquid line connected to the second condenser (5) via the second throttle valve (22) - the refrigerant vapor generated by the second generator As the driving heat medium of the third generator, the third generator (12) and the refrigerant vapor passage are in communication with the second condenser (5) to form a double-effect-recovery single-effect third-type absorption heat pump.
22. 第三类吸收式热泵，是在权利要求 2-3内任一权利要求所述的第三类吸收式热泵中， 增加第三发生器、 第四溶液热交换器和第二节流阀， 将第二溶液泵 （14) 有浓溶液管路经第 三溶液热交换器（15)和第二溶液热交换器（11 ) 与第二发生器（2)连通调整为第二溶液泵 22. A third type of absorption heat pump, in the third type of absorption heat pump according to any one of claims 2-3, wherein the third generator, the fourth solution heat exchanger and the second throttle valve are added The second solution pump (14) has a concentrated solution line connected to the second generator (2) via the third solution heat exchanger (15) and the second solution heat exchanger (11) to be adjusted into a second solution pump.
( 14)有浓溶液管路经第三溶液热交换器（15 )、 第二溶液热交换器（11 )和第四溶液热交换 器（24)与第二发生器（2)连通， 将第二发生器（2)有浓溶液管路经第二溶液热交换器（11 ) 与吸收器 （3) 连通调整为第二发生器 （2 ) 有浓溶液管路经第四溶液热交换器 （24) 与第三 发生器 （12) 连通， 第三发生器 （12) 还有浓溶液管路经第二溶液热交换器 （11 ) 与吸收器(14) a concentrated solution line is connected to the second generator (2) via the third solution heat exchanger (15), the second solution heat exchanger (11), and the fourth solution heat exchanger (24), The second generator (2) has a concentrated solution line connected to the absorber (3) via the second solution heat exchanger (11) to be adjusted to a second generator (2) having a concentrated solution line through the fourth solution heat exchanger ( 24) communicating with the third generator (12), the third generator (12) and the concentrated solution line passing through the second solution heat exchanger (11) and the absorber
(3)连通，将第二发生器（2 )有冷剂蒸汽通道与第二冷凝器（5 )连通调整为第二发生器（2) 有冷剂蒸汽通道与第三发生器 （12) 连通后第三发生器 （12) 再有冷剂液管路经第二节流阀(3) communicating, adjusting the refrigerant flow channel of the second generator (2) to the second condenser (5) to be a second generator (2) having a refrigerant vapor channel connected to the third generator (12) After the third generator (12), the refrigerant liquid line passes through the second throttle valve
(22)与第二冷凝器（5)连通——第一发生器产生的冷剂蒸汽作为第三发生器的驱动热介质， 第三发生器 （12 ) 还有冷剂蒸汽通道与第二冷凝器 （5 ) 连通， 形成双效-回热式单效第三类 吸收式热泵。 (22) communicating with the second condenser (5) - the refrigerant vapor generated by the first generator acts as a driving heat medium for the third generator, and the third generator (12) also has a refrigerant vapor passage and a second condensation The device (5) is connected to form a double-effect-recovery single-effect third-class absorption heat pump.
23. 第三类吸收式热泵， 是在权利要求 22所述的第三类吸收式热泵中， 增加溶液节流 阀， 将第二溶液泵 （14) 有浓溶液管路经第三溶液热交换器 （15 )、 第二溶液热交换器 （11 ) 和第四溶液热交换器（24 ) 与第二发生器（2 )连通调整为第二溶液泵 （14)有浓溶液管路经 第三溶液热交换器（15)、 第二溶液热交换器（11 )之后分别再经溶液节流阀 （22) 与第三发 生器 （12) 连通和再经第四溶液热交换器 （24 ) 与第二发生器 （2) 连通， 形成双效-回热式 单效第三类吸收式热泵。  23. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 22, wherein the solution throttle valve is added, and the second solution pump (14) has a concentrated solution line through the third solution heat exchange The second solution heat exchanger (11) and the fourth solution heat exchanger (24) are connected to the second generator (2) to be adjusted to be a second solution pump (14) having a concentrated solution line through the third The solution heat exchanger (15) and the second solution heat exchanger (11) are respectively connected to the third generator (12) via the solution throttle valve (22) and then to the fourth solution heat exchanger (24). The second generator (2) is connected to form a double-effect-recovery single-effect third-class absorption heat pump.
24. 第三类吸收式热泵，是在权利要求 2-3内任一权利要求所述的第三类吸收式热泵中， 权 利 要 求 书 24. A third type of absorption heat pump, in the third type of absorption heat pump according to any of claims 2-3, Claim
一 WO 2013/003982 PCT/CN2011/001118 增加第三发生器、 第四溶液热交换器、 第二节流阀、 第三溶液泵或第四溶液泵， 将第二溶液 泵 （14) 有浓溶液管路经第三溶液热交换器 （15) 和第二溶液热交换器 （11 ) 与第二发生器 (2)连通调整为第二溶液泵（14)有浓溶液管路经第三溶液热交换器（15 )和第二溶液热交 换器（11 ) 与第三发生器（12)连通， 第三发生器 （12)还有浓溶液管路经第三溶液泵 （21 ) 或第四溶液泵、 第四溶液热交换器 （24) 与第二发生器 （2) 连通， 将第二发生器 （2 ) 有浓 溶液管路经第二溶液热交换器 （11 ) 与吸收器 （3) 连通调整为第二发生器 （2) 有浓溶液管 路经第四溶液热交换器（24)和第二溶液热交换器（11 ) 与吸收器（3)连通， 将第二发生器 (2)有冷剂蒸汽通道与第二冷凝器（5 )连通调整为第二发生器（2)有冷剂蒸汽通道与第三 发生器（12 )连通后第三发生器（12 )再有冷剂液管路经第二节流阀（22)与第二冷凝器（5 ) 连通——第二发生器产生的冷剂蒸汽作为第三发生器的驱动热介质， 第三发生器 （12) 还有 冷剂蒸汽通道与第二冷凝器 （5) 连通， 形成双效 -回热式单效第三类吸收式热泵。 A WO 2013/003982 PCT/CN2011/001118 adding a third generator, a fourth solution heat exchanger, a second throttle valve, a third solution pump or a fourth solution pump, the second solution pump (14) having a concentrated solution The pipeline is connected to the second generator (2) via the third solution heat exchanger (15) and the second solution heat exchanger (11) to be adjusted to a second solution pump (14) having a concentrated solution pipeline through the third solution heat The exchanger (15) and the second solution heat exchanger (11) are in communication with the third generator (12), and the third generator (12) has a concentrated solution line via the third solution pump (21) or the fourth solution The pump, the fourth solution heat exchanger (24) is in communication with the second generator (2), and the second generator (2) has a concentrated solution line through the second solution heat exchanger (11) and the absorber (3) The communication is adjusted to the second generator (2). The concentrated solution line is connected to the absorber (3) via the fourth solution heat exchanger (24) and the second solution heat exchanger (11), and the second generator (2) a refrigerant vapor passage is connected to the second condenser (5) to be adjusted to a second generator (2) having a refrigerant vapor passage and a third generator (12) After the communication, the third generator (12) has a refrigerant liquid line connected to the second condenser (5) via the second throttle valve (22) - the refrigerant vapor generated by the second generator is generated as the third The driving heat medium, the third generator (12) and the refrigerant vapor passage are connected with the second condenser (5) to form a double-effect-recovery single-effect third-type absorption heat pump.
25. 第三类吸收式热泵， 是在权利要求 24所述的第三类吸收式热泵中， 增加溶液节流 阀， 将第二溶液泵（14)有浓溶液管路经第三溶液热交换器（15)和第二溶液热交换器（11 ) 与第三发生器 （12) 连通调整为第二溶液泵 （14) 有浓溶液管路经第三溶液热交换器 （15) 和第二溶液热交换器（11 )之后分别直接与第二发生器（2)连通和再经溶液节流阀 （22) 与 第三发生器 （12) 连通， 形成双效 -回热式单效第三类吸收式热泵。  25. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 24, wherein the solution throttle valve is added, and the second solution pump (14) has a concentrated solution line through the third solution heat exchange The second solution heat exchanger (15) and the second solution heat exchanger (11) are connected to the third generator (12) to be adjusted to a second solution pump (14) having a concentrated solution line through the third solution heat exchanger (15) and the second The solution heat exchanger (11) is directly connected to the second generator (2) and then communicates with the third generator (12) via the solution throttle valve (22) to form a double-effect-recovery single-effect third. Absorption heat pump.
26. 第三类吸收式热泵， 是在权利要求 21所述的第三类吸收式热泵中， 增加第四发生 器、 第五溶液热交换器和第三节流阀， 第二溶液泵 （14) 经第三溶液热交换器 （15) 增设浓 溶液管路并再经第五溶液热交换器与第四发生器 （23) 连通， 第四发生器 （23) 还有浓溶液 管路经第五溶液热交换器与吸收器（3 )连通， 将第三发生器（12)有冷剂蒸汽通道与第二冷 凝器（5)连通调整为第三发生器（12 )有冷剂蒸汽通道与第四发生器（23 )连通后第四发生 器 （23) 再有冷剂液管路经第三节流阀 （25) 与第二冷凝器 （5)连通， 第四发生器 （23) 还 有冷剂蒸汽通道与第二冷凝器 （5) 连通， 形成三效 -回热式单效第三类吸收式热泵。  26. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 21, wherein the fourth generator, the fifth solution heat exchanger and the third throttle valve are added, and the second solution pump (14) Adding a concentrated solution line through the third solution heat exchanger (15) and communicating with the fourth generator (23) via the fifth solution heat exchanger, the fourth generator (23) and the concentrated solution line The five-solution heat exchanger is in communication with the absorber (3), and the third generator (12) has a refrigerant vapor passage connected to the second condenser (5) to be adjusted to a third generator (12) having a refrigerant vapor passage and After the fourth generator (23) is connected, the fourth generator (23) is further connected to the second condenser (5) via the third throttle valve (25), and the fourth generator (23) is further A refrigerant vapor passage is connected to the second condenser (5) to form a three-effect-recovery single-effect third-type absorption heat pump.
27. 第三类吸收式热泵， 是在权利要求 22所述的第三类吸收式热泵中， 增加第四发生 器、 第五溶液热交换器和第三节流阀， 将第二溶液泵 （14) 有浓溶液管路经第三溶液热交换 器 （15)、 第二溶液热交换器 （11 ) 和第四溶液热交换器 （24 ) 与第二发生器 （2) 连通调整 为第二溶液泵 （14) 有浓溶液管路经第三溶液热交换器 （15)、 第二溶液热交换器 （11 )、 第 五溶液热交换器和第四溶液热交换器 （24) 与第二发生器（2)连通， 将第三发生器 （12 )有 浓溶液管路经第二溶液热交换器（11 ) 与吸收器（3)连通调整为第三发生器（12)有浓溶液 管路经第五溶液热交换器与第四发生器 （23) 连通， 第四发生器 （23 ) 还有浓溶液管路经第 二溶液热交换器（11 ) 与吸收器（3)连通， 将第三发生器 （12 )有冷剂蒸汽通道与第二冷凝 器（5)连通调整为第三发生器（12)有冷剂蒸汽通道与第四发生器（23)连通后第四发生器 27. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 22, wherein the fourth generator, the fifth solution heat exchanger and the third throttle valve are added, and the second solution pump is 14) The concentrated solution line is connected to the second generator (2) via the third solution heat exchanger (15), the second solution heat exchanger (11), and the fourth solution heat exchanger (24) to be adjusted to the second The solution pump (14) has a concentrated solution line through the third solution heat exchanger (15), the second solution heat exchanger (11), the fifth solution heat exchanger, and the fourth solution heat exchanger (24) and the second The generator (2) is connected, and the third generator (12) has a concentrated solution pipeline connected to the absorber (3) via the second solution heat exchanger (11) to be adjusted to a third generator (12) with a concentrated solution tube. The fifth solution heat exchanger is in communication with the fourth generator (23), and the fourth generator (23) and the concentrated solution line are connected to the absorber (3) via the second solution heat exchanger (11), The third generator (12) has a refrigerant vapor passage connected to the second condenser (5) and is adjusted to have a third generator (12) The refrigerant vapor generator and the fourth passage (23) communicating with the fourth generator after
(23) 再有冷剂液管路经第三节流阀 （25 ) 与第二冷凝器 （5 ) 连通， 第四发生器 （23 )还有 冷剂蒸汽通道与第二冷凝器 （5) 连通， 形成三效 -回热式单效第三类吸收式热泵。 (23) a further refrigerant liquid line is connected to the second condenser (5) via a third throttle valve (25), and the fourth generator (23) has a refrigerant vapor passage and a second condenser (5) Connected to form a three-effect-recovery single-effect third-class absorption heat pump.
28. 第三类吸收式热泵， 是在权利要求 24所述的第三类吸收式热泵中， 增加第四发生 器、 第五溶液热交换器、 第三节流阀、 第四溶液泵或第五溶液泵， 将第二溶液泵 （14) 有浓 溶液管路经第三溶液热交换器 （15) 和第二溶液热交换器 （11 ) 与第三发生器 （12 ) 连通调 整为第二溶液泵 （14) 有浓溶液管路经第三溶液热交换器 （15) 和第二溶液热交换器 （11 ) 与第四发生器 （23) 连通， 第四发生器 （23) 还有浓溶液管路经第四溶液泵或第五溶液泵、 第五溶液热交换器与第三发生器（12 )连通， 将第二发生器（2)有浓溶液管路经第四溶液热 权 利 要 求 书 28. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 24, wherein the fourth generator, the fifth solution heat exchanger, the third throttle valve, the fourth solution pump or the first a five-solution pump, the second solution pump (14) having a concentrated solution line is connected to the third generator (12) through the third solution heat exchanger (15) and the second solution heat exchanger (11) to be adjusted to a second The solution pump (14) has a concentrated solution line connected to the fourth generator (23) via the third solution heat exchanger (15) and the second solution heat exchanger (11), and the fourth generator (23) is also rich The solution line is connected to the third generator (12) via the fourth solution pump or the fifth solution pump, the fifth solution heat exchanger, and the second generator (2) has a concentrated solution line through the fourth solution heat Claim
― WO 2013/003982 PCT/CN2011/001118 交换器 （24) 和第二溶液热交换器 （11 ) 与吸收器 （3) 连通调整为第二发生器 （2) 有浓溶 液管路经第四溶液热交换器（24)、第五溶液热交换器和第二溶液热交换器（ 11 )与吸收器（3) 连通， 将第三发生器 （12) 有冷剂蒸汽通道与第二冷凝器 （5) 连通调整为第三发生器 （12) 有冷剂蒸汽通道与第四发生器 （23 ) 连通后第四发生器 （23 ) 再有冷剂液管路经第三节流阀 (25) 与第二冷凝器 （5) 连通， 第四发生器 （23) 还有冷剂蒸汽通道与第二冷凝器 （5 ) 连 通， 形成三效-回热式单效第三类吸收式热泵。  ― WO 2013/003982 PCT/CN2011/001118 The exchanger (24) and the second solution heat exchanger (11) are connected to the absorber (3) to be adjusted to the second generator (2) with a concentrated solution line through the fourth solution The heat exchanger (24), the fifth solution heat exchanger and the second solution heat exchanger (11) are in communication with the absorber (3), and the third generator (12) has a refrigerant vapor passage and a second condenser ( 5) The communication is adjusted to the third generator (12). The refrigerant flow channel is connected to the fourth generator (23), and the fourth generator (23) has a refrigerant liquid line through the third throttle valve (25). In communication with the second condenser (5), the fourth generator (23) and the refrigerant vapor passage are in communication with the second condenser (5) to form a three-effect-recovery single-effect third-type absorption heat pump.
29. 第三类吸收式热泵，是在权利要求 4所述的第三类吸收式热泵中，增加第三发生器、 第四溶液热交换器和第二节流阀， 第二溶液泵 （14) 经第三溶液热交换器 （15) 增设浓溶液 管路并再经第四溶液热交换器 （24) 与第三发生器 （12 ) 连通， 第三发生器 （12 ) 还有浓溶 液管路经第四溶液热交换器 （24) 与吸收器 （3) 连通， 将第二发生器 （2 ) 有冷剂蒸汽通道 与第二冷凝器 （5 ) 连通调整为第二发生器 （2) 有冷剂蒸汽通道与第三发生器 （12 ) 连通后 第三发生器（12) 再有冷剂液管路经第二节流阀 （22 ) 与第二冷凝器（5)连通——第二发生 器产生的冷剂蒸汽作为第三发生器的驱动热介质， 第三发生器 （12) 还有冷剂蒸汽通道与第 二冷凝器 （5) 连通， 形成双效-回热式单效第三类吸收式热泵。  29. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 4, adding a third generator, a fourth solution heat exchanger and a second throttle valve, and a second solution pump (14) Adding a concentrated solution line through the third solution heat exchanger (15) and communicating with the third generator (12) via the fourth solution heat exchanger (24), the third generator (12) and the concentrated solution tube The fourth solution heat exchanger (24) is connected to the absorber (3), and the second generator (2) has a refrigerant vapor channel connected to the second condenser (5) to be adjusted to the second generator (2). After the refrigerant vapor passage is in communication with the third generator (12), the third generator (12) is further connected to the second condenser (5) via the second throttle valve (22). The refrigerant vapor generated by the second generator serves as a driving heat medium for the third generator, and the third generator (12) and the refrigerant vapor passage are connected to the second condenser (5) to form a double-effect-recovery single effect. The third type of absorption heat pump.
30. 第三类吸收式热泵，是在权利要求 4所述的第三类吸收式热泵中，增加第三发生器、 第四溶液热交换器和第二节流阀，将第二溶液泵（14)有浓溶液管路经第三溶液热交换器（15) 和第二溶液热交换器（11 ) 与第二发生器（2 )连通调整为第二溶液泵 （14)有浓溶液管路经 第三溶液热交换器（15)、 第二溶液热交换器（11 )和第四溶液热交换器（24) 与第二发生器 30. A third type of absorption heat pump, wherein in the third type of absorption heat pump according to claim 4, the third generator, the fourth solution heat exchanger and the second throttle valve are added, and the second solution pump is 14) The concentrated solution line is connected to the second generator (2) via the third solution heat exchanger (15) and the second solution heat exchanger (11) to adjust the second solution pump (14) to have a concentrated solution line a third solution heat exchanger (15), a second solution heat exchanger (11), and a fourth solution heat exchanger (24) and a second generator
(2 )连通， 将第二发生器 （2)有浓溶液管路经第二溶液热交换器 （11 ) 与吸收器（3)连通 调整为第二发生器 （2) 有浓溶液管路经第四溶液热交换器 （24) 与第三发生器 （12 ) 连通， 第三发生器（12)还有浓溶液管路经第二溶液热交换器（11 ) 与吸收器（3) 连通， 将第二发 生器（2)有冷剂蒸汽通道与第二冷凝器（5)连通调整为第二发生器（2)有冷剂蒸汽通道与 第三发生器 （12) 连通后第三发生器 （12) 再有冷剂液管路经第二节流阀 （22) 与第二冷凝 器（5)连通——第一发生器产生的冷剂蒸汽作为第三发生器的驱动热介质，第三发生器（12) 还有冷剂蒸汽通道与第二冷凝器 （5) 连通， 形成双效-回热式单效第三类吸收式热泵。 (2) communicating, connecting the second generator (2) having a concentrated solution line through the second solution heat exchanger (11) to the absorber (3) to be adjusted to a second generator (2) having a concentrated solution line The fourth solution heat exchanger (24) is in communication with the third generator (12), and the third generator (12) and the concentrated solution line are in communication with the absorber (3) via the second solution heat exchanger (11). The second generator (2) has a refrigerant vapor passage connected to the second condenser (5) and is adjusted to be a second generator (2) having a refrigerant vapor passage connected to the third generator (12) and a third generator (12) a refrigerant liquid line is connected to the second condenser (5) via the second throttle valve (22) - the refrigerant vapor generated by the first generator is used as the driving heat medium of the third generator, The three generators (12) also have a refrigerant vapor passage communicating with the second condenser (5) to form a double-effect regenerative single-effect third-stage absorption heat pump.
