WO2015143927A1 - 第五类吸收式热泵 - Google Patents

第五类吸收式热泵 Download PDF

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Publication number
WO2015143927A1
WO2015143927A1 PCT/CN2015/000204 CN2015000204W WO2015143927A1 WO 2015143927 A1 WO2015143927 A1 WO 2015143927A1 CN 2015000204 W CN2015000204 W CN 2015000204W WO 2015143927 A1 WO2015143927 A1 WO 2015143927A1
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Prior art keywords
generator
solution
absorber
heat exchanger
new
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PCT/CN2015/000204
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English (en)
French (fr)
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李华玉
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李华玉
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Publication of WO2015143927A1 publication Critical patent/WO2015143927A1/zh

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    • 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
    • F25B15/12—Sorption machines, plants or systems, operating continuously, e.g. absorption type with resorber
    • 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
    • F25B30/00—Heat pumps
    • F25B30/04—Heat pumps of the sorption type
    • 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
    • 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
    • F25B15/02—Sorption machines, plants or systems, operating continuously, e.g. absorption type without inert gas
    • 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
    • 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
    • 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

Definitions

  • the invention belongs to the technical field of absorption heat pump and waste heat utilization.
  • the main purpose of the present invention is to provide a fifth type of absorption heat pump, and the specific contents of the invention are as follows:
  • the fifth type of absorption heat pump is mainly composed of a generator, a second generator, a third generator, an absorber, a second absorber, a condenser, an evaporator, a throttle valve, a solution pump, a second solution pump, a solution heat exchanger and a second solution heat exchanger; the absorber has a dilute solution line connected to the second absorber via the solution heat exchanger, and the second absorber has a dilute solution line through the solution pump and the second solution
  • the heat exchanger is connected to the generator, the generator has a concentrated solution pipeline connected