31. 第三类吸收式热泵， 是在权利要求 30所述的第三类吸收式热泵中， 增加溶液节流 阀， 将第二溶液泵 （14) 有浓溶液管路经第三溶液热交换器 （15 )、 第二溶液热交换器 （11 ) 和第四溶液热交换器（24) 与第二发生器（2 )连通调整为第二溶液泵 （14)有浓溶液管路经 第三溶液热交换器（15)、 第二溶液热交换器（11 )之后分别再经溶液节流阀 （22 ) 与第三发 生器 （12) 连通和再经第四溶液热交换器 （24) 与第二发生器 （2) 连通， 形成双效-回热式 单效第三类吸收式热泵。  31. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 30, wherein the solution throttle valve is added, and the second solution pump (14) has a concentrated solution line through the third solution heat exchange The second solution heat exchanger (15) and the fourth solution heat exchanger (24) are connected to the second generator (2) to be adjusted to be a second solution pump (14) having a concentrated solution line through the third The solution heat exchanger (15) and the second solution heat exchanger (11) are respectively connected to the third generator (12) via the solution throttle valve (22) and then to the fourth solution heat exchanger (24). The second generator (2) is connected to form a double-effect-recovery single-effect third-class absorption heat pump.
32. 第三类吸收式热泵，是在权利要求 4所述的第三类吸收式热泵中，增加第三发生器、 第四溶液热交换器、 第三溶液泵和第二节流阀， 将第二溶液泵 （14) 有浓溶液管路经第三溶 液热交换器（15 )和第二溶液热交换器（11 )与第二发生器（2)连通调整为第二溶液泵（14) 有浓溶液管路经第三溶液热交换器 （15 ) 和第二溶液热交换器 （11 ) 与第三发生器 （12 ) 连 通， 第三发生器 （12 ) 还有浓溶液管路经第三溶液泵 （21 ) 和第四溶液热交换器 （24) 与第 二发生器 （2) 连通， 将第二发生器 （2) 有浓溶液管路经第二溶液热交换器 （11 ) 与吸收器 32. The third type of absorption heat pump is the third type of absorption heat pump according to claim 4, wherein the third generator, the fourth solution heat exchanger, the third solution pump and the second throttle valve are added, The second solution pump (14) has a concentrated solution line connected to the second generator (2) via the third solution heat exchanger (15) and the second solution heat exchanger (11) to be adjusted to the second solution pump (14) The concentrated solution line is connected to the third generator (12) via the third solution heat exchanger (15) and the second solution heat exchanger (11), and the third generator (12) and the concentrated solution line are passed through The three solution pump (21) and the fourth solution heat exchanger (24) are in communication with the second generator (2), and the second generator (2) has a concentrated solution line through the second solution heat exchanger (11) Absorber
(3) 连通调整为第二发生器 （2) 有浓溶液管路经第四溶液热交换器 （24) 和第二溶液热交 换器 （11 ) 与吸收器 （3 ) 连通， 将第二发生器 （2)有冷剂蒸汽通道与第二冷凝器 （5)连通 调整为第二发生器（2)有冷剂蒸汽通道与第三发生器（12 )连通后第三发生器（12)再有冷 权 利 要 求 书 (3) Connected to the second generator (2) The concentrated solution line is connected to the absorber (3) via the fourth solution heat exchanger (24) and the second solution heat exchanger (11), which will occur second. The second generator (2) has a refrigerant vapor passage connected to the second condenser (5) and is adjusted to be a second generator (2) having a refrigerant vapor passage connected to the third generator (12) and then a third generator (12) Have cold Claim
_ WO 201層 3982 PCT/CN2011/001118 剂液管路经第二节流阀（22 )与第二冷凝器（5 )连通——第二发生器产生的冷剂蒸汽作为第 三发生器的驱动热介质， 第三发生器（12 )还有冷剂蒸汽通道与第二冷凝器（5)连通， 形成 双效 -回热式单效第三类吸收式热泵。  _ WO 201 layer 3982 PCT/CN2011/001118 The liquid supply line is connected to the second condenser (5) via the second throttle valve (22) - the refrigerant vapor generated by the second generator is used as the drive for the third generator The heat medium, the third generator (12) and the refrigerant vapor passage communicate with the second condenser (5) to form a double-effect-recovery single-effect third-type absorption heat pump.
33. 第三类吸收式热泵， 是在权利要求 32所述的第三类吸收式热泵中， 增加溶液节流 阀， 将第二溶液泵 （14 )有浓溶液管路经第三溶液热交换器（15)和第二溶液热交换器（11 ) 与第三发生器 （12) 连通调整为第二溶液泵 （14 ) 有浓溶液管路经第三溶液热交换器 （15) 和第二溶液热交换器（11 )之后分别直接与第二发生器（2)连通和再经溶液节流阀 （22) 与 第三发生器 （12) 连通， 形成双效 -回热式单效第三类吸收式热泵。  33. A third type of absorption heat pump, wherein in the third type of absorption heat pump according to claim 32, the solution throttle valve is added, and the second solution pump (14) has a concentrated solution line and is subjected to a third solution heat exchange. The second solution heat exchanger (15) and the second solution heat exchanger (11) are connected to the third generator (12) to be adjusted to a second solution pump (14) having a concentrated solution line through the third solution heat exchanger (15) and the second The solution heat exchanger (11) is directly connected to the second generator (2) and then communicates with the third generator (12) via the solution throttle valve (22) to form a double-effect-recovery single-effect third. Absorption heat pump.
34. 第三类吸收式热泵， 是在权利要求 29所述的第三类吸收式热泵中， 增加第四发生 器、 第五溶液热交换器和第三节流阀， 第二溶液泵 （14 ) 经第三溶液热交换器 （15 ) 增设浓 溶液管路并再经第五溶液热交换器与第四发生器 （23) 连通， 第四发生器 （23) 还有浓溶液 管路经第五溶液热交换器与吸收器（3 )连通， 将第三发生器（12 )有冷剂蒸汽通道与第二冷 凝器（5)连通调整为第三发生器（12)有冷剂蒸汽通道与第四发生器（23)连通后第四发生 器（23) 再有冷剂液管路经第三节流阀 （25) 与第二冷凝器 （5 ) 连通， 第四发生器 （23 ) 还 有冷剂蒸汽通道与第二冷凝器 （5) 连通， 形成三效-回热式单效第三类吸收式热泵。  34. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 29, wherein the fourth generator, the fifth solution heat exchanger and the third throttle valve are added, and the second solution pump (14) Adding a concentrated solution line through the third solution heat exchanger (15) and communicating with the fourth generator (23) via the fifth solution heat exchanger, the fourth generator (23) and the concentrated solution line The five-solution heat exchanger is in communication with the absorber (3), and the third generator (12) has a refrigerant vapor passage connected to the second condenser (5) to be adjusted to a third generator (12) having a refrigerant vapor passage and After the fourth generator (23) is connected, the fourth generator (23) is further connected to the second condenser (5) via the third throttle valve (25), and the fourth generator (23) is further connected. A refrigerant vapor passage is connected to the second condenser (5) to form a three-effect-recovery single-effect third-type absorption heat pump.
35. 第三类吸收式热泵， 是在权利要求 30所述的第三类吸收式热泵中， 增加第四发生 器、 第五溶液热交换器和第三节流阔， 将第二溶液泵 （14) 有浓溶液管路经第三溶液热交换 器 （15)、 第二溶液热交换器 （11 ) 和第四溶液热交换器 （24) 与第二发生器 （2) 连通调整 为第二溶液泵 （14) 有浓溶液管路经第三溶液热交换器 （15)、 第二溶液热交换器 （11 )、 第 五溶液热交换器和第四溶液热交换器（24) 与第二发生器（2)连通， 将第三发生器 （12)有 浓溶液管路经第二溶液热交换器（11 ) 与吸收器（3)连通调整为第三发生器（12)有浓溶液 管路经第五溶液热交换器与第四发生器 （23) 连通， 第四发生器 （23 ) 还有浓溶液管路经第 二溶液热交换器（11 ) 与吸收器 （3 )连通， 将第三发生器 （12)有冷剂蒸汽通道与第二冷凝 器（5 )连通调整为第三发生器（12)有冷剂蒸汽通道与第四发生器（23)连通后第四发生器 35. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 30, wherein the fourth generator, the fifth solution heat exchanger and the third section are widened, and the second solution pump is 14) The concentrated solution line is connected to the second generator (2) via the third solution heat exchanger (15), the second solution heat exchanger (11), and the fourth solution heat exchanger (24) to be adjusted to the second The solution pump (14) has a concentrated solution line through the third solution heat exchanger (15), the second solution heat exchanger (11), the fifth solution heat exchanger, and the fourth solution heat exchanger (24) and the second The generator (2) is connected, and the third generator (12) has a concentrated solution line connected to the absorber (3) via the second solution heat exchanger (11) to be adjusted to a third generator (12) with a concentrated solution tube. The fifth solution heat exchanger is in communication with the fourth generator (23), and the fourth generator (23) and the concentrated solution line are connected to the absorber (3) via the second solution heat exchanger (11), The third generator (12) has a refrigerant vapor passage connected to the second condenser (5) and is adjusted to have a third generator (12) The refrigerant vapor generator and the fourth passage (23) communicating with the fourth generator after
(23) 再有冷剂液管路经第三节流阀 （25) 与第二冷凝器 （5) 连通， 第四发生器（23)还有 冷剂蒸汽通道与第二冷凝器 （5) 连通， 形成三效 -回热式单效第三类吸收式热泵。 (23) The refrigerant liquid line is connected to the second condenser (5) via the third throttle valve (25), and the fourth generator (23) has a refrigerant vapor passage and a second condenser (5) Connected to form a three-effect-recovery single-effect third-class absorption heat pump.
36. 第三类吸收式热泵， 是在权利要求 32所述的第三类吸收式热泵中， 增加第四发生 器、 第五溶液热交换器、 第三节流阀和第四溶液泵， 将第二溶液泵 （14 ) 有浓溶液管路经第 三溶液热交换器 （15 ) 和第二溶液热交换器 （11 ) 与第三发生器 （12) 连通调整为第二溶液 泵 （14) 有浓溶液管路经第三溶液热交换器 （15) 和第二溶液热交换器 （11 ) 与第四发生器 36. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 32, wherein the fourth generator, the fifth solution heat exchanger, the third throttle valve and the fourth solution pump are added, The second solution pump (14) has a concentrated solution line connected to the third generator (12) via the third solution heat exchanger (15) and the second solution heat exchanger (11) to be adjusted to the second solution pump (14) a concentrated solution line through the third solution heat exchanger (15) and the second solution heat exchanger (11) and the fourth generator
(23) 连通， 第四发生器 （23) 还有浓溶液管路经第四溶液泵和第五溶液热交换器与第三发 生器（12)连通， 将第二发生器（2)有浓溶液管路经第四溶液热交换器（24)和第二溶液热 交换器 （11 ) 与吸收器 （3) 连通调整为第二发生器 （2) 有浓溶液管路经第四溶液热交换器(23) connected, the fourth generator (23) and the concentrated solution line are connected to the third generator (12) via the fourth solution pump and the fifth solution heat exchanger, and the second generator (2) is thick The solution line is connected to the absorber (3) via the fourth solution heat exchanger (24) and the second solution heat exchanger (11) to be adjusted to the second generator (2). The concentrated solution line is subjected to the fourth solution heat exchange. Device
(24)、第五溶液热交换器和第二溶液热交换器（11 )与吸收器（3)连通， 将第三发生器（12) 有冷剂蒸汽通道与第二冷凝器（5)连通调整为第三发生器（12 )有冷剂蒸汽通道与第四发生 器（23 )连通后第四发生器 （23) 再有冷剂液管路经第三节流阀 （25) 与第二冷凝器（5)连 通， 第四发生器 （23 ) 还有冷剂蒸汽通道与第二冷凝器 （5) 连通， 形成三效-回热式单效第 三类吸收式热泵。 (24), the fifth solution heat exchanger and the second solution heat exchanger (11) are in communication with the absorber (3), and the third generator (12) has a refrigerant vapor passage connected to the second condenser (5) Adjusted to a third generator (12) having a refrigerant vapor passage in communication with the fourth generator (23), the fourth generator (23) having a refrigerant liquid line through the third throttle valve (25) and the second The condenser (5) is connected, and the fourth generator (23) and the refrigerant vapor passage are connected with the second condenser (5) to form a three-effect-recovery type single-effect third-type absorption heat pump.
37. 第三类吸收式热泵， 是在权利要求 1所提及的单效-单效第三类吸收式热泵以及权 利要求 5- 12内任一权利要求所述的第三类吸收式热泵中， 增加新增发生器、新增溶液热交换 权 利 要 求 书 37. A third type of absorption heat pump, which is the single-effect single-effect third-type absorption heat pump of claim 1 and the third type of absorption heat pump according to any one of claims 5-12. , add new generator, add solution heat exchange Claim
_ O 2013/003982 PCT/CN2011/001118 器、 新增节流阀和新增溶液泵， 吸收器 （3) 增设稀溶液管路经新增溶液热交换器 （B) 与新 增发生器（A)连通， 新增发生器 （A)还有浓溶液管路经新增溶液泵（D)和新增溶液热交换 器（B)之后与第一发生器 （1 ) 经溶液泵 （7)和第一溶液热交换器 （10)之后的浓溶液管路 汇合， 将第一发生器（1 )有冷剂蒸汽通道与第一冷凝器（4)连通调整为第一发生器 （1 )有 冷剂蒸汽通道与新增发生器 （A) 连通后新增发生器 （A) 再有冷剂液管路经新增节流阀 （C) 与第一冷凝器 （4)连通， 新增发生器 （A)还有冷剂蒸汽通道与第一冷凝器 （4)连通， 形成 以双效为低温发生流程的第三类吸收式热泵。  _ O 2013/003982 PCT/CN2011/001118, new throttle valve and new solution pump, absorber (3) additional dilute solution line via new solution heat exchanger (B) and new generator (A Connected, the new generator (A) and the concentrated solution line through the new solution pump (D) and the new solution heat exchanger (B) and the first generator (1) via the solution pump (7) and The concentrated solution line after the first solution heat exchanger (10) merges, and the first generator (1) has a refrigerant vapor channel connected to the first condenser (4) to be adjusted to be the first generator (1) has cold Add a generator (A) after connecting the new steam generator to the new generator (A). Then connect the coolant line to the first condenser (4) via the new throttle valve (C). (A) There is also a refrigerant vapor passage communicating with the first condenser (4) to form a third type of absorption heat pump having a double effect as a low temperature generation process.
38. 第三类吸收式热泵， 是在权利要求 1所提及的单效 -单效第三类吸收式热泵以及权 利要求 5- 12内任一权利要求所述的第三类吸收式热泵中， 增加新增发生器、新增溶液热交换 器和新增节流阀， 将第一发生器（1 )有浓溶液管路经溶液泵 （7 )和第一溶液热交换器（10) 与第二溶液热交换器（11 )连通调整为第一发生器（ 1 )有浓溶液管路经新增溶液热交换器（B) 与新增发生器 （A) 连通， 新增发生器 （A) 还有浓溶液管路经溶液泵 （7)、 新增溶液热交换 器 （B) 和第一溶液热交换器 （10) 与第二溶液热交换器 （11 ) 连通， 将第一发生器 （1 ) 有 冷剂蒸汽通道与第一冷凝器 （4) 连通调整为第一发生器 （1 ) 有冷剂蒸汽通道与新增发生器 38. A third type of absorption heat pump, which is the single-effect single-effect third-type absorption heat pump mentioned in claim 1 and the third-type absorption heat pump according to any one of claims 5-12. , adding a new generator, a new solution heat exchanger and a new throttle valve, the first generator (1) has a concentrated solution line through the solution pump (7) and the first solution heat exchanger (10) The second solution heat exchanger (11) is connected to be adjusted to be a first generator (1) having a concentrated solution line connected to the newly added generator (A) via a new solution heat exchanger (B), and a new generator (A) a concentrated solution line is connected to the second solution heat exchanger (11) via a solution pump (7), a new solution heat exchanger (B), and a first solution heat exchanger (10), and the first generator is (1) The refrigerant vapor passage is connected to the first condenser (4) to be adjusted to the first generator (1) with a refrigerant vapor passage and a new generator
(A) 连通后新增发生器 （A) 再有冷剂液管路经新增节流阀 （C) 与第一冷凝器 （4) 连通， 新增发生器 （A) 还有冷剂蒸汽通道与第一冷凝器 （4) 连通， 形成以双效为低温发生流程的 第三类吸收式热泵。 (A) New generator (A) after communication. Then the refrigerant liquid line is connected to the first condenser (4) via the new throttle valve (C). The new generator (A) and refrigerant vapor are added. The passage communicates with the first condenser (4) to form a third type of absorption heat pump that performs a dual-effect low temperature generation process.
39. 第三类吸收式热泵， 是在权利要求 1所提及的单效-单效第三类吸收式热泵以及权 利要求 5-12内任一权利要求所述的第三类吸收式热泵中， 增加新增发生器、新增溶液热交换 器、 新增节流阀和新增溶液泵， 将吸收器（3 )有稀溶液管路经第一溶液热交换器（10)与第 一发生器 （1 ) 连通调整为吸收器 （3) 有稀溶液管路经第一溶液热交换器 （10) 和新增溶液 热交换器 （B) 与新增发生器（A) 连通， 新增发生器 （A) 还有浓溶液管路经新增溶液泵 （D) 和新增溶液热交换器（B) 与第一发生器（1 )连通， 将第一发生器（1 )有冷剂蒸汽通道与第 一冷凝器（4)连通调整为第一发生器（1 )有冷剂蒸汽通道与新增发生器（A)连通后新增发 生器 （A) 再有冷剂液管路经新增节流阀 （C) 与第一冷凝器 （4) 连通， 新增发生器 （A) 还 有冷剂蒸汽通道与第一冷凝器 （4) 连通， 形成以双效为低温发生流程的第三类吸收式热泵。  39. A third type of absorption heat pump, which is the single-effect single-effect third-type absorption heat pump of claim 1 and the third type of absorption heat pump according to any one of claims 5-12. , adding new generators, new solution heat exchangers, new throttle valves and new solution pumps, the absorber (3) has a dilute solution line through the first solution heat exchanger (10) and the first occurrence (1) Connected to the absorber (3) The dilute solution line is connected to the new generator (A) via the first solution heat exchanger (10) and the new solution heat exchanger (B). (A) and a concentrated solution line is connected to the first generator (1) via a new solution pump (D) and a new solution heat exchanger (B), and the first generator (1) has a refrigerant vapor. The passage is connected to the first condenser (4) to be adjusted to be the first generator (1). The refrigerant vapor passage is connected with the newly added generator (A), and the new generator (A) is added. The throttle valve (C) is connected to the first condenser (4), and the new generator (A) and the refrigerant vapor passage are connected to the first condenser (4). , Forming a third type of absorption heat pump with double effect as the low temperature generation process.
40. 第三类吸收式热泵， 是在权利要求 37所述的第三类吸收式热泵中， 增加新增第二 发生器、 新增第二溶液热交换器、 新增第二节流阔和新增第二溶液泵， 吸收器（3)增设稀溶 液管路经新增第二溶液热交换器（F) 与新增第二发生器 （E)连通， 新增第二发生器（E)还 有浓溶液管路经新增第二溶液泵 （H) 和新增第二溶液热交换器 （F) 之后与第一发生器 （1 ) 经溶液泵 （7) 和第一溶液热交换器 （10) 之后的浓溶液管路汇合， 将新增第一发生器 （A) 有冷剂蒸汽通道与第一冷凝器 （4) 连通调整为新增第一发生器 （A) 有冷剂蒸汽通道与新增 第二发生器（E)连通后新增第二发生器（E)再有冷剂液管路经新增第二节流阀 （G)与第一 冷凝器（4)连通， 新增第二发生器 （E) 还有冷剂蒸汽通道与第一冷凝器（4)连通， 形成以 三效为低温发生流程的第三类吸收式热泵。  40. The third type of absorption heat pump is the third type of absorption heat pump according to claim 37, wherein a second addition generator is added, a second solution heat exchanger is added, and a second section is added. Adding a second solution pump, the absorber (3) adding a dilute solution line is connected with the newly added second generator (E) by adding a second solution heat exchanger (F), and adding a second generator (E) There is also a concentrated solution line through the addition of the second solution pump (H) and the addition of the second solution heat exchanger (F) to the first generator (1) via the solution pump (7) and the first solution heat exchanger (10) After the concentrated solution pipeline merges, the new first generator (A) has a refrigerant vapor passage connected to the first condenser (4) and is adjusted to add a first generator (A) with refrigerant vapor. The second generator (E) is added after the channel is connected with the newly added second generator (E), and the refrigerant liquid pipeline is connected to the first condenser (4) by adding a second throttle valve (G). A second generator (E) is added, and a refrigerant vapor passage is connected to the first condenser (4) to form a third type of absorption heat with a three-effect low temperature generation process. .
41. 第三类吸收式热泵， 是在权利要求 38所述的第三类吸收式热泵中， 增加新增第二 发生器、 新增第二溶液热交换器和新增第二节流阔， 将新增第一发生器（A)有浓溶液管路经 溶液泵（7 )、新增第一溶液热交换器（B)和第一溶液热交换器（10)与第二溶液热交换器（11 ) 连通调整为新增第一发生器 （A) 有浓溶液管路经新增第二溶液热交换器 （F) 与新增第二发 生器 （E) 连通， 新增第二发生器 （E) 还有浓溶液管路经溶液泵 （7)、 新增第二溶液热交换 权 利 要 求 书 41. The third type of absorption heat pump is the third type of absorption heat pump according to claim 38, wherein a new second generator is added, a second solution heat exchanger is added, and a second section is added. The first generator (A) has a concentrated solution line through the solution pump (7), a new first solution heat exchanger (B), and a first solution heat exchanger (10) and a second solution heat exchanger. (11) The connection is adjusted to add a new generator (A). The concentrated solution line is connected to the newly added second generator (E) via a new second solution heat exchanger (F), and a second generator is added. (E) There is also a concentrated solution line through the solution pump (7), adding a second solution heat exchange Claim
― WO 2013/003982 PCT/CN2011/001118 器 （E)、 新增第一溶液热交换器 （B) 和第一溶液热交换器 （10) 与第二溶液热交换器 （11 ) 连通， 将新增第一发生器 （A) 有冷剂蒸汽通道与第一冷凝器 （4) 连通调整为新增第一发生 器（A)有冷剂蒸汽通道与新增第二发生器（E)连通后新增第二发生器（E) 再有冷剂液管路 经新增第二节流阀 （G) 与第一冷凝器（4)连通， 新增第二发生器 （E)还有冷剂蒸汽通道与 第一冷凝器 （4) 连通， 形成以三效为低温发生流程的第三类吸收式热泵。  ― WO 2013/003982 PCT/CN2011/001118 (E), new first solution heat exchanger (B) and first solution heat exchanger (10) connected to the second solution heat exchanger (11), will be new Increasing the first generator (A) has a refrigerant vapor passage connected to the first condenser (4) to adjust to add a first generator (A) having a refrigerant vapor passage connected to the newly added second generator (E) A second generator (E) is added, and a refrigerant liquid line is connected to the first condenser (4) via a new second throttle valve (G), and a second generator (E) and a refrigerant are added. The steam passage is in communication with the first condenser (4) to form a third type of absorption heat pump having a three-effect low temperature generation process.
42. 第三类吸收式热泵， 是在权利要求 39所述的第三类吸收式热泵中， 增加新增第二 发生器、 新增第二溶液热交换器、 新增第二节流阀和新增第二溶液泵， 将吸收器（3)有稀溶 液管路经第一溶液热交换器 （10) 和新增第一溶液热交换器 （B) 与新增第一发生器 （A) 连 通调整为吸收器 （3) 有稀溶液管路经第一溶液热交换器 （10)、 新增第一溶液热交换器 （B) 和新增第二溶液热交换器（F) 与新增第二发生器（E)连通， 新增第二发生器（E)还有浓溶 液管路经新增第二溶液泵 （H) 和新增第二溶液热交换器 （F) 与新增第一发生器 （A) 连通， 将新增第一发生器 （A) 有冷剂蒸汽通道与第一冷凝器 （4) 连通调整为新增第一发生器 （A) 有冷剂蒸汽通道与新增第二发生器 （E) 连通后新增第二发生器 （E) 再有冷剂液管路经新增 第二节流阀 （G) 与第一冷凝器 （4 )连通， 新增第二发生器 （E)还有冷剂蒸汽通道与第一冷 凝器 （4) 连通， 形成以三效为低温发生流程的第三类吸收式热泵。  42. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 39, adding a new second generator, adding a second solution heat exchanger, adding a second throttle valve, and Add a second solution pump, the absorber (3) has a dilute solution line through the first solution heat exchanger (10) and a new first solution heat exchanger (B) with a new first generator (A) Connected to the absorber (3) with a dilute solution line through the first solution heat exchanger (10), a new first solution heat exchanger (B) and a new second solution heat exchanger (F) with new The second generator (E) is connected, the second generator (E) is added, and the concentrated solution line is added by the second solution pump (H) and the second solution heat exchanger (F) is added. A generator (A) is connected, and a new first generator (A) has a refrigerant vapor passage connected to the first condenser (4) to adjust to a new first generator (A) with a refrigerant vapor passage and a new Adding the second generator (E) to connect the new generator (E) and then adding the second coolant valve (G) to the first condenser (4) Connected, a new second generator (E) and a refrigerant vapor passage are connected to the first condenser (4) to form a third type of absorption heat pump with a three-effect low temperature generation process.
43. 第三类吸收式热泵， 是在权利要求 1、 13-20内任一权利要求所述的第三类吸收式 热泵中， 增加新增发生器、 新增溶液热交换器和新增节流阀， 第二溶液泵 （14) 增设稀溶液 管路经新增溶液热交换器（B) 与新增发生器（A)连通， 新增发生器（A)还有浓溶液管路经 新增溶液热交换器 （B) 与第三发生器 （12) 连通， 将第一发生器 （1 ) 有冷剂蒸汽通道与第 一冷凝器（4)连通调整为第一发生器（1 )有冷剂蒸汽通道与新增发生器（A)连通后新增发 生器 （A) 再有冷剂液管路经新增节流阀 （C) 与第一冷凝器 （4) 连通， 新增发生器 （A) 还 有冷剂蒸汽通道与第一冷凝器（4)连通， 形成以回热式双效为低温发生流程的第三类吸收式 热泵。  43. A third type of absorption heat pump, in the third type of absorption heat pump according to any one of claims 1, 13-20, adding a new generator, a new solution heat exchanger and an additional section Flow valve, second solution pump (14) Adding dilute solution line through new solution heat exchanger (B) to connect with new generator (A), new generator (A) and concentrated solution line through new The solution heat exchanger (B) is in communication with the third generator (12), and the first generator (1) has a refrigerant vapor passage connected to the first condenser (4) to be adjusted to be the first generator (1) A new generator (A) is added after the refrigerant vapor passage is connected to the new generator (A), and the refrigerant liquid line is connected to the first condenser (4) via the newly added throttle valve (C). The refrigerant (A) also has a refrigerant vapor passage communicating with the first condenser (4) to form a third type of absorption heat pump having a regenerative double effect as a low temperature generation process.
44. 第三类吸收式热泵， 是在权利要求 1、 13- 20内任一权利要求所述的第三类吸收式 热泵中， 增加新增发生器、 新增溶液热交换器和新增节流阀， 将第二溶液泵 （14) 有稀溶液 管路经第三溶液热交换器（15) 与第一发生器（1 )连通调整为第二溶液泵 （14)有稀溶液管 路经新增溶液热交换器 （B) 和第三溶液热交换器 （15) 与第一发生器 （1 ) 连通， 将第一发 生器（1 )有浓溶液管路经第三溶液热交换器（15) 与第三发生器（12)连通调整为第一发生 器 （1 ) 有浓溶液管路经第三溶液热交换器 （15) 与新增发生器 （A) 连通， 新增发生器 （A) 还有浓溶液管路经新增溶液热交换器 （B) 与第三发生器 （12) 连通， 将第一发生器 （1 ) 有 冷剂蒸汽通道与第一冷凝器 （4) 连通调整为第一发生器 （1 ) 有冷剂蒸汽通道与新增发生器 44. A third type of absorption heat pump, which is a third type of absorption heat pump according to any one of claims 1, 13-20, adding a new generator, a new solution heat exchanger and an additional section a flow valve, the second solution pump (14) has a dilute solution line connected to the first generator (1) via the third solution heat exchanger (15) to be adjusted to a second solution pump (14) having a dilute solution line The new solution heat exchanger (B) and the third solution heat exchanger (15) are in communication with the first generator (1), and the first generator (1) has a concentrated solution line through the third solution heat exchanger ( 15) Connected to the third generator (12) to adjust to the first generator (1). The concentrated solution line is connected to the newly added generator (A) via the third solution heat exchanger (15), and a new generator is added. A) further, the concentrated solution pipeline is connected to the third generator (12) via the new solution heat exchanger (B), and the first generator (1) has a refrigerant vapor passage connected to the first condenser (4) Adjusted to the first generator (1) with refrigerant vapor channel and new generator
(A) 连通后新增发生器 （A) 再有冷剂液管路经新增节流阀 （C) 与第一冷凝器 （4) 连通， 新增发生器 （A) 还有冷剂蒸汽通道与第一冷凝器 （4) 连通， 形成以回热式双效为低温发生 流程的第三类吸收式热泵。 (A) New generator (A) after communication. Then the refrigerant liquid line is connected to the first condenser (4) via the new throttle valve (C). The new generator (A) and refrigerant vapor are added. The passage is connected to the first condenser (4) to form a third type of absorption heat pump with a regenerative double effect as a low temperature generation process.
45. 第三类吸收式热泵， 是在权利要求 1、 13-20内任一权利要求所述的第三类吸收式 热泵中，增加新增发生器、新增溶液热交换器、新增节流阀和新增溶液泵，将第二溶液泵（14) 有稀溶液管路经第三溶液热交换器（15)与第一发生器（1 )连通调整为第二溶液泵 （14)有 稀溶液管路经第三溶液热交换器 （15 ) 与新增发生器 （A) 连通， 新增发生器 （A) 还有浓溶 液管路经新增溶液泵 （D)和新增溶液热交换器（B) 与第一发生器（1 ) 连通， 将第一发生器 45. A third type of absorption heat pump, which is a third type of absorption heat pump according to any one of claims 1, 13-20, adding a new generator, a new solution heat exchanger, and an adding section a flow valve and a new solution pump, the second solution pump (14) has a dilute solution line connected to the first generator (1) via the third solution heat exchanger (15) to be adjusted to a second solution pump (14) The dilute solution line is connected to the newly added generator (A) via the third solution heat exchanger (15), the new generator (A) and the concentrated solution line are added to the new solution pump (D) and the new solution heat. The exchanger (B) is in communication with the first generator (1), and the first generator is
( 1 )有浓溶液管路经第三溶液热交换器（15 )与第三发生器（12 )连通调整为第一发生器（1 ) 权 利 要 求 书 (1) The concentrated solution line is connected to the third generator (12) via the third solution heat exchanger (15) to be adjusted to the first generator (1) Claim
_ WO 2013/003982 PCT/CN2011/001118 有浓溶液管路经新增溶液热交换器（B)和第三溶液热交换器（15)与第三发生器（12)连通, 将第一发生器（1 )有冷剂蒸汽通道与第一冷凝器（4)连通调整为第一发生器（1 )有冷剂蒸 汽通道与新增发生器（A)连通后新增发生器（A)再有冷剂液管路经新增节流阀 （C) 与第一 冷凝器（4)连通， 新增发生器（A)还有冷剂蒸汽通道与第一冷凝器（4 )连通， 形成以回热 式双效为低温发生流程的第三类吸收式热泵。  _ WO 2013/003982 PCT/CN2011/001118 The concentrated solution line is connected to the third generator (12) via the new solution heat exchanger (B) and the third solution heat exchanger (15), the first generator (1) The refrigerant vapor passage is connected to the first condenser (4) to be adjusted to be the first generator (1). The refrigerant vapor passage is connected with the newly added generator (A), and the new generator (A) is further The refrigerant liquid pipeline is connected to the first condenser (4) via a new throttle valve (C), and a new generator (A) and a refrigerant vapor passage are connected to the first condenser (4) to form a return. The thermal double effect is the third type of absorption heat pump for the low temperature generation process.
46. 第三类吸收式热泵，是在权利要求 43- 45内任一权利要求所述的第三类吸收式热泵 中， 取消第三发生器 （12) 与外部连通的余热介质管路， 增加新增第二节流阀， 第一发生器 The third type of absorption heat pump is the third type of absorption heat pump according to any one of claims 43 to 45, wherein the residual heat medium line connecting the third generator (12) to the outside is canceled, New second throttle valve, first generator
( 1 )增设冷剂蒸汽通道与第三发生器（12 )连通后第三发生器（12)再有冷剂液管路经新增 第二节流阀 （G) 与第一冷凝器 （4) 连通， 形成以回热式双效为低温发生流程的第三类吸收 式热泵。 (1) Adding a refrigerant vapor passage to communicate with the third generator (12), the third generator (12) and the refrigerant liquid pipeline are further added with a second throttle valve (G) and a first condenser (4) Connected to form a third type of absorption heat pump with a regenerative double effect as a low temperature generation process.
47. 第三类吸收式热泵， 是在权利要求 43所述的第三类吸收式热泵中， 增加新增第二 发生器、 新增第二溶液热交换器和新增第二节流阀， 第二溶液泵 （14) 增设稀溶液管路经新 增第二溶液热交换器（F) 与新增第二发生器（E)连通， 新增第二发生器（E)还有浓溶液管 路经新增第二溶液热交换器 （F) 与第三发生器 （12) 连通， 将新增第一发生器 （A) 有冷剂 蒸汽通道与第一冷凝器 （4) 连通调整为新增第一发生器 （A) 有冷剂蒸汽通道与新增第二发 生器（E)连通后新增第二发生器（E) 再有冷剂液管路经新增第二节流阀 （G) 与第一冷凝器 47. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 43, wherein a second addition generator, a second addition solution heat exchanger, and a second addition throttle valve are added. The second solution pump (14) adds a dilute solution line to the newly added second generator (E) via the addition of the second solution heat exchanger (F), and adds a second generator (E) and a concentrated solution tube. The second solution heat exchanger (F) is connected to the third generator (12), and the new first generator (A) has a refrigerant vapor passage connected to the first condenser (4) and is adjusted to be new. The first generator (A) has a refrigerant vapor passage connected to the newly added second generator (E), and a second generator (E) is added. Then, the refrigerant liquid pipeline is added with a second throttle valve ( G) with the first condenser
(4)连通， 新增第二发生器（E)还有冷剂蒸汽通道与第一冷凝器（4)连通， 形成以回热式 三效为低温发生流程的第三类吸收式热泵。 (4) Connect, add a second generator (E) and a refrigerant vapor passage to communicate with the first condenser (4) to form a third type of absorption heat pump with a regenerative three-effect low temperature generation process.
48. 第三类吸收式热泵， 是在权利要求 44所述的第三类吸收式热泵中， 增加新增第二 发生器、 新增第二溶液热交换器和新增第二节流阀， 将第二溶液泵 （14) 有稀溶液管路经新 增第一溶液热交换器 （B) 和第三溶液热交换器 （15 ) 与第一发生器 （1 ) 连通调整为第二溶 液泵（14)有稀溶液管路经新增第二溶液热交换器（F)、 新增第一溶液热交换器（B)和第三 溶液热交换器 （15 ) 与第一发生器 （1 ) 连通， 将新增第一发生器 （A) 有浓溶液管路经新增 第一溶液热交换器 （B) 与第三发生器 （12 ) 连通调整为新增第一发生器 （A) 有浓溶液管路 经新增第一溶液热交换器（B)与新增第二发生器（E)连通， 新增第二发生器 （E)还有浓溶 液管路经新增第二溶液热交换器 （F) 与第三发生器 （12 ) 连通， 将新增第一发生器 （A) 有 冷剂蒸汽通道与第一冷凝器 （4) 连通调整为新增第一发生器 （A) 有冷剂蒸汽通道与新增第 二发生器（E)连通后新增第二发生器（E) 再有冷剂液管路经新增第二节流阀 （G)与第一冷 凝器（4)连通， 新增第二发生器 （E)还有冷剂蒸汽通道与第一冷凝器（4 )连通， 形成以回 热式三效为低温发生流程的第三类吸收式热泵。  48. The third type of absorption heat pump is the third type of absorption heat pump according to claim 44, wherein a new second generator is added, a second solution heat exchanger is added, and a second throttle valve is added. The second solution pump (14) has a dilute solution line connected to the first generator (1) via the newly added first solution heat exchanger (B) and the third solution heat exchanger (15) to be adjusted into a second solution pump (14) a dilute solution line is added with a second solution heat exchanger (F), a new first solution heat exchanger (B) and a third solution heat exchanger (15) and a first generator (1) Connected, the first generator (A) has a new concentrated solution. The new first heat exchanger (B) is connected to the third generator (12) to adjust to the new first generator (A). The concentrated solution pipeline is connected to the newly added second generator (E) by adding the first solution heat exchanger (B), and the second generator (E) and the concentrated solution pipeline are added with the second solution heat. The exchanger (F) is in communication with the third generator (12), and the first new generator (A) has a refrigerant vapor passage connected to the first condenser (4) Adjusted to add the first generator (A). There is a refrigerant vapor channel connected to the new second generator (E). The second generator (E) is added. The flow valve (G) is in communication with the first condenser (4), and the second generator (E) and the refrigerant vapor passage are connected to the first condenser (4) to form a regenerative three-effect low temperature. The third type of absorption heat pump for the process.
49. 第三类吸收式热泵， 是在权利要求 45所述的第三类吸收式热泵中， 增加新增第二 发生器、 新增第二溶液热交换器、 新增第二节流阀和新增第二溶液泵， 将第二溶液泵 （14) 有稀溶液管路经第三溶液热交换器（15 )与新增第一发生器（A)连通调整为第二溶液泵（14) 有稀溶液管路经第三溶液热交换器（15 ) 与新增第二发生器（E)连通， 新增第二发生器（E) 还有浓溶液管路经新增第二溶液泵（H)和新增第二溶液热交换器（F)与新增第一发生器（A) 连通， 将第一发生器 （1 ) 有浓溶液管路经新增第一溶液热交换器 （B) 和第三溶液热交换器 49. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 45, adding a new second generator, adding a second solution heat exchanger, adding a second throttle valve, and a second solution pump is added, and the second solution pump (14) has a dilute solution line connected to the newly added first generator (A) via the third solution heat exchanger (15) to be adjusted into a second solution pump (14) The dilute solution line is connected to the newly added second generator (E) via the third solution heat exchanger (15), the second generator (E) is added, and the concentrated solution line is added by the second solution pump ( H) and the newly added second solution heat exchanger (F) is connected with the newly added first generator (A), and the first generator (1) has a concentrated solution line through the newly added first solution heat exchanger (B) And the third solution heat exchanger
( 15)与第三发生器（12 )连通调整为第二发生器（2 )有浓溶液管路经新增第一溶液热交换 器 （B)、 新增第二溶液热交换器 （F) 和第三溶液热交换器 （15 ) 与第三发生器 （12) 连通， 将新增第一发生器 （A) 有冷剂蒸汽通道与第一冷凝器 （4) 连通调整为新增第一发生器 （A) 有冷剂蒸汽通道与新增第二发生器 （E) 连通后新增第二发生器 （E) 再有冷剂液管路经新增 权 利 要 求 书 (15) communicating with the third generator (12) to adjust to the second generator (2) having a concentrated solution line by adding a first solution heat exchanger (B), adding a second solution heat exchanger (F) And the third solution heat exchanger (15) is in communication with the third generator (12), and the newly added first generator (A) has a refrigerant vapor passage connected to the first condenser (4) to be newly added first Generator (A) has a refrigerant vapor channel connected to the new second generator (E) and adds a second generator (E). Claim
_WO 201 /003982 PCT/CN2011/001118  _WO 201 /003982 PCT/CN2011/001118
第二节流阀 （G) 与第一冷凝器 （4)连通， 新增第二发生器（E)还有冷剂蒸汽通道与第一冷 凝器 （4) 连通， 形成以回热式三效为低温发生流程的第三类吸收式热泵。 The second throttle valve (G) is in communication with the first condenser (4), and the second generator (E) and the refrigerant vapor passage are connected to the first condenser (4) to form a regenerative three-effect The third type of absorption heat pump for low temperature generation processes.
50. 第三类吸收式热泵，是在权利要求 47-49内任一权利要求所述的第三类吸收式热泵 中， 取消第三发生器 （12) 与外部连通的余热介质管路， 增加新增第三节流阀， 第一发生器 50. The third type of absorption heat pump is the third type of absorption heat pump according to any one of claims 47-49, wherein the residual heat medium pipeline connecting the third generator (12) to the outside is eliminated, New third throttle valve, first generator
( 1 )增设冷剂蒸汽通道与第三发生器（12)连通后第三发生器（12 )再有冷剂液管路经新增 第三节流阀 （I ) 与第一冷凝器 （4) 连通， 形成以三效为低温发生流程的回热式第三类吸收 式热泵。 (1) Adding a refrigerant vapor passage to communicate with the third generator (12), the third generator (12) and the refrigerant liquid pipeline are further added with a third throttle valve (I) and a first condenser (4) Connected to form a regenerative third-type absorption heat pump with a three-effect process for low temperature generation.
51. 第三类吸收式热泵，是在权利要求 47-49内任一权利要求所述的第三类吸收式热泵 中， 取消第三发生器 （12) 与外部连通的余热介质管路， 增加新增第三节流阀， 新增第一发 生器（A)增设冷剂蒸汽通道与第三发生器（12)连通后第三发生器（12) 再有冷剂液管路经 新增第三节流阀 （I ) 与第一冷凝器 （4) 连通， 形成以回热式三效为低温发生流程的第三类 吸收式热泵。  The third type of absorption heat pump is the third type of absorption heat pump according to any one of claims 47 to 49, wherein the residual heat medium pipe connecting the third generator (12) to the outside is cancelled, A third throttle valve is added, a new first generator (A) is added to add a refrigerant vapor passage to the third generator (12), and a third generator (12) is further provided with a refrigerant liquid pipeline. The three-way valve (I) is in communication with the first condenser (4) to form a third type of absorption heat pump with a regenerative three-effect process for low temperature generation.
52. 第三类吸收式热泵， 是在权利要求 2-3、 21-28内任一权利要求所述的第三类吸收 式热泵中， 增加新增发生器、 新增溶液热交换器和新增节流阔， 将第一发生器（1 )有浓溶液 管路经第一溶液泵 （7)、 第一溶液热交换器（10)和吸收-发生器 （16) 与分汽室 （17)连通 调整为第一发生器 （1 ) 有浓溶液管路经第一溶液热交换器 （10) 和吸收-发生器 （16) 与分 汽室 （17) 连通， 吸收-发生器 （16) 增设稀溶液管路经新增溶液热交换器 （B) 与新增发生 器 （A)连通， 新增发生器（A)还有浓溶液管路经第一溶液泵 （7) 和新增溶液热交换器 （B) 之后与第一发生器（1 )经第一溶液热交换器（10)之后的浓溶液管路汇合，将第一发生器（1 ) 有冷剂蒸汽通道与第一冷凝器 （4) 连通调整为第一发生器 （1 ) 有冷剂蒸汽通道与新增发生 器（A)连通后新增发生器（A) 再有冷剂液管路经新增节流闽 (C) 与第一冷凝器（4)连通， 新增发生器 （A) 还有冷剂蒸汽通道与第一冷凝器 （4) 连通， 形成以回热式双效为低温发生 流程的第三类吸收式热泵。  52. A third type of absorption heat pump, which is a third type of absorption heat pump according to any one of claims 2-3, 21-28, adding a new generator, a new solution heat exchanger and a new one. Increasing the flow, the first generator (1) has a concentrated solution line through the first solution pump (7), the first solution heat exchanger (10) and the absorption-generator (16) and the steam separation chamber (17) The communication is adjusted to the first generator (1). The concentrated solution line is connected to the steam distribution chamber (17) via the first solution heat exchanger (10) and the absorption-generator (16), and the absorption-generator (16) Adding a dilute solution line through the new solution heat exchanger (B) to the new generator (A), adding a new generator (A) and a concentrated solution line through the first solution pump (7) and adding a new solution The heat exchanger (B) is then merged with the first generator (1) through the concentrated solution line after the first solution heat exchanger (10), and the first generator (1) has a refrigerant vapor passage and a first condensation (4) Connected to the first generator (1) With the refrigerant vapor channel connected to the new generator (A), the generator (A) is added and the refrigerant is added. The pipeline is connected to the first condenser (4) via a new throttle (C), and a new generator (A) and a refrigerant vapor passage are connected to the first condenser (4) to form a double-heating type. The third type of absorption heat pump that functions as a low temperature generation process.
53. 第三类吸收式热泵， 是在权利要求 2-3、 21- 28内任一权利要求所述的第三类吸收 式热泵中， 增加新增发生器、 新增节流阀和新增溶液节流阀， 将第一发生器（1 )有浓溶液管 路经第一溶液泵 （7 )、 第一溶液热交换器 （10) 和吸收-发生器 （16) 与分汽室 （17 ) 连通调 整为第一发生器 （1 ) 有浓溶液管路经溶液节流阀 （J) 和吸收-发生器 （16) 与分汽室 （17) 连通， 将吸收-发生器 （16) 有稀溶液管路经第一溶液热交换器 （10) 与第一发生器 （1 ) 连 通调整为吸收-发生器 （16) 有稀溶液管路直接与第一发生器 （1 ) 连通， 吸收-发生器 （16) 增设稀溶液管路经第一溶液热交换器 （10) 与新增发生器 （A) 连通， 新增发生器 （A) 还有 浓溶液管路经第一溶液泵 （7) 和第一溶液热交换器 （10) 之后与第一发生器 （1 ) 经溶液节 流阀 （J)之后的浓溶液管路汇合， 将第一发生器（1 )有冷剂蒸汽通道与第一冷凝器（4)连 通调整为第一发生器（1 )有冷剂蒸汽通道与新增发生器（A)连通后新增发生器（A)再有冷 剂液管路经新增节流阀 （C) 与第一冷凝器（4)连通， 新增发生器 （A)还有冷剂蒸汽通道与 第一冷凝器 （4) 连通； 取消第一蒸发器 （6) 或第二蒸发器 （19 ) 与吸收-发生器（16)连通 的冷剂蒸汽通道， 第一发生器 （1 ) 增设冷剂蒸汽通道与吸收-发生器 （16) 连通， 取消第三 溶液泵 （21 )， 吸收器（3)有稀溶液管路经第三溶液热交换器（15) 与吸收-发生器 （16)连 通， 形成以回热式双效为低温发生流程的第三类吸收式热泵。  53. The third type of absorption heat pump is a third type of absorption heat pump according to any one of claims 2-3, 21-28, adding a new generator, adding a new throttle valve and adding a solution throttle valve, the first generator (1) has a concentrated solution line through the first solution pump (7), the first solution heat exchanger (10), and the absorption-generator (16) and the steam separation chamber (17) The connection is adjusted to the first generator (1). The concentrated solution line is connected to the steam distribution chamber (17) via the solution throttle valve (J) and the absorption-generator (16), and the absorption-generator (16) is provided. The dilute solution line is connected to the first generator (1) via the first solution heat exchanger (10) to be adjusted as an absorption-generator (16) having a dilute solution line directly communicating with the first generator (1), absorbing - The generator (16) adds a dilute solution line to the new generator (A) via the first solution heat exchanger (10), and adds a new generator (A) and a concentrated solution line through the first solution pump (7). And the first solution heat exchanger (10) is then merged with the first generator (1) through the concentrated solution line after the solution throttle (J), The first generator (1) has a refrigerant vapor passage connected to the first condenser (4) and is adjusted to be a first generator (1) having a refrigerant vapor passage connected with the newly added generator (A) to add a new generator (A) The refrigerant liquid line is connected to the first condenser (4) via a new throttle valve (C), and the new generator (A) has a refrigerant vapor passage and a first condenser (4). Connected; cancels the refrigerant vapor passage of the first evaporator (6) or the second evaporator (19) and the absorption-generator (16), and the first generator (1) adds a refrigerant vapor passage and an absorption-generator (16) Connect, cancel the third solution pump (21), and the absorber (3) has a dilute solution line connected to the absorption-generator (16) through the third solution heat exchanger (15) to form a double-heating type The third type of absorption heat pump that functions as a low temperature generation process.
54. 第三类吸收式热泵， 是在权利要求 2-3、 21-28内任一权利要求所述的第三类吸收 式热泵中， 增加新增发生器、 新增溶液热交换器和新增节流阀， 将第一发生器（1 )有浓溶液 权 利 要 求 书 54. A third type of absorption heat pump, which is a third type of absorption heat pump according to any one of claims 2-3, 21-28, adding a new generator, a new solution heat exchanger and a new one. Increase the throttle valve, the first generator (1) has a concentrated solution Claim
― WO 2013/003982 PCT/CN2011/001118 管路经第一溶液泵 （7 )、 第一溶液热交换器（10) 和吸收-发生器（16) 与分汽室 （17)连通 调整为第一发生器（1 )有浓溶液管路经新增溶液热交换器（B) 与新增发生器（A)连通， 新 增发生器（A)还有浓溶液管路经第一溶液泵（7)、 新增溶液热交换器（B)、 第一溶液热交换 器 （10) 和吸收-发生器 （16) 与分汽室 （17 ) 连通， 将第一发生器 （1 ) 有冷剂蒸汽通道与 第一冷凝器（4)连通调整为第一发生器（1 )有冷剂蒸汽通道与新增发生器（A)连通后新增 发生器 （A) 再有冷剂液管路经新增节流阔 (C) 与第一冷凝器 （4) 连通， 新增发生器 （A) 还有冷剂蒸汽通道与第一冷凝器（4)连通， 形成以回热式双效为低温发生流程的第三类吸收 式热泵。  ― WO 2013/003982 PCT/CN2011/001118 The pipeline is connected to the first solution pump (7), the first solution heat exchanger (10) and the absorption-generator (16) and the steam distribution chamber (17) to adjust to the first The generator (1) has a concentrated solution line connected to the new generator (A) via the new solution heat exchanger (B), and a new generator (A) and a concentrated solution line through the first solution pump (7) The new solution heat exchanger (B), the first solution heat exchanger (10) and the absorption-generator (16) are in communication with the steam distribution chamber (17), and the first generator (1) has refrigerant vapor The passage is connected to the first condenser (4) to be adjusted to be the first generator (1). The refrigerant vapor passage is connected with the newly added generator (A), and the new generator (A) is added. The additional section (C) is in communication with the first condenser (4), and the new generator (A) and the refrigerant vapor passage are connected to the first condenser (4) to form a regenerative double effect for low temperature generation. The third type of absorption heat pump for the process.
55. 第三类吸收式热泵， 是在权利要求 2-3、 21-28内任一权利要求所述的第三类吸收 式热泵中， 增加新增发生器和新增节流阀， 将吸收-发生器（16)有稀溶液管路经第一溶液热 交换器 （10) 与第一发生器 （1 ) 连通调整为吸收-发生器 （16) 有稀溶液管路直接与第一发 生器（1 )连通， 将第一发生器（1 )有浓溶液管路经第一溶液泵（7)、第一溶液热交换器（10) 和吸收-发生器 （16) 与分汽室 （17) 连通调整为第一发生器 （1 ) 有浓溶液管路经第一溶液 热交换器（10)与新增发生器（A)连通， 新增发生器（A)还有浓溶液管路经第一溶液泵（7)、 第一溶液热交换器 （10) 和吸收-发生器 （16) 与分汽室 （17 ) 连通， 将第一发生器 （1 ) 有 冷剂蒸汽通道与第一冷凝器 （4 ) 连通调整为第一发生器 （1 ) 有冷剂蒸汽通道与新增发生器 55. The third type of absorption heat pump is the third type of absorption heat pump according to any one of claims 2-3, 21-28, adding a new generator and adding a new throttle valve, which will absorb - the generator (16) has a dilute solution line connected to the first generator (1) via the first solution heat exchanger (10) to adjust to an absorption-generator (16) having a dilute solution line directly to the first generator (1) Connected, the first generator (1) has a concentrated solution line through the first solution pump (7), the first solution heat exchanger (10), and the absorption-generator (16) and the steam separation chamber (17) The connection is adjusted to the first generator (1). The concentrated solution line is connected to the newly added generator (A) via the first solution heat exchanger (10), and the new generator (A) and the concentrated solution line are added. The first solution pump (7), the first solution heat exchanger (10) and the absorption-generator (16) are in communication with the steam distribution chamber (17), and the first generator (1) has a refrigerant vapor passage and the first The condenser (4) is connected to the first generator (1) with a refrigerant vapor channel and a new generator
(A) 连通后新增发生器 （A) 再有冷剂液管路经新增节流阀 （C) 与第一冷凝器 （4) 连通， 新增发生器（A)还有冷剂蒸汽通道与第一冷凝器 （4)连通； 取消第一蒸发器（6)或第二蒸 发器 （19) 与吸收-发生器 （16) 连通的冷剂蒸汽通道， 第一发生器 （1 ) 增设冷剂蒸汽通道 与吸收-发生器 （16) 连通， 取消第三溶液泵， 吸收器 （3) 有稀溶液管路经第三溶液热交换 器（15 )与吸收-发生器（16)连通， 形成以回热式双效为低温发生流程的第三类吸收式热泵。 (A) New generator after connection (A) The coolant line is connected to the first condenser (4) via the new throttle valve (C). The new generator (A) and refrigerant vapor are added. The passage is in communication with the first condenser (4); canceling the refrigerant vapor passage of the first evaporator (6) or the second evaporator (19) and the absorption-generator (16), the first generator (1) is added The refrigerant vapor passage is connected to the absorption-generator (16) to cancel the third solution pump, and the absorber (3) has a dilute solution line connected to the absorption-generator (16) via the third solution heat exchanger (15). A third type of absorption heat pump with a regenerative double effect as a low temperature generation process is formed.
56. 第三类吸收式热泵， 是在权利要求 2-3、 21-28内任一权利要求所述的第三类吸收 式热泵中， 增加新增发生器、 新增溶液热交换器、 新增节流阀和新增溶液泵， 将吸收-发生器 56. A third type of absorption heat pump, which is a third type of absorption heat pump according to any one of claims 2-3, 21-28, adding a new generator, a new solution heat exchanger, a new Increased throttle valve and new solution pump, will absorb-generator
( 16) 有稀溶液管路经第一溶液热交换器 （10) 与第一发生器 （1 ) 连通调整为吸收-发生器 ( 16) 有稀溶液管路第一溶液热交换器 （10) 和新增溶液热交换器 （B) 与新增发生器 （A) 连通， 新增发生器（A)还有浓溶液管路经新增溶液泵 （D)和新增溶液热交换器（B) 与第一 发生器（1 )连通， 将第一发生器（1 )有冷剂蒸汽通道与第一冷凝器（4)连通调整为第一发 生器（1 )有冷剂蒸汽通道与新增发生器（A)连通后新增发生器（A)再有冷剂液管路经新增 节流阀 （C) 与第一冷凝器 （4) 连通， 新增发生器（A) 还有冷剂蒸汽通道与第一冷凝器 （4) 连通， 形成以回热式双效为低温发生流程的第三类吸收式热泵。 (16) The dilute solution line is connected to the first generator (1) via the first solution heat exchanger (10) to be adjusted to the absorption-generator (16). The dilute solution line first solution heat exchanger (10) And the new solution heat exchanger (B) is connected to the new generator (A), the new generator (A) and the concentrated solution line are added to the new solution pump (D) and the new solution heat exchanger (B). Connecting with the first generator (1), connecting the first generator (1) with the refrigerant vapor passage and the first condenser (4) to adjust to the first generator (1) having the refrigerant vapor passage and adding After the generator (A) is connected, the generator (A) is added, and then the refrigerant liquid line is connected to the first condenser (4) via the newly added throttle valve (C), and the new generator (A) is also cooled. The agent vapor channel is in communication with the first condenser (4) to form a third type of absorption heat pump with a regenerative double effect as a low temperature generation process.
57. 第三类吸收式热泵， 是在权利要求 2-3、 21-28内任一权利要求所述的第三类吸收 式热泵中， 增加新增发生器、 新增溶液节流阀和新增节流阀， 将第一发生器（1 )有浓溶液管 路经第一溶液泵 （7)、 第一溶液热交换器（10)和吸收-发生器 （16) 与分汽室 （17 )连通调 整为第一发生器（1 )有浓溶液管路经新增溶液节流阀（J)和吸收-发生器（16)与分汽室（17 ) 连通， 将吸收-发生器 （16) 有稀溶液管路经第一溶液热交换器 （10) 与第一发生器 （1 ) 连 通调整为吸收-发生器（16)有稀溶液管路第一溶液热交换器（10) 与新增发生器（A)连通， 新增发生器 （A) 还有浓溶液管路经第一溶液泵 （7 ) 和第一溶液热交换器 （10) 与第一发生 器（1 )连通， 将第一发生器 （1 )有冷剂蒸汽通道与第一冷凝器（4)连通调整为第一发生器 57. A third type of absorption heat pump, which is a third type of absorption heat pump according to any one of claims 2-3, 21-28, adding a new generator, a new solution throttle valve and a new one. The throttle valve is added, and the first generator (1) has a concentrated solution pipeline through the first solution pump (7), the first solution heat exchanger (10), and the absorption-generator (16) and the steam distribution chamber (17). The communication is adjusted to be that the first generator (1) has a concentrated solution line connected to the steam distribution chamber (17) via the new solution throttle valve (J) and the absorption-generator (16), and the absorption-generator (16) a dilute solution line is connected to the first generator (1) via the first solution heat exchanger (10) to be adjusted to an absorption-generator (16) having a dilute solution line first solution heat exchanger (10) and new The generator (A) is connected, the new generator (A) and the concentrated solution line are connected to the first generator (1) via the first solution pump (7) and the first solution heat exchanger (10), The first generator (1) has a refrigerant vapor passage connected to the first condenser (4) to be adjusted to the first generator
( 1 )有冷剂蒸汽通道与新增发生器（A)连通后新增发生器（A) 再有冷剂液管路经新增节流 m (C) 与第一冷凝器 （4 ) 连通， 新增发生器 （A) 还有冷剂蒸汽通道与第一冷凝器 （4) 连 权 利 要 求 书 (1) A new generator (A) is added after the refrigerant vapor passage is connected with the new generator (A), and the refrigerant liquid pipeline is connected to the first condenser (4) via the newly added throttle m (C). , new generator (A) and refrigerant vapor channel connected to the first condenser (4) Claim
_ WO 2013/003982 PCT/CN2011/001118 通； 取消第一蒸发器 （6) 或第二蒸发器 （19 ) 与吸收-发生器 （16) 连通的冷剂蒸汽通道， 第一发生器（1 )增设冷剂蒸汽通道与吸收-发生器（16)连通， 取消第三溶液泵， 吸收器（3) 有稀溶液管路经第三溶液热交换器（15 ) 与吸收-发生器（16)连通， 形成以回热式双效为低 温发生流程的第三类吸收式热泵。  _ WO 2013/003982 PCT/CN2011/001118 pass; cancel the first evaporator (6) or the second evaporator (19) and the absorption-generator (16) in the refrigerant vapor channel, the first generator (1) An additional refrigerant vapor passage is connected to the absorption-generator (16) to cancel the third solution pump, and the absorber (3) has a dilute solution line connected to the absorption-generator (16) via the third solution heat exchanger (15) A third type of absorption heat pump with a regenerative double effect as a low temperature generation process is formed.
58. 第三类吸收式热泵， 是在权利要求 52所述的第三类吸收式热泵中， 增加新增第二 发生器、 新增第二溶液热交换器和新增第二节流阀， 将新增第一发生器（A)有浓溶液管路经 第一溶液泵（7)和新增第一溶液热交换器（B)之后与第一发生器（1 )经第一溶液热交换器 58. The third type of absorption heat pump is the third type of absorption heat pump according to claim 52, wherein a new second generator is added, a second solution heat exchanger is added, and a second throttle valve is added. The first generator (A) has a concentrated solution line through the first solution pump (7) and the first solution heat exchanger (B) is added, and the first generator (1) is exchanged with the first solution through the first solution. Device
( 10)之后的浓溶液管路汇合调整为新增第一发生器（A)有浓溶液管路经新增第一溶液热交 换器（B)之后与第一发生器（1 )经第一溶液热交换器（10)之后的浓溶液管路汇合， 吸收- 发生器 （16) 增设稀溶液管路经新增第二溶液热交换器 （F) 与新增第二发生器 （E) 连通， 新增第二发生器（E)还有浓溶液管路经第一溶液泵（7)和新增第二溶液热交换器（F)之后 与第一发生器（1 )经第一溶液热交换器（10)之后的浓溶液管路汇合，将新增第一发生器（A) 有冷剂蒸汽通道与第一冷凝器 （4) 连通调整为新增第一发生器 （A) 有冷剂蒸汽通道与新增 第二发生器（E)连通后新增第二发生器（E) 再有冷剂液管路经新增第二节流阀 （G) 与第一 冷凝器（4)连通， 新增第二发生器（E)还有冷剂蒸汽通道与第一冷凝器 （4) 连通， 形成以 回热式三效为低温发生流程的第三类吸收式热泵。 (10) After the confluence of the concentrated solution pipeline is adjusted to add the first generator (A) with the concentrated solution pipeline after adding the first solution heat exchanger (B) and the first generator (1) after the first The concentrated solution line after the solution heat exchanger (10) merges, and the absorption-generator (16) adds a dilute solution line through the newly added second solution heat exchanger (F) to the newly added second generator (E). , adding a second generator (E) and a concentrated solution line through the first solution pump (7) and adding a second solution heat exchanger (F) and the first generator (1) is heated by the first solution The concentrated solution line after the exchanger (10) merges, and the first new generator (A) has a refrigerant vapor passage connected to the first condenser (4) to be adjusted to add a new first generator (A). The second steam generator (E) is connected to the newly added second generator (E), and the second coolant (G) and the first condenser (4) are added to the refrigerant liquid line. Connected, a new second generator (E) and a refrigerant vapor passage are connected to the first condenser (4) to form a third type of absorption type with a regenerative three-effect process for low temperature generation. Heat pump.
59. 第三类吸收式热泵， 是在权利要求 53所述的第三类吸收式热泵中， 增加新增第二 发生器、 新增溶液热交换器和新增第二节流阔， 将新增第一发生器（A)有浓溶液管路经第一 溶液泵 （7)和第一溶液热交换器 （10) 与第一发生器 （1 ) 经新增溶液节流阀 （J)之后的浓 溶液管路汇合调整为新增第一发生器（A)有浓溶液管路经第一溶液热交换器（10)之后与第 一发生器（1 )经新增溶液节流阀 （J)之后的浓溶液管路汇合， 吸收-发生器（16)增设稀溶 液管路经新增溶液热交换器（B) 与新增第二发生器（E)连通， 新增第二发生器（E)还有浓 溶液管路经第一溶液泵 （7)和新增溶液热交换器（B)之后与第一发生器（1 )经新增溶液节 流阀（J)之后的浓溶液管路汇合， 将新增第一发生器（A)有冷剂蒸汽通道与第一冷凝器（4) 连通调整为新增第一发生器 （A) 有冷剂蒸汽通道与新增第二发生器 （E) 连通后新增第二发 生器（E)再有冷剂液管路经新增第二节流阀 （G) 与第一冷凝器（4)连通， 新增第二发生器 59. The third type of absorption heat pump is the third type of absorption heat pump according to claim 53, adding a new second generator, adding a new solution heat exchanger and adding a second section to the flow, which will be new Increasing the first generator (A) after the concentrated solution line is passed through the first solution pump (7) and the first solution heat exchanger (10) and the first generator (1) after adding the solution throttle valve (J) Concentrated solution pipeline confluence is adjusted to add a first generator (A) with a concentrated solution pipeline through the first solution heat exchanger (10) and a first generator (1) via a new solution throttle valve (J After the concentrated solution line meets, the absorption-generator (16) adds a dilute solution line through the new solution heat exchanger (B) to the new second generator (E), adding a second generator ( E) there is also a concentrated solution tube after the first solution pump (7) and the new solution heat exchanger (B) and the first generator (1) after the new solution throttle valve (J) Road junction, the first new generator (A) has a refrigerant vapor channel connected to the first condenser (4) to adjust to add a new generator (A) with refrigerant vapor The second generator (E) is added after the circuit is connected with the newly added second generator (E), and the refrigerant liquid pipeline is connected to the first condenser (4) by adding a second throttle valve (G). Add a second generator
(E) 还有冷剂蒸汽通道与第一冷凝器 （4) 连通， 形成以回热式三效为低温发生流程的第三 类吸收式热泵。 (E) There is also a refrigerant vapor passage communicating with the first condenser (4) to form a third type of absorption heat pump having a regenerative three-effect low temperature generation process.
60. 第三类吸收式热泵， 是在权利要求 59所述的第三类吸收式热泵中， 将吸收-发生器 ( 16) 有稀溶液管路直接与第一发生器 （1 ) 连通调整为吸收-发生器 （16) 有稀溶液管路经 第一溶液热交换器 （10) 与第一发生器 （1 ) 连通， 将第一发生器 （1 ) 有浓溶液管路经新增 溶液节流阀 （J) 和吸收-发生器 （16) 与分汽室 （17)连通调整为第一发生器 （1 )有浓溶液 管路经第一溶液热交换器 （10) 和吸收-发生器 （16) 与分汽室 （17) 连通， 将吸收-发生器 ( 16) 有稀溶液管路经第一溶液热交换器 （10) 与新增第一发生器 （A) 连通调整为吸收-发 生器 （16) 有稀溶液管路直接与新增第一发生器 （A) 连通， 将新增第一发生器 （A) 有浓溶 液管路经第一溶液热交换器（10)和吸收-发生器（16) 与分汽室 （17 )连通调整为新增第一 发生器（A)有浓溶液管路经新增溶液节流阀（J)和吸收-发生器（16)与分汽室（17 )连通， 将第一发生器（1 )有冷剂蒸汽通道与吸收-发生器（16)连通调整为新增第一发生器（A)有 冷剂蒸汽通道与吸收-发生器（16)连通， 形成以回热式三效为低温发生流程的第三类吸收式 热泵。 权 利 要 求 书 60. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 59, wherein the absorption-generator (16) having a dilute solution line is directly connected to the first generator (1) to be adjusted to The absorption-generator (16) has a dilute solution line connected to the first generator (1) via the first solution heat exchanger (10), and the first generator (1) has a concentrated solution line through the new solution section The flow valve (J) and the absorption-generator (16) are connected to the steam distribution chamber (17) to be adjusted to a first generator (1) having a concentrated solution line through the first solution heat exchanger (10) and an absorption-generator (16) Connected to the steam distribution chamber (17), and the absorption-generator (16) dilute solution line is connected to the newly added first generator (A) through the first solution heat exchanger (10) to be absorbed. The generator (16) has a dilute solution line directly connected to the newly added first generator (A), and the first generator (A) is added with a concentrated solution line through the first solution heat exchanger (10) and absorbed. - The generator (16) is connected to the steam distribution chamber (17) to adjust the new first generator (A) with a concentrated solution line through the new solution throttle valve (J) and absorption-generator (16) The steam dividing chamber (17) is connected, and the first generator (1) has a refrigerant vapor channel and the absorption-generator (16) is connected to be adjusted to add a first generator (A) having a refrigerant vapor channel and absorption-occurring The device (16) is connected to form a third type of absorption heat pump with a regenerative three-effect process as a low temperature generation process. Claim
WO 2013/003982 PCT/CN2011/001118  WO 2013/003982 PCT/CN2011/001118
61. 第三类吸收式热泵， 是在权利要求 54所述的第三类吸收式热泵中， 增加新增第二 发生器、 新增第二溶液热交换器和新增第二节流阀， 将新增第一发生器（A)有浓溶液管路经 第一溶液泵 （7) 和新增第一溶液热交换器 （B) 与第一溶液热交换器 （10) 连通调整为新增 第一发生器 （A) 有浓溶液管路经新增第二溶液热交换器 （F) 与新增第二发生器 （E) 连通， 新增第二发生器 （E) 还有浓溶液管路经第一溶液泵 （7)、 新增第二溶液热交换器 （F) 和新 增第一溶液热交换器 （B) 与第一溶液热交换器 （10) 连通， 将新增第一发生器 （A) 有冷剂 蒸汽通道与第一冷凝器 （4) 连通调整为新增第一发生器 （A) 有冷剂蒸汽通道与新增第二发 生器（E)连通后新增第二发生器（E) 再有冷剂液管路经新增第二节流阀 （G)与第一冷凝器 61. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 54, wherein a second addition generator, a second addition solution heat exchanger, and a second addition throttle valve are added. The newly added first generator (A) concentrated solution line is connected to the first solution heat exchanger (10) via the first solution pump (7) and the newly added first solution heat exchanger (B) to be newly added. The first generator (A) has a concentrated solution line connected to the newly added second generator (E) via a new second solution heat exchanger (F), and a second generator (E) and a concentrated solution tube are added. The first solution pump (7), the new second solution heat exchanger (F), and the newly added first solution heat exchanger (B) are connected to the first solution heat exchanger (10), and a new first will be added. The generator (A) has a refrigerant vapor passage connected to the first condenser (4) and is adjusted to add a first generator (A). A refrigerant vapor passage is connected with the newly added second generator (E). The second generator (E) has a refrigerant liquid line added by the second throttle valve (G) and the first condenser
(4)连通， 新增第二发生器（E)还有冷剂蒸汽通道与第一冷凝器（4) 连通， 形成以回热式 三效为低温发生流程的第三类吸收式热泵。 (4) Connected, a new second generator (E) and a refrigerant vapor passage are connected to the first condenser (4) to form a third type of absorption heat pump with a regenerative three-effect low temperature generation process.
62. 第三类吸收式热泵， 是在权利要求 55所述的第三类吸收式热泵中， 增加新增第二 发生器、 新增溶液热交换器和新增第二节流阀， 将新增第一发生器（A)有浓溶液管路经第一 溶液泵 （7 ) 与第一溶液热交换器 （10) 连通调整为新增第一发生器 （A) 有浓溶液管路经新 增溶液热交换器 （B) 与新增第二发生器（E)连通， 新增第二发生器（E)还有浓溶液管路经 第一溶液泵 （7) 和新增溶液热交换器 （B) 与第一溶液热交换器 （10) 连通， 将新增第一发 生器（A)有冷剂蒸汽通道与第一冷凝器（4)连通调整为新增第一发生器（A)有冷剂蒸汽通 道与新增第二发生器（E)连通后新增第二发生器（E)再有冷剂液管路经新增第二节流阀（G) 与第一冷凝器 （4) 连通， 新增第二发生器 （E) 还有冷剂蒸汽通道与第一冷凝器 （4 ) 连通， 形成以回热式三效为低温发生流程的第三类吸收式热泵。  62. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 55, adding a new second generator, a new solution heat exchanger and a new second throttle valve, Increasing the first generator (A) has a concentrated solution line connected to the first solution heat exchanger (10) via the first solution pump (7) to adjust the new first generator (A) with a concentrated solution line through the new The solution heat exchanger (B) is connected to the newly added second generator (E), and the second generator (E) and the concentrated solution line are fed through the first solution pump (7) and the new solution heat exchanger. (B) communicating with the first solution heat exchanger (10), adjusting the newly added first generator (A) refrigerant vapor passage to the first condenser (4) to adjust the first generator (A) A second generator (E) is added after the refrigerant vapor passage is connected with the newly added second generator (E), and a refrigerant liquid line is added through the second throttle valve (G) and the first condenser ( 4) Connect, add a second generator (E) and a refrigerant vapor channel to communicate with the first condenser (4) to form a regenerative three-effect process Absorption heat pump.
63. 第三类吸收式热泵， 是在权利要求 62所述的第三类吸收式热泵中， 增加新增溶液 泵， 将吸收-发生器（16)有稀溶液管路直接与第一发生器（1 )连通调整为吸收-发生器（16) 有稀溶液管路经新增溶液泵 （D) 和第一溶液热交换器 （10) 与第一发生器 （1 ) 连通， 将新 增第二发生器（E)有浓溶液管路经第一溶液泵（7)和新增溶液热交换器（B) 与第一溶液热 交换器 （10) 连通调整为新增第二发生器 （E) 有浓溶液管路经第一溶液泵 （7) 和新增溶液 热交换器 （B) 与吸收-发生器 （16) 连通， 将第一发生器 （1 ) 有冷剂蒸汽通道与吸收-发生 器 （16) 连通调整为新增第一发生器 （A) 有冷剂蒸汽通道与吸收-发生器 （16) 连通， 形成 以回热式三效为低温发生流程的第三类吸收式热泵。  63. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 62, adding a new solution pump, the absorption-generator (16) having a dilute solution line directly connected to the first generator (1) Connected adjustment to absorption-generator (16) The dilute solution line is connected to the first generator (1) via the new solution pump (D) and the first solution heat exchanger (10). The second generator (E) has a concentrated solution line connected to the first solution heat exchanger (10) via the first solution pump (7) and the new solution heat exchanger (B) to be added to the second generator (E) The concentrated solution line is connected to the absorption-generator (16) via the first solution pump (7) and the new solution heat exchanger (B), and the first generator (1) has a refrigerant vapor channel and absorption - The generator (16) is connected to the first generator (A). The refrigerant vapor channel is connected to the absorption-generator (16) to form a third type of absorption heat pump with a regenerative three-effect process. .
64. 第三类吸收式热泵， 是在权利要求 56所述的第三类吸收式热泵中， 增加新增第二 发生器、 新增第二溶液热交换器、 新增第二节流阀和新增第二溶液泵， 将吸收-发生器 （16) 有稀溶液管路经第一溶液热交换器（ 10)和新增第一溶液热交换器（B)与新增第一发生器（A) 连通调整为吸收-发生器 （16) 有稀溶液管路经第一溶液热交换器 （10)、 新增第一溶液热交 换器（B)和新增第二溶液热交换器 （F) 与新增第二发生器 （E)连通， 新增第二发生器 （E) 还有浓溶液管路经新增第二溶液泵（H)和新增第二溶液热交换器（F)与新增第一发生器（A) 连通， 将新增第一发生器 （A) 有冷剂蒸汽通道与第一冷凝器 （4 ) 连通调整为新增第一发生 器（A)有冷剂蒸汽通道与新增第二发生器（E)连通后新增第二发生器 （E) 再有冷剂液管路 经新增第二节流阀 （G) 与第一冷凝器 （4)连通， 新增第二发生器（E)还有冷剂蒸汽通道与 第一冷凝器 （4) 连通， 形成以回热式三效为低温发生流程的第三类吸收式热泵。  64. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 56, adding a second addition generator, adding a second solution heat exchanger, adding a second throttle valve, and Adding a second solution pump, the absorption-generator (16) has a dilute solution line through the first solution heat exchanger (10) and a new first solution heat exchanger (B) with a new first generator ( A) Connected to the absorption-generator (16) with a dilute solution line through the first solution heat exchanger (10), a new first solution heat exchanger (B) and a new second solution heat exchanger (F) ) Connected with the new second generator (E), added a second generator (E) and a concentrated solution line via a new second solution pump (H) and a new second solution heat exchanger (F) Connected with the newly added first generator (A), the newly added first generator (A) has a refrigerant vapor passage connected to the first condenser (4) and is adjusted to add a first generator (A) with a refrigerant The second flow generator (E) is added after the steam passage is connected with the newly added second generator (E), and the second throttle valve (G) and the first condenser are added through the refrigerant liquid line. (4) Connect, add a second generator (E) and a refrigerant vapor passage to communicate with the first condenser (4) to form a third type of absorption heat pump with a regenerative three-effect low temperature generation process.
65. 第三类吸收式热泵， 是在权利要求 57所述的第三类吸收式热泵中， 增加新增第二 发生器、 新增溶液热交换器、 新增第二节流阀和新增溶液泵， 将吸收-发生器（16)有稀溶液 管路第一溶液热交换器 （10) 与新增第一发生器 （A) 连通调整为吸收-发生器 （16) 有稀溶 权 利 要 求 书 65. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 57, adding a new second generator, a new solution heat exchanger, adding a second throttle valve, and adding The solution pump, the absorption-generator (16) has a dilute solution line, the first solution heat exchanger (10) is connected to the newly added first generator (A), and is adjusted to an absorption-generator (16). Claim
― WO 2013/003982 PCT/CN2011/001118  ― WO 2013/003982 PCT/CN2011/001118
液管路经第一溶液热交换器 （10) 和新增溶液热交换器 （B) 与新增第二发生器 （E) 连通， 新增第二发生器（E)还有浓溶液管路经新增溶液泵 （D)和新增溶液热交换器（B) 与新增第 一发生器（A)连通， 将新增第一发生器（A)有冷剂蒸汽通道与第一冷凝器 （4)连通调整为 新增第一发生器（A)有冷剂蒸汽通道与新增第二发生器（E)连通后新增第二发生器（E)再 有冷剂液管路经新增第二节流阀 （G) 与第一冷凝器（4)连通， 新增第二发生器（E)还有冷 剂蒸汽通道与第一冷凝器（4)连通，形成以回热式三效为低温发生流程的第三类吸收式热泵。 The liquid line is connected to the newly added second generator (E) via the first solution heat exchanger (10) and the new solution heat exchanger (B), and the second generator (E) and the concentrated solution line are added. The new solution pump (D) and the new solution heat exchanger (B) are connected to the newly added first generator (A), and the first generator (A) has a refrigerant vapor passage and a first condenser. (4) Connected adjustment to add new first generator (A) with refrigerant vapor channel and new second generator (E) connected to add new second generator (E) and then refrigerant liquid pipeline through new The second throttle valve (G) is connected to the first condenser (4), and the second generator (E) and the refrigerant vapor passage are connected to the first condenser (4) to form a regenerative three. The third type of absorption heat pump that functions as a low temperature generation process.
66. 第三类吸收式热泵， 是在权利要求 65所述的第三类吸收式热泵中， 取消新增溶液 节流阀， 将第一发生器（1 )有浓溶液管路经新增溶液节流阔 (J)和吸收-发生器（16) 与分 汽室 （17) 连通调整为第一发生器 （1 ) 有浓溶液管路经第一溶液热交换器 （10) 和吸收-发 生器（16)与分汽室（17 )连通，将吸收-发生器（16)有稀溶液管路经第一溶液热交换器（10) 和新增溶液热交换器（B) 与新增第二发生器（E)连通调整为吸收-发生器（16)有稀溶液管 路经新增溶液热交换器 （B) 与新增第二发生器（E)连通， 将第一发生器（1 )有冷剂蒸汽通 道与吸收-发生器（ 16)连通调整为新增第一发生器（A)增设冷剂蒸汽通道与吸收-发生器（ 16) 连通， 形成以回热式三效为低温发生流程的第三类吸收式热泵。  66. A third type of absorption heat pump, wherein in the third type of absorption heat pump according to claim 65, the new solution throttle valve is cancelled, and the first generator (1) has a concentrated solution line through the newly added solution. The throttle width (J) and the absorption-generator (16) are connected to the steam distribution chamber (17) to adjust to the first generator (1). The concentrated solution line passes through the first solution heat exchanger (10) and absorbs - occurs The device (16) is in communication with the steam dividing chamber (17), and the absorption-generator (16) has a dilute solution line through the first solution heat exchanger (10) and the new solution heat exchanger (B) with a new addition The second generator (E) is connected to the absorption-generator (16) having a dilute solution line connected to the newly added second generator (E) via the new solution heat exchanger (B), and the first generator (1) The refrigerant vapor passage and the absorption-generator (16) are connected to each other to adjust the addition of the first generator (A) to the refrigerant vapor passage and the absorption-generator (16) to form a regenerative three-effect low temperature. The third type of absorption heat pump in which the process takes place.
67. 第三类吸收式热泵， 是在权利要求 4、 29-36内任一权利要求所述的第三类吸收式 热泵中， 增加新增发生器、新增溶液热交换器、新增节流阀和新增溶液泵， 吸收-发生器（16) 增设稀溶液管路经新增溶液热交换器（B) 与新增发生器（A)连通， 新增发生器（A)还有浓 溶液管路经新增溶液泵 （D)和新增溶液热交换器 （B) 与吸收-发生器（16)连通， 将第一发 生器（1 )有冷剂蒸汽通道与第一冷凝器（4)连通调整为第一发生器（1 )有冷剂蒸汽通道与 新增发生器（A)连通后新增发生器（A)再有冷剂液管路经新增节流阀（C)与第一冷凝器（4) 连通， 新增发生器 （A) 还有冷剂蒸汽通道与第一冷凝器 （4) 连通， 形成以回热式双效为低 温发生流程的第三类吸收式热泵。  67. A third type of absorption heat pump, which is a third type of absorption heat pump according to any one of claims 4, 29-36, adding a new generator, a new solution heat exchanger, and an adding section Flow valve and new solution pump, absorption-generator (16) Adding dilute solution line via new solution heat exchanger (B) to new generator (A), new generator (A) and thick The solution line is connected to the absorption-generator (16) via a new solution pump (D) and a new solution heat exchanger (B), and the first generator (1) has a refrigerant vapor passage and a first condenser ( 4) Connected to the first generator (1) with the refrigerant vapor channel connected to the new generator (A), the new generator (A) and then the refrigerant liquid pipeline through the new throttle valve (C) Connected with the first condenser (4), a new generator (A) and a refrigerant vapor passage are connected to the first condenser (4) to form a third type of absorption type with a regenerative double effect as a low temperature generation process. Heat pump.
68. 第三类吸收式热泵， 是在权利要求 4、 29- 36内任一权利要求所述的第三类吸收式 热泵中， 增加新增发生器、 新增溶液热交换器和新增节流阀， 将第一发生器（1 )有浓溶液管 路经第一溶液泵 （7) 和第一溶液热交换器 （10) 与吸收-发生器 （16) 连通调整为第一发生 器 （1 ) 有浓溶液管路经新增溶液热交换器 （B) 与新增发生器 （A) 连通， 新增发生器 （A) 还有浓溶液管路经第一溶液泵（7)、 新增溶液热交换器（B)和第一溶液热交换器（10) 与吸 收-发生器（16)连通， 将第一发生器（1 )有冷剂蒸汽通道与第一冷凝器 （4)连通调整为第 一发生器（1 )有冷剂蒸汽通道与新增发生器（A)连通后新增发生器（A) 再有冷剂液管路经 新增节流阔 (C) 与第一冷凝器（4)连通， 新增发生器 （A)还有冷剂蒸汽通道与第一冷凝器 68. A third type of absorption heat pump, which is a third type of absorption heat pump according to any one of claims 4, 29-36, adding a new generator, a new solution heat exchanger and an additional section a flow valve, wherein the first generator (1) has a concentrated solution line connected to the first solution pump (7) and the first solution heat exchanger (10) and the absorption-generator (16) to be adjusted into a first generator ( 1) The concentrated solution line is connected to the new generator (A) via the new solution heat exchanger (B), the new generator (A) and the concentrated solution line are passed through the first solution pump (7), new The solution heating heat exchanger (B) and the first solution heat exchanger (10) are in communication with the absorption-generator (16), and the first generator (1) has a refrigerant vapor channel connected to the first condenser (4) Adjusted to the first generator (1) with a refrigerant vapor channel connected to the new generator (A), the new generator (A) and then the refrigerant liquid pipeline through the new throttle (C) and the first The condenser (4) is connected, and the new generator (A) has a refrigerant vapor passage and a first condenser.
(4) 连通， 形成以回热式双效为低温发生流程的第三类吸收式热泵。 (4) Connected to form a third type of absorption heat pump with a regenerative double effect as a low temperature generation process.
69. 第三类吸收式热泵， 是在权利要求 4、 29-36内任一权利要求所述的第三类吸收式 热泵中，增加新增发生器、新增溶液热交换器、新增节流阀和新增溶液泵，将吸收-发生器（16) 有稀溶液管路经第一溶液热交换器 （10) 与第一发生器 （1 ) 连通调整为吸收-发生器 （16) 有稀溶液管路第一溶液热交换器 （10) 和新增溶液热交换器 （B) 与新增发生器 （A) 连通， 新增发生器（A)还有浓溶液管路经新增溶液泵（D)和新增溶液热交换器（B) 与第一发生器 69. A third type of absorption heat pump, which is a third type of absorption heat pump according to any one of claims 4, 29-36, adding a new generator, a new solution heat exchanger, and an adding section Flow valve and new solution pump, the absorption-generator (16) has a dilute solution line connected to the first generator (1) through the first solution heat exchanger (10) to adjust to an absorption-generator (16) The dilute solution line first solution heat exchanger (10) and the new solution heat exchanger (B) are connected to the new generator (A), and the new generator (A) and the concentrated solution line are added with the new solution. Pump (D) and new solution heat exchanger (B) with first generator
( 1 )连通，将第一发生器（1 )有冷剂蒸汽通道与第一冷凝器（4)连通调整为第一发生器（1 ) 有冷剂蒸汽通道与新增发生器（A)连通后新增发生器（A)再有冷剂液管路经新增节流阀（C) 与第一冷凝器 （4) 连通， 新增发生器（A)还有冷剂蒸汽通道与第一冷凝器（4)连通， 形成 以回热式双效为低温发生流程的第三类吸收式热泵。 权 利 要 求 书 (1) communicating, connecting the first generator (1) having a refrigerant vapor passage to the first condenser (4) to be adjusted to be the first generator (1) having a refrigerant vapor passage connected to the newly added generator (A) After the addition of the generator (A), the refrigerant liquid line is connected to the first condenser (4) via the new throttle valve (C), and the new generator (A) has a refrigerant vapor passage and the first The condenser (4) is connected to form a third type of absorption heat pump with a regenerative double effect as a low temperature generation process. Claim
― WO 2013/003982 PCT/CN2011/001118  ― WO 2013/003982 PCT/CN2011/001118
70. 第三类吸收式热泵， 是在权利要求 67所述的第三类吸收式热泵中， 增加新增第二 发生器、 新增第二溶液热交换器、 新增第二节流阀和新增第二溶液泵， 吸收-发生器（16)增 设稀溶液管路经新增第二溶液热交换器 （F) 与新增第二发生器 （E) 连通， 新增第二发生器 70. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 67, adding a second addition generator, adding a second solution heat exchanger, adding a second throttle valve, and A second solution pump is added, and the absorption-generator (16) is added with a dilute solution line. The second solution heat exchanger (F) is connected to the newly added second generator (E), and a second generator is added.
(E) 还有浓溶液管路经新增第二溶液泵 （H) 和新增第二溶液热交换器 （F) 与吸收-发生器 ( 16) 连通， 将新增第一发生器 （A) 有冷剂蒸汽通道与第一冷凝器 （4) 连通调整为新增第 一发生器（A)有冷剂蒸汽通道与新增第二发生器（E)连通后新增第二发生器（E)再有冷剂 液管路经新增第二节流阔 (G) 与第一冷凝器（4)连通， 新增第二发生器（E)还有冷剂蒸汽 通道与第一冷凝器 （4) 连通， 形成以回热式三效为低温发生流程的第三类吸收式热泵。 (E) The concentrated solution line is connected to the absorption-generator (16) via the addition of the second solution pump (H) and the addition of the second solution heat exchanger (F), and the first generator (A) is added. The refrigerant vapor passage is connected to the first condenser (4) to adjust to add a first generator (A) to have a refrigerant vapor passage and to connect the newly added second generator (E) to add a second generator ( E) The refrigerant liquid line is connected to the first condenser (4) by adding a second section of the flow (G), and the second generator (E) is further provided with a refrigerant vapor passage and a first condenser. (4) Connected to form a third type of absorption heat pump with a regenerative three-effect process as a low temperature generation process.
71. 第三类吸收式热泵， 是在权利要求 68所述的第三类吸收式热泵中， 增加新增第二 发生器、 新增第二溶液热交换器和新增第二节流阀， 将新增第一发生器（A)有浓溶液管路经 第一溶液泵 （7) 和新增第一溶液热交换器 （B) 与第一溶液热交换器 （10) 连通调整为新增 第一发生器 （A) 有浓溶液管路经新增第二溶液热交换器 （F) 与新增第二发生器 （E) 连通， 新增第二发生器 （E) 还有浓溶液管路经第一溶液泵 （7 )、 新增第二溶液热交换器 （F) 和新 增第一溶液热交换器 （B) 与第一溶液热交换器 （10) 连通， 将新增第一发生器 （A) 有冷剂 蒸汽通道与第一冷凝器 （4) 连通调整为新增第一发生器 （A) 有冷剂蒸汽通道与新增第二发 生器（E)连通后新增第二发生器（E)再有冷剂液管路经新增第二节流阀 （G) 与第一冷凝器 71. A third type of absorption heat pump, in the third type of absorption heat pump according to claim 68, adding a new second generator, adding a second solution heat exchanger, and adding a second throttle valve, The newly added first generator (A) concentrated solution line is connected to the first solution heat exchanger (10) via the first solution pump (7) and the newly added first solution heat exchanger (B) to be newly added. The first generator (A) has a concentrated solution line connected to the newly added second generator (E) via a new second solution heat exchanger (F), and a second generator (E) and a concentrated solution tube are added. The first solution pump (7), the new second solution heat exchanger (F), and the newly added first solution heat exchanger (B) are connected to the first solution heat exchanger (10), and a new first will be added. The generator (A) has a refrigerant vapor passage connected to the first condenser (4) and is adjusted to add a first generator (A). A refrigerant vapor passage is connected with the newly added second generator (E). The second generator (E) has a refrigerant liquid line added by the second throttle valve (G) and the first condenser
(4)连通， 新增第二发生器（E)还有冷剂蒸汽通道与第一冷凝器（4)连通， 形成以回热式 三效为低温发生流程的第三类吸收式热泵。 (4) Connect, add a second generator (E) and a refrigerant vapor passage to communicate with the first condenser (4) to form a third type of absorption heat pump with a regenerative three-effect low temperature generation process.
72. 第三类吸收式热泵， 是在权利要求 69所述的第三类吸收式热泵中， 增加新增第二 发生器、 新增第二溶液热交换器、 新增第二节流阔和新增第二溶液泵， 将吸收-发生器 （16) 有稀溶液管路经第一溶液热交换器（ 10)和新增第一溶液热交换器（B)与新增第一发生器（A) 连通调整为吸收-发生器 （16) 有稀溶液管路经第一溶液热交换器 （10)、 新增第一溶液热交 换器（B)和新增第二溶液热交换器 （F) 与新增第二发生器（E)连通， 新增第二发生器（E) 还有浓溶液管路经新增第二溶液泵（H)和新增第二溶液热交换器（F)与新增第一发生器（A) 连通， 将新增第一发生器 （A) 有冷剂蒸汽通道与第一冷凝器 （4) 连通调整为新增第一发生 器（A)有冷剂蒸汽通道与新增第二发生器（E)连通后新增第二发生器（E)再有冷剂液管路 经新增第二节流阀 （G) 与第一冷凝器（4)连通， 新增第二发生器（E) 还有冷剂蒸汽通道与 第一冷凝器 （4) 连通， 形成以回热式三效为低温发生流程的第三类吸收式热泵。  72. The third type of absorption heat pump is the third type of absorption heat pump according to claim 69, wherein a new second generator is added, a second solution heat exchanger is added, and a second section is added. Adding a second solution pump, the absorption-generator (16) has a dilute solution line through the first solution heat exchanger (10) and a new first solution heat exchanger (B) with a new first generator ( A) Connected to the absorption-generator (16) with a dilute solution line through the first solution heat exchanger (10), a new first solution heat exchanger (B) and a new second solution heat exchanger (F) ) Connected with the new second generator (E), added a second generator (E) and a concentrated solution line via a new second solution pump (H) and a new second solution heat exchanger (F) Connected with the newly added first generator (A), the newly added first generator (A) has a refrigerant vapor passage connected to the first condenser (4) and is adjusted to add a first generator (A) with a refrigerant After the steam passage is connected with the newly added second generator (E), a second generator (E) is added, and then a refrigerant liquid line is added through the second throttle valve (G) and the first condenser (4). Connected, a new second generator (E) is added, and a refrigerant vapor passage is connected to the first condenser (4) to form a third type of absorption heat pump having a regenerative three-effect low temperature generation process.
73. 第三类吸收式热泵， 是在权利要求 1所提及的单效-单效第三类吸收式热泵以及权 利要求 5- 12内任一权利要求所述的第三类吸收式热泵中， 增加新增冷剂液泵或新增节流阀、 新增溶液热交换器和新增吸收-蒸发器，将吸收器（3 )有稀溶液管路经第一溶液热交换器（ 10) 与第一发生器（1 )连通调整为吸收器（3 )有稀溶液管路经新增溶液热交换器（B) 与新增吸 收-蒸发器 （K) 连通， 新增吸收-蒸发器 （K) 还有稀溶液管路经第一溶液热交换器 （10) 与 第一发生器 （1 )连通， 将第一发生器（1 )有浓溶液管路经第一溶液泵 （7 )和第一溶液热交 换器（10) 与第二溶液热交换器（11 )连通调整为第一发生器（1 )有浓溶液管路经第一溶液 泵（7)、 第一溶液热交换器（10)和新增溶液热交换器（B)与第二溶液热交换器（11 )连通， 将蒸发器（6 )有冷剂蒸汽通道与吸收器（3 )连通调整为蒸发器（6)有冷剂蒸汽通道与新增 吸收-蒸发器（K)连通， 蒸发器（6)或第一冷凝器（4)增设冷剂液管路经新增冷剂液泵（L) 与新增吸收-蒸发器（K)连通后新增吸收-蒸发器（K)再有冷剂蒸汽通道与吸收器（3)连通、 或第二冷凝器 （5) 增设冷剂液管路经新增节流阀 （C) 与新增吸收-蒸发器 （K) 连通后新增 权 利 要 求 书 73. A third type of absorption heat pump, which is the single-effect single-effect third-type absorption heat pump of claim 1 and the third type of absorption heat pump according to any one of claims 5-12. , adding new refrigerant liquid pump or new throttle valve, new solution heat exchanger and new absorption-evaporator, and the absorber (3) has a dilute solution pipeline through the first solution heat exchanger (10) Connected to the first generator (1) to adjust to the absorber (3) with a dilute solution line connected to the new absorption-evaporator (K) via the new solution heat exchanger (B), adding an absorption-evaporator ( K) a dilute solution line is connected to the first generator (1) via the first solution heat exchanger (10), and the first generator (1) has a concentrated solution line through the first solution pump (7) and The first solution heat exchanger (10) is connected to the second solution heat exchanger (11) to be adjusted to have a first generator (1) having a concentrated solution line passing through the first solution pump (7) and the first solution heat exchanger ( 10) communicating with the new solution heat exchanger (B) and the second solution heat exchanger (11), and connecting the evaporator (6) with the refrigerant vapor passage to the absorber (3) Adjusted to evaporator (6) with refrigerant vapor channel connected to new absorption-evaporator (K), evaporator (6) or first condenser (4) additional refrigerant liquid pipeline via new refrigerant liquid pump (L) Adding an absorption-evaporator (K) to the new absorption-evaporator (K) and then connecting the refrigerant vapor channel to the absorber (3), or adding a coolant solution to the second condenser (5) The pipeline is added after the new throttle valve (C) is connected to the new absorption-evaporator (K). Claim
― WO 2013/003982 PCT/CN2011/001118 吸收-蒸发器（K)再有冷剂蒸汽通道与吸收器（3)连通， 形成以 1. 5级为低温发生流程的第 三类吸收式热泵。  ― WO 2013/003982 PCT/CN2011/001118 The absorption-evaporator (K) is further connected to the absorber (3) via a refrigerant vapor channel to form a third type of absorption heat pump with a stage 1.
74. 第三类吸收式热泵， 是在权利要求 1所提及的单效-单效第三类吸收式热泵以及权 利要求 5- 12内任一权利要求所述的第三类吸收式热泵中， 增加新增溶液热交换器、新增溶液 泵、新增吸收-蒸发器、 新增冷剂液泵或新增节流阀， 将浓溶液提供器有浓溶液管路与吸收器 74. A third type of absorption heat pump, which is the single-effect-single-effect third-type absorption heat pump of claim 1 and the third type of absorption heat pump according to any one of claims 5-12. , adding new solution heat exchanger, new solution pump, new absorption-evaporator, new refrigerant liquid pump or new throttle valve, concentrated solution provider with concentrated solution line and absorber
(3)连通调整为浓溶液提供器有浓溶液管路经新增溶液热交换器（B)与新增吸收-蒸发器（K) 连通， 新增吸收-蒸发器 （K) 还有稀溶液管路经新增溶液泵 （D) 和新增溶液热交换器 （B) 与吸收器 （3) 连通， 将蒸发器 （6) 有冷剂蒸汽通道与吸收器 （3 ) 连通调整为蒸发器 （6) 有冷剂蒸汽通道与新增吸收-蒸发器 （K) 连通， 蒸发器 （6) 或第一冷凝器 （4) 增设冷剂液 管路经新增冷剂液泵 （L) 与新增吸收-蒸发器（K)连通后新增吸收-蒸发器（K)再有冷剂蒸 汽通道与吸收器（3 )连通、 或第二冷凝器（5)增设冷剂液管路经新增节流阀 （C) 与新增吸 收-蒸发器（K)连通后新增吸收-蒸发器（K) 再有冷剂蒸汽通道与吸收器（3)连通， 形成以 1. 5级为低温发生流程的第三类吸收式热泵。 (3) Connected to a concentrated solution provider with a concentrated solution line connected to the new absorption-evaporator (K) via a new solution heat exchanger (B), a new absorption-evaporator (K) and a dilute solution The pipeline is connected to the absorber (3) via a new solution pump (D) and a new solution heat exchanger (B), and the evaporator (6) has a refrigerant vapor passage connected to the absorber (3) to be adjusted to an evaporator. (6) The refrigerant vapor passage is connected to the new absorption-evaporator (K), and the evaporator (6) or the first condenser (4) is provided with a refrigerant liquid pipeline via a new refrigerant liquid pump (L). Adding absorption-evaporator (K) connection, adding absorption-evaporator (K) and then connecting the refrigerant vapor channel to the absorber (3), or adding a coolant line to the second condenser (5) The lower throttle valve (C) is connected to the new absorption-evaporator (K), and the absorption-evaporator (K) is added to the refrigerant vapor channel and the absorber (3). The third type of absorption heat pump in which the process takes place.
75. 第三类吸收式热泵， 是在权利要求 1所提及的单效-单效第三类吸收式热泵以及权 利要求 5-12内任一权利要求所述的第三类吸收式热泵中， 增加新增溶液热交换器、新增溶液 泵、 新增吸收-蒸发器、 新增冷剂液泵或新增节流阀， 将第一发生器 （1 ) 有浓溶液管路经第 一溶液泵（7 )和第一溶液热交换器（10) 与第二溶液热交换器（11 )连通调整为第一发生器 75. A third type of absorption heat pump, which is the single-effect-single-effect third-type absorption heat pump of claim 1 and the third type of absorption heat pump according to any one of claims 5-12. , adding new solution heat exchanger, new solution pump, new absorption-evaporator, new refrigerant liquid pump or new throttle valve, the first generator (1) has a concentrated solution pipeline through the first The solution pump (7) and the first solution heat exchanger (10) are connected to the second solution heat exchanger (11) to be adjusted to the first generator
( 1 ) 有浓溶液管路经第一溶液泵 （7)、 第一溶液热交换器 （10) 和新增溶液热交换器 （B) 与新增吸收-蒸发器 （K)连通， 新增吸收-蒸发器（K)还有稀溶液管路经新增溶液泵 （D)和 新增溶液热交换器 （B) 与第二溶液热交换器 （11 ) 连通， 将蒸发器 （6) 有冷剂蒸汽通道与 吸收器 （3) 连通调整为蒸发器 （6) 有冷剂蒸汽通道与新增吸收-蒸发器 （K) 连通， 蒸发器(1) The concentrated solution line is connected to the new absorption-evaporator (K) via the first solution pump (7), the first solution heat exchanger (10), and the new solution heat exchanger (B). The absorption-evaporator (K) and the dilute solution line are connected to the second solution heat exchanger (11) via a new solution pump (D) and a new solution heat exchanger (B), and the evaporator (6) is provided The refrigerant vapor passage is connected to the absorber (3) to adjust to the evaporator (6). The refrigerant vapor passage is connected to the new absorption-evaporator (K).
(6)或第一冷凝器 （4)增设冷剂液管路经新增冷剂液泵 （L) 与新增吸收-蒸发器（K)连通 后新增吸收-蒸发器 （K) 再有冷剂蒸汽通道与吸收器 （3) 连通、 或第二冷凝器 （5) 增设冷 剂液管路经新增节流阀 （C)与新增吸收-蒸发器（K)连通后新增吸收-蒸发器（K)再有冷剂 蒸汽通道与吸收器 （3) 连通， 形成以 1. 5级为低温发生流程的第三类吸收式热泵。 (6) or the first condenser (4) is added with a refrigerant liquid pipeline. After the new refrigerant liquid pump (L) is connected with the new absorption-evaporator (K), the absorption-evaporator (K) is added. The refrigerant vapor passage is connected to the absorber (3), or the second condenser (5) is added with a refrigerant liquid pipeline. The new throttle valve (C) is connected to the new absorption-evaporator (K) to newly absorb. The evaporator (K) is further connected to the absorber (3) by a refrigerant vapor passage to form a third type of absorption heat pump having a flow rate of 1.5.
76. 第三类吸收式热泵， 是在权利要求 1、 13- 20内任一权利要求所述的第三类吸收式 热泵中， 增加新增溶液热交换器、 新增吸收-蒸发器、 新增冷剂液泵或新增节流阀， 将吸收器 76. A third type of absorption heat pump, in the third type of absorption heat pump according to any one of claims 1, 13-20, adding a new solution heat exchanger, adding an absorption-evaporator, a new Refrigerant liquid pump or new throttle valve, will be the absorber
(3) 有稀溶液管路经第一溶液热交换器 （10) 与第二吸收器 （13) 连通调整为吸收器 （3 ) 有稀溶液管路经新增溶液热交换器（B)与新增吸收-蒸发器（K)连通， 新增吸收-蒸发器（K) 还有稀溶液管路经第一溶液热交换器 （10) 与第二吸收器 （13 ) 连通， 将第三发生器 （12 ) 有浓溶液管路经第一溶液泵（7 )和第一溶液热交换器（10) 与第二溶液热交换器（11 )连通 调整为第三发生器 （12 ) 有浓溶液管路经第一溶液泵 （7)、 第一溶液热交换器 （10) 和新增 溶液热交换器 （B) 与第二溶液热交换器 （11 ) 连通， 将蒸发器 （6) 有冷剂蒸汽通道与吸收 器 （3) 连通调整为蒸发器 （6) 有冷剂蒸汽通道与新增吸收-蒸发器 （K) 连通， 蒸发器 （6) 或第一冷凝器 （4) 增设冷剂液管路经新增冷剂液泵 （L) 与新增吸收-蒸发器 （K) 连通后新 增吸收-蒸发器 （K) 再有冷剂蒸汽通道与吸收器 （3 ) 连通、 或第二冷凝器 （5) 增设冷剂液 管路经新增节流阔 (C) 与新增吸收-蒸发器（K)连通后新增吸收-蒸发器（K)再有冷剂蒸汽 通道与吸收器 （3 ) 连通， 形成以回热式 1. 5级为低温发生流程的第三类吸收式热泵。 (3) The dilute solution line is connected to the second absorber (13) through the first solution heat exchanger (10) to adjust to the absorber (3). The dilute solution line is connected to the new solution heat exchanger (B). A new absorption-evaporator (K) connection, a new absorption-evaporator (K) and a dilute solution line are connected to the second absorber (13) via the first solution heat exchanger (10), which will occur third. The (12) concentrated solution line is connected to the second solution heat exchanger (11) via the first solution pump (7) and the first solution heat exchanger (10) to adjust the third generator (12) to have a concentrated solution. The pipeline is connected to the second solution heat exchanger (11) via the first solution pump (7), the first solution heat exchanger (10) and the new solution heat exchanger (B), and the evaporator (6) is cold. The vapor channel of the agent is connected to the absorber (3) and is adjusted to be an evaporator (6). The refrigerant vapor channel is connected to the new absorption-evaporator (K), and the evaporator (6) or the first condenser (4) is provided with a coolant. The liquid pipeline is connected to the new absorption-evaporator (K) via the new refrigerant pump (L), and the absorption-evaporator (K) is added. Connected to the absorber (3), or the second condenser (5) is added with a refrigerant liquid line. After the new throttle (C) is connected with the new absorption-evaporator (K), an absorption-evaporator is added. K) A refrigerant vapor passage is connected to the absorber (3) to form a third type of absorption heat pump in which the heat recovery type 1.5 is a low temperature generation process.
77. 第三类吸收式热泵， 是在权利要求 1、 13-20内任一权利要求所述的第三类吸收式 热泵中， 增加新增溶液热交换器、 新增溶液泵、 新增吸收-蒸发器、 新增冷剂液泵或新增节流 权 利 要 求 书 77. The third type of absorption heat pump is the third type of absorption heat pump according to any one of claims 1, 13-20, adding a new solution heat exchanger, adding a new solution pump, adding new absorption - evaporator, new coolant pump or new throttle Claim
― WO 2013/003982 PCT/CN2011/001118  ― WO 2013/003982 PCT/CN2011/001118
阀， 将浓溶液提供器有浓溶液管路与吸收器（3)连通调整为浓溶液提供器有浓溶液管路经新 增溶液热交换器（B) 与新增吸收-蒸发器 )连通， 新增吸收-蒸发器（κ)还有稀溶液管路 经新增溶液泵 （D) 和新增溶液热交换器 （Β) 与吸收器 （3) 连通， 将蒸发器 （6) 有冷剂蒸 汽通道与吸收器（3)连通调整为蒸发器（6)有冷剂蒸汽通道与新增吸收-蒸发器（Κ)连通, 蒸发器（6)或第一冷凝器（4)增设冷剂液管路经新增冷剂液泵（L)与新增吸收-蒸发器（Κ) 连通后新增吸收-蒸发器 （Κ) 再有冷剂蒸汽通道与吸收器 （3) 连通、 或第二冷凝器 （5) 增 设冷剂液管路经新增节流阀 （C) 与新增吸收-蒸发器（Κ)连通后新增吸收-蒸发器（Κ) 再有 冷剂蒸汽通道与吸收器（3)连通，形成以回热式 1. 5级为低温发生流程的第三类吸收式热泵。 Valve, the concentrated solution provider has a concentrated solution line connected to the absorber (3) to adjust to a concentrated solution provider, the concentrated solution line is connected to the new solution heat exchanger (B) and the new absorption-evaporator. A new absorption-evaporator (κ) and a dilute solution line are connected to the absorber (3) via a new solution pump (D) and a new solution heat exchanger (Β), and the evaporator (6) has a refrigerant. The steam passage is connected to the absorber (3) and is adjusted to be an evaporator (6) having a refrigerant vapor passage communicating with a new absorption-evaporator (Κ), and an evaporator (6) or a first condenser (4) adding a coolant liquid The pipeline is connected to the newly added absorption liquid evaporator (L) and the new absorption-evaporator (Κ), and then the absorption-evaporator (Κ) is added, and then the refrigerant vapor passage is connected to the absorber (3), or the second Condenser (5) Adding refrigerant liquid line through new throttle valve (C) and adding new absorption-evaporator (Κ), adding absorption-evaporator (Κ) and then refrigerant vapor channel and absorber (3) Connected to form a third type of absorption heat pump with a regenerative type 1.5 as a low temperature generation process.
78. 第三类吸收式热泵， 是在权利要求 1、 13- 20内任一权利要求所述的第三类吸收式 热泵中， 增加新增溶液热交换器、 新增溶液泵、 新增吸收-蒸发器、 新增冷剂液泵或新增节流 阀， 将第三发生器（12)有浓溶液管路经第一溶液泵 （7)和第一溶液热交换器（10) 与第二 溶液热交换器 （11 ) 连通调整为第三发生器 （12) 有浓溶液管路经第一溶液泵 （7)、 第一溶 液热交换器 （10) 和新增溶液热交换器 （Β) 与新增吸收-蒸发器 （Κ) 连通， 新增吸收 -蒸发 器（Κ)还有稀溶液管路经新增溶液泵（D)和新增溶液热交换器（Β)与第二溶液热交换器（11 ) 连通， 将蒸发器（6)有冷剂蒸汽通道与吸收器（3)连通调整为蒸发器 （6)有冷剂蒸汽通道 与新增吸收-蒸发器 （Κ) 连通， 蒸发器 （6) 或第一冷凝器 （4) 增设冷剂液管路经新增冷剂 液泵 （U 与新增吸收-蒸发器（Κ)连通后新增吸收-蒸发器（Κ)再有冷剂蒸汽通道与吸收器 78. The third type of absorption heat pump is the third type of absorption heat pump according to any one of claims 1, 13-20, adding a new solution heat exchanger, adding a new solution pump, adding new absorption - an evaporator, a new refrigerant pump or a new throttle valve, the third generator (12) has a concentrated solution line through the first solution pump (7) and the first solution heat exchanger (10) The two solution heat exchanger (11) is connected to the third generator (12). The concentrated solution line is passed through the first solution pump (7), the first solution heat exchanger (10), and the new solution heat exchanger (Β). ) Connected to the new absorption-evaporator (Κ), added absorption-evaporator (Κ) and dilute solution line via new solution pump (D) and new solution heat exchanger (Β) and second solution The heat exchanger (11) is connected, and the evaporator (6) has a refrigerant vapor passage connected to the absorber (3) and is adjusted to be an evaporator (6) having a refrigerant vapor passage connected to the new absorption-evaporator (Κ). Evaporator (6) or first condenser (4) Add refrigerant liquid line via new refrigerant liquid pump (U and new absorption-evaporator (Κ) After through new absorber - evaporator (K0) and then the refrigerant vapor channel and the absorber
(3) 连通、 或第二冷凝器 （5) 增设冷剂液管路经新增节流阀 （C) 与新增吸收-蒸发器 （Κ) 连通后新增吸收-蒸发器（Κ)再有冷剂蒸汽通道与吸收器（3)连通， 形成以回热式 1. 5级为 低温发生流程的第三类吸收式热泵。 (3) Connected, or the second condenser (5) is added with a refrigerant liquid line. After the new throttle valve (C) is connected with the new absorption-evaporator (Κ), the absorption-evaporator (Κ) is added. A refrigerant vapor passage is connected to the absorber (3) to form a third type of absorption heat pump in which the heat recovery type 1.5 is a low temperature generation process.
79. 第三类吸收式热泵， 是在权利要求 2-3、 21-28内任一权利要求所述且无第二蒸发 器的第三类吸收式热泵中， 取消第三溶液泵 21， 吸收器 3有稀溶液管路经第三溶液热交换器 15与吸收-发生器 16连通； 增加新增冷剂液泵或新增节流阔， 取消第一蒸发器 （6) 与吸收 器（3)连通的冷剂蒸汽通道， 第一冷凝器 （4)或蒸发器（6)增设冷剂液管路经新增冷剂液 泵 （U 与吸收-发生器 （16) 连通后吸收-发生器 （16) 还有冷剂蒸汽通道与吸收器 （3) 连 通、 或第二冷凝器 （5) 增设冷剂液管路经新增节流阀 （C) 与新增吸收-蒸发器 （Κ) 连通后 新增吸收-蒸发器（Κ)再有冷剂蒸汽通道与吸收器（3)连通， 形成以回热式 1. 5级为低温发 生流程的第三类吸收式热泵。  79. A third type of absorption heat pump, which is a third type of absorption heat pump according to any one of claims 2-3, 21-28 and having no second evaporator, canceling the third solution pump 21, absorbing The dilute solution line has a dilute solution line connected to the absorption-generator 16 via the third solution heat exchanger 15; adding a new refrigerant liquid pump or adding a new throttle, canceling the first evaporator (6) and the absorber (3) The connected refrigerant vapor channel, the first condenser (4) or the evaporator (6) is provided with a refrigerant liquid pipeline through the newly added refrigerant liquid pump (U and the absorption-generator (16) are connected to the absorption-generator (16) There is also a refrigerant vapor passage connected to the absorber (3), or a second condenser (5) is provided with a refrigerant liquid line via a new throttle valve (C) and a new absorption-evaporator (Κ) After the connection, a new absorption-evaporator (Κ) is added, and then a refrigerant vapor channel is connected to the absorber (3) to form a third type of absorption heat pump in which the regenerative type 1.5 is a low temperature generation process.
80. 第三类吸收式热泵， 是在权利要求 2-3、 21- 28内任一权利要求所述的第三类吸收 式热泵中， 增加新增吸收-蒸发器、 新增冷剂液泵或新增节流阀， 将吸收-发生器 （16) 有稀 溶液管路经第一溶液热交换器 （10) 与第一发生器 （1 ) 连通调整为吸收-发生器 （16) 有稀 溶液管路直接与新增吸收-蒸发器 （Κ) 连通， 新增吸收-蒸发器 （Κ) 还有稀溶液管路经第一 溶液热交换器 （10) 与第一发生器 （1 ) 连通， 将第一蒸发器 （6) 有冷剂蒸汽通道与吸收器 80. The third type of absorption heat pump is the third type of absorption heat pump according to any one of claims 2-3, 21-28, adding a new absorption-evaporator and a new refrigerant liquid pump. Or add a new throttle valve, and connect the absorption-generator (16) with a dilute solution line through the first solution heat exchanger (10) to the first generator (1) to adjust to the absorption-generator (16). The solution line is directly connected to the new absorption-evaporator (Κ), and the new absorption-evaporator (Κ) and the dilute solution line are connected to the first generator (1) via the first solution heat exchanger (10). , the first evaporator (6) has a refrigerant vapor channel and an absorber
(3) 连通调整为第一蒸发器 （6) 有冷剂蒸汽通道与新增吸收-蒸发器 （Κ) 连通， 第一冷凝 器 （4) 或第一蒸发器 （6) 增设冷剂液管路经新增冷剂液泵 （L) 与吸收-发生器 （16) 连通 后吸收-发生器（16)还有冷剂蒸汽通道与吸收器（3)连通、 或第二冷凝器（5)增设冷剂液 管路经新增节流阀 （C) 与新增吸收-蒸发器（Κ)连通后新增吸收-蒸发器（Κ)再有冷剂蒸汽 通道与吸收器 （3) 连通， 形成以回热式 1. 5级为低温发生流程的第三类吸收式热泵。 (3) The connection is adjusted to the first evaporator (6). The refrigerant vapor channel is connected to the new absorption-evaporator (Κ), and the first condenser (4) or the first evaporator (6) is provided with a refrigerant liquid pipe. After the new refrigerant liquid pump (L) is connected to the absorption-generator (16), the absorption-generator (16) and the refrigerant vapor channel are connected to the absorber (3), or the second condenser (5) The additional refrigerant liquid pipeline is connected to the new absorption-evaporator (Κ) via a new throttle valve (C), and then a new absorption-evaporator (Κ) is connected, and a refrigerant vapor passage is connected to the absorber (3). A third type of absorption heat pump is formed which is a regenerative type 1.5 low temperature generation process.
81. 第三类吸收式热泵， 是在权利要求 2-3、 21-28内任一权利要求所述的第三类吸收 式热泵中， 增加新增溶液热交换器、 新增溶液泵、 新增吸收-蒸发器、 新增冷剂液泵或新增节 权 利 要 求 书 81. The third type of absorption heat pump is the third type of absorption heat pump according to any one of claims 2-3, 21-28, adding a new solution heat exchanger, adding a new solution pump, new Increased absorption-evaporator, new coolant pump or new section Claim
― WO 2013/003982 PCT/CN2011/001118  ― WO 2013/003982 PCT/CN2011/001118
流阀， 将浓溶液提供器有浓溶液管路与吸收器（3)连通调整为浓溶液提供器有浓溶液管路经 新增溶液热交换器（B) 与新增吸收-蒸发器 （K)连通， 新增吸收-蒸发器（K)还有稀溶液管 路经新增溶液泵 （D) 和新增溶液热交换器 （B) 与吸收器 （3 ) 连通， 将第一蒸发器 （6) 有 冷剂蒸汽通道与吸收器（3 )连通调整为第一蒸发器（6)有冷剂蒸汽通道与新增吸收-蒸发器 (K) 连通， 第一蒸发器 （6 ) 或第一冷凝器 （4) 增设冷剂液管路经新增冷剂液泵 （L) 与新 增吸收-蒸发器（K)连通后新增吸收-蒸发器（K)再有冷剂蒸汽通道与吸收器（3)连通、 或 第二冷凝器 （5) 增设冷剂液管路经新增节流阀 （C) 与新增吸收-蒸发器 （K) 连通后新增吸 收-蒸发器（K)再有冷剂蒸汽通道与吸收器（3)连通， 形成以回热式 1. 5级为低温发生流程 的第三类吸收式热泵。 Flow valve, connect the concentrated solution provider with concentrated solution line and absorber (3) to adjust to a concentrated solution provider with concentrated solution line through new solution heat exchanger (B) and new absorption-evaporator (K Connected, the new absorption-evaporator (K) and the dilute solution line are connected to the absorber (3) via the new solution pump (D) and the new solution heat exchanger (B), and the first evaporator ( 6) The refrigerant vapor channel is connected to the absorber (3) to adjust to the first evaporator (6). The refrigerant vapor channel is connected to the new absorption-evaporator (K), the first evaporator (6) or the first The condenser (4) is added with a refrigerant liquid pipeline. The new refrigerant liquid pump (L) is connected with the new absorption-evaporator (K), and then the absorption-evaporator (K) is added to the refrigerant vapor channel and absorption. (3) connected, or the second condenser (5) is added with a refrigerant liquid line. After the new throttle valve (C) is connected with the new absorption-evaporator (K), the absorption-evaporator (K) is added. Further, a refrigerant vapor passage is connected to the absorber (3) to form a third type of absorption heat pump in which the heat recovery type 1.5 is a low temperature generation process.
82. 第三类吸收式热泵， 是在权利要求 2-3、 21- 28内任一权利要求所述的第三类吸收 式热泵中， 增加新增溶液热交换器、 新增溶液泵、 新增吸收-蒸发器、 新增冷剂液泵或新增节 流阀， 将分汽室 （17) 有浓溶液管路经第二溶液泵 （14) 和第三溶液热交换器 （15 ) 与第二 溶液热交换器（11 )连通调整为分汽室 （17)有浓溶液管路经第二溶液泵 （14)、 第三溶液热 交换器（15)和新增溶液热交换器（B)与新增吸收-蒸发器（K)连通， 新增吸收-蒸发器（K) 还有稀溶液管路经新增溶液泵 （D) 和新增溶液热交换器 （B) 与第二溶液热交换器 （11 ) 连 通， 将第一蒸发器（6)有冷剂蒸汽通道与吸收器（3)连通调整为第一蒸发器（6)有冷剂蒸 汽通道与新增吸收-蒸发器 （K) 连通， 蒸发器 （6) 或第一冷凝器 （4) 增设冷剂液管路经新 增冷剂液泵（L) 与新增吸收-蒸发器（Κ)连通后新增吸收-蒸发器 （Κ)再有冷剂蒸汽通道与 吸收器 （3) 连通、 或第二冷凝器 （5) 增设冷剂液管路经新增节流阀 （C) 与新增吸收 -蒸发 器 （Κ) 连通后新增吸收-蒸发器 （Κ) 再有冷剂蒸汽通道与吸收器 （3) 连通， 形成以回热式 1. 5级为低温发生流程的第三类吸收式热泵。  82. The third type of absorption heat pump is the third type of absorption heat pump according to any one of claims 2-3, 21-28, adding a new solution heat exchanger, adding a new solution pump, and a new An absorption-evaporator, a new refrigerant liquid pump or a new throttle valve, and a concentrated solution line of the steam distribution chamber (17) through the second solution pump (14) and the third solution heat exchanger (15) The second solution heat exchanger (11) is connected to be adjusted into a steam dividing chamber (17) having a concentrated solution line passing through the second solution pump (14), the third solution heat exchanger (15) and the new solution heat exchanger (B). ) connected to the new absorption-evaporator (K), new absorption-evaporator (K) and dilute solution line via new solution pump (D) and new solution heat exchanger (B) and second solution The heat exchanger (11) is connected to connect the refrigerant vapor channel of the first evaporator (6) with the absorber (3) to adjust the first evaporator (6) with a refrigerant vapor channel and a new absorption-evaporator ( K) Connect, evaporator (6) or first condenser (4) Add refrigerant liquid line via new refrigerant pump (L) and new absorption-evaporator (Κ) After the pass, add the absorption-evaporator (Κ) and then connect the refrigerant vapor channel to the absorber (3), or the second condenser (5) to add the coolant line through the new throttle valve (C) and the new The absorption-evaporator (Κ) is connected to the new absorption-evaporator (Κ) and then the refrigerant vapor channel is connected to the absorber (3) to form a third type of regenerative type 1.5 low temperature generation process. Absorption heat pump.
83. 第三类吸收式热泵， 是在权利要求 4、 29-36内任一权利要求所述的第三类吸收式 热泵中， 增加新增溶液热交换器、 新增吸收-蒸发器、 新增冷剂液泵或新增节流阀， 将吸收器 83. A third type of absorption heat pump, which is a third type absorption heat pump according to any one of claims 4, 29-36, adding a new solution heat exchanger, adding an absorption-evaporator, a new Refrigerant liquid pump or new throttle valve, will be the absorber
(3) 有稀溶液管路经第三溶液热交换器 （15 ) 和吸收-发生器 （16) 与分汽室 （17) 连通调 整为吸收器 （3) 有稀溶液管路经新增溶液热交换器 （Β) 与新增吸收-蒸发器 （Κ) 连通， 新 增吸收-蒸发器（Κ)还有稀溶液管路经第三溶液热交换器（15 )和吸收-发生器（16)与分汽 室 （17) 连通， 将第二溶液泵 （14) 有浓溶液管路经第三溶液热交换器 （15) 与第二溶液热 交换器 （11 ) 连通调整为第二溶液泵 （14) 有浓溶液管路经第三溶液热交换器 （15) 和新增 溶液热交换器（Β) 与第二溶液热交换器（11 )连通， 将第二蒸发器（19) 有冷剂蒸汽通道与 吸收器（3)连通调整为第二蒸发器（19)有冷剂蒸汽通道与新增吸收-蒸发器（Κ)连通， 第 三冷凝器 （18 ) 或第二蒸发器 （19 ) 增设冷剂液管路经新增冷剂液泵 （L) 与新增吸收-蒸发 器 （Κ) 连通后新增吸收-蒸发器 （Κ) 再有冷剂蒸汽通道与吸收器 （3) 连通、 或第二冷凝器(3) The dilute solution line is connected to the steam distribution chamber (17) through the third solution heat exchanger (15) and the absorption-generator (16) to adjust to the absorber (3) The heat exchanger (Β) is connected to the new absorption-evaporator (Κ), the new absorption-evaporator (Κ) and the dilute solution line are passed through the third solution heat exchanger (15) and the absorption-generator (16). Connecting with the steam dividing chamber (17), adjusting the second solution pump (14) concentrated solution line to the second solution heat exchanger (15) and the second solution heat exchanger (11) to adjust to the second solution pump (14) The concentrated solution line is connected to the second solution heat exchanger (11) via the third solution heat exchanger (15) and the new solution heat exchanger (Β), and the second evaporator (19) is cold. The agent vapor passage is connected to the absorber (3) to be adjusted to be a second evaporator (19) having a refrigerant vapor passage communicating with a new absorption-evaporator (Κ), a third condenser (18) or a second evaporator (19) The additional refrigerant liquid line is connected with the new absorption liquid evaporator (L) and the new absorption-evaporator (Κ), and then the absorption-evaporator (Κ) is added. (3) communicates with the refrigerant vapor channel absorber, or the second condenser
(5)增设冷剂液管路经新增节流阀（C)与新增吸收-蒸发器（Κ)连通后新增吸收-蒸发器（Κ) 再有冷剂蒸汽通道与吸收器（3)连通， 以回热式 1. 5级为低温发生流程的第三类吸收式热泵。 (5) Adding a refrigerant liquid pipeline through the addition of a new throttle valve (C) and a new absorption-evaporator (Κ) to add an absorption-evaporator (Κ) and then a refrigerant vapor channel and absorber (3) The third type of absorption heat pump that is connected to the regenerative type 1.5 is a low temperature generation process.
84. 第三类吸收式热泵， 是在权利要求 4、 29-36内任一权利要求所述的第三类吸收式 热泵中， 增加新增溶液热交换器、 新增溶液泵、 新增吸收-蒸发器、 新增冷剂液泵或新增节流 阀， 将浓溶液提供器有浓溶液管路与吸收器（3 )连通调整为浓溶液提供器有浓溶液管路经新 增溶液热交换器（Β) 与新增吸收-蒸发器（Κ)连通， 新增吸收-蒸发器（Κ)还有稀溶液管路 经新增溶液泵 （D)和新增溶液热交换器 （Β) 与吸收器 （3) 连通， 将第二蒸发器 （19) 有冷 剂蒸汽通道与吸收器 （3) 连通调整为第二蒸发器 （19) 有冷剂蒸汽通道与新增吸收-蒸发器 权 利 要 求 书 84. The third type of absorption heat pump is the third type absorption heat pump according to any one of claims 4, 29-36, adding a new solution heat exchanger, adding a new solution pump, adding new absorption - Evaporator, new coolant pump or new throttle valve, connect the concentrated solution provider with concentrated solution line and absorber (3) to adjust the concentrated solution to the thick solution line. The exchanger (Β) is connected to the new absorption-evaporator (Κ), the new absorption-evaporator (Κ) and the dilute solution line via the new solution pump (D) and the new solution heat exchanger (Β) Connected to the absorber (3), the second evaporator (19) has a refrigerant vapor channel connected to the absorber (3) and is adjusted to a second evaporator (19) with a refrigerant vapor channel and a new absorption-evaporator Claim
― WO 2013/003982 PCT/CN2011/001118  ― WO 2013/003982 PCT/CN2011/001118
( ) 连通， 第三冷凝器 （18) 或第二蒸发器 （19) 增设冷剂液管路经新增冷剂液泵 （L) 与 新增吸收-蒸发器 （K) 连通后新增吸收-蒸发器 （K) 再有冷剂蒸汽通道与吸收器 （3) 连通、 或第二冷凝器 （5) 增设冷剂液管路经新增节流阀 （C) 与新增吸收-蒸发器 （K) 连通后新增 吸收-蒸发器（K)再有冷剂蒸汽通道与吸收器（3 )连通， 形成以回热式 1. 5级为低温发生流 程的第三类吸收式热泵。  ( ) Connected, the third condenser (18) or the second evaporator (19) is added with a refrigerant liquid line. The new refrigerant liquid pump (L) is connected to the new absorption-evaporator (K) to add absorption. - The evaporator (K) has a refrigerant vapor passage connected to the absorber (3), or the second condenser (5) is provided with a refrigerant liquid line via a new throttle valve (C) and a new absorption-evaporator (K) After the connection, a new absorption-evaporator (K) is connected, and a refrigerant vapor channel is connected to the absorber (3) to form a third type of absorption heat pump in which the regenerative type 1.5 is a low temperature generation process.
85. 第三类吸收式热泵， 是在权利要求 4、 29-36内任一权利要求所述的第三类吸收式 热泵中， 增加新增溶液热交换器、 新增溶液泵、 新增吸收-蒸发器、 新增冷剂液泵或新增节流 阀， 将分汽室 （17 ) 有浓溶液管路经第二溶液泵 （14) 和第三溶液热交换器 （15 ) 与第二溶 液热交换器（11 )连通调整为分汽室 （17)有浓溶液管路经第二溶液泵（14)、 第三溶液热交 换器 （15 ) 和新增溶液热交换器 （B) 与新增吸收-蒸发器 （K) 连通， 新增吸收-蒸发器 （K) 还有稀溶液管路经新增溶液泵 （D) 和新增溶液热交换器 （B) 与第二溶液热交换器 （11 ) 连 通， 将第二蒸发器（19 )有冷剂蒸汽通道与吸收器 （3)连通调整为第二蒸发器（19)有冷剂 蒸汽通道与新增吸收-蒸发器 （K) 连通， 第三冷凝器 （18) 或第二蒸发器 （19) 增设冷剂液 管路经新增冷剂液泵（L) 与新增吸收-蒸发器（Κ)连通后新增吸收-蒸发器（Κ)再有冷剂蒸 汽通道与吸收器（3)连通、 或第二冷凝器（5)增设冷剂液管路经新增节流阀 （C) 与新增吸 收-蒸发器（Κ)连通后新增吸收-蒸发器（Κ) 再有冷剂蒸汽通道与吸收器（3)连通， 形成以 回热式 1. 5级为低温发生流程的第三类吸收式热泵。  85. The third type of absorption heat pump is the third type absorption heat pump according to any one of claims 4, 29-36, adding a new solution heat exchanger, adding a new solution pump, adding new absorption - evaporator, new coolant pump or new throttle valve, the split solution chamber (17) has a concentrated solution line through the second solution pump (14) and the third solution heat exchanger (15) and the second The solution heat exchanger (11) is connected and adjusted to a steam separation chamber (17) having a concentrated solution line via a second solution pump (14), a third solution heat exchanger (15) and a new solution heat exchanger (B). New absorption-evaporator (K) connection, new absorption-evaporator (K) and dilute solution line exchanged with the second solution via the new solution pump (D) and the new solution heat exchanger (B) The device (11) is connected, and the second evaporator (19) has a refrigerant vapor channel connected to the absorber (3) to be adjusted to a second evaporator (19) with a refrigerant vapor channel and a new absorption-evaporator (K) Connected, the third condenser (18) or the second evaporator (19) is added with a refrigerant liquid line via a new refrigerant liquid pump (L) and newly absorbed - After the evaporator (Κ) is connected, a new absorption-evaporator (Κ) is added, and then a refrigerant vapor channel is connected to the absorber (3), or a second condenser (5) is provided with a refrigerant liquid line through a new throttle valve. (C) After the connection with the new absorption-evaporator (Κ), the absorption-evaporator (Κ) is added, and then the refrigerant vapor channel is connected to the absorber (3). The third type of absorption heat pump for the process.
86. 第三类吸收式热泵， 是在权利要求 4、 29-36内任一权利要求所述的第三类吸收式 热泵中， 增加新增溶液热交换器、 新增吸收 -蒸发器和新增冷剂液泵， 将吸收-发生器 （16) 有稀溶液管路经第一溶液热交换器 （10) 与第一发生器 （1 ) 连通调整为吸收-发生器 （16) 有稀溶液管路经第一溶液热交换器（10)与新增吸收-蒸发器（Κ)连通，新增吸收-蒸发器（Κ) 还有稀溶液管路经新增溶液热交换器（Β) 与第一发生器 （1 )连通， 将第一发生器（1 )有浓 溶液管路经第一溶液泵 （7 ) 和第一溶液热交换器 （10) 与吸收-发生器 （16) 连通调整为第 一发生器 （1 ) 有浓溶液管路经第一溶液泵 （7)、 新增溶液热交换器 （Β) 和第一溶液热交换 器（10)与吸收-发生器（16)连通， 将第一蒸发器（6)有冷剂蒸汽通道与吸收-发生器（16) 连通调整为第一蒸发器（6)有冷剂蒸汽通道与新增吸收-蒸发器（Κ)连通， 第一冷凝器（4) 或第一蒸发器（6)增设冷剂液管路经新增吸收-蒸发器（Κ)连通后新增吸收-蒸发器（Κ)还 有冷剂蒸汽通道与吸收-发生器（16)连通， 形成以回热式 1. 5级为低温发生流程的第三类吸 收式热泵。  86. A third type of absorption heat pump, which is a third type absorption heat pump according to any one of claims 4, 29-36, adding a new solution heat exchanger, adding an absorption-evaporator and a new one. a refrigerant pump, the absorption-generator (16) has a dilute solution line connected to the first generator (1) via the first solution heat exchanger (10) to adjust to an absorption-generator (16) with a dilute solution The pipeline is connected to the newly added absorption-evaporator (Κ) via the first solution heat exchanger (10), and the new absorption-evaporator (Κ) and the dilute solution pipeline are connected to the new solution heat exchanger (Β). The first generator (1) is connected, and the first generator (1) has a concentrated solution pipeline connected to the first solution pump (7) and the first solution heat exchanger (10) and the absorption-generator (16). a first solution (1) having a concentrated solution line connected to the absorption-generator (16) via a first solution pump (7), a new solution heat exchanger (Β), and a first solution heat exchanger (10) , the first evaporator (6) has a refrigerant vapor channel connected to the absorption-generator (16) to adjust to a first evaporator (6) with a refrigerant vapor pass The road is connected with a new absorption-evaporator (Κ), and the first condenser (4) or the first evaporator (6) is provided with a refrigerant liquid pipeline connected by a new absorption-evaporator (Κ) and newly absorbed. The evaporator (Κ) and the refrigerant vapor passage are connected to the absorption-generator (16) to form a third type of absorption heat pump in which the regenerative type 1.5 is a low temperature generation process.
87. 第三类吸收式热泵， 是在权利要求 4、 29-36内任一权利要求所述的第三类吸收式 热泵中， 增加新增溶液热交换器、 新增溶液泵、 新增吸收 -蒸发器和新增冷剂液泵， 将第一发 生器 （1 ) 有浓溶液管路经第一溶液泵 （7 ) 和第一溶液热交换器 （10) 与吸收-发生器 （16) 连通调整为第一发生器 （1 ) 有浓溶液管路经第一溶液泵 （7 ) 和第一溶液热交换器 （10) 与 新增吸收-蒸发器（Κ)连通， 新增吸收-蒸发器（Κ)还有稀溶液管路经新增溶液泵（D)和新 增溶液热交换器（Β) 与吸收-发生器 （16)连通， 将吸收-发生器 （16)有稀溶液管路经第一 溶液热交换器 （10) 与第一发生器 （1 ) 连通调整为吸收-发生器 （16) 有稀溶液管路经新增 溶液热交换器 （Β) 和第一溶液热交换器 （10) 与第一发生器 （1 ) 连通， 将第一蒸发器 （6) 有冷剂蒸汽通道与吸收-发生器 （16) 连通调整为第一蒸发器 （6) 有冷剂蒸汽通道与新增吸 收-蒸发器（Κ)连通， 第一冷凝器（4)或第一蒸发器（6) 增设冷剂液管路经新增吸收 -蒸发 器 （Κ) 连通后新增吸收-蒸发器 （Κ) 还有冷剂蒸汽通道与吸收-发生器 （16) 连通， 形成以 回热式 1. 5级为低温发生流程的第三类吸收式热泵。  87. The third type of absorption heat pump is the third type absorption heat pump according to any one of claims 4, 29-36, adding a new solution heat exchanger, adding a new solution pump, adding new absorption - an evaporator and a new refrigerant liquid pump, the first generator (1) has a concentrated solution line through the first solution pump (7) and the first solution heat exchanger (10) and the absorption-generator (16) The connection is adjusted to the first generator (1). The concentrated solution line is connected to the first absorption pump (7) via the first solution pump (7) and the first solution heat exchanger (10), and the absorption-evaporation is newly added. (稀) and the dilute solution line is connected to the absorption-generator (16) via a new solution pump (D) and a new solution heat exchanger (Β), and the absorption-generator (16) has a dilute solution tube. The first solution heat exchanger (10) is connected to the first generator (1) and is adjusted to be an absorption-generator (16). The dilute solution line is exchanged with the first solution through the new solution heat exchanger (Β) and the first solution. The device (10) is in communication with the first generator (1), and the first evaporator (6) has a refrigerant vapor channel and an absorption-generator (16) The connection is adjusted to the first evaporator (6). The refrigerant vapor passage is connected to the new absorption-evaporator (Κ), and the first condenser (4) or the first evaporator (6) is provided with a refrigerant liquid line. The new absorption-evaporator (Κ) is connected to the new absorption-evaporator (Κ) and the refrigerant vapor channel is connected to the absorption-generator (16) to form a regenerative type 1.5. The third type of absorption heat pump.
PCT/CN2011/001118 2011-07-06 2011-07-06 Third-type absorption heat pump WO2013003982A1 (en)

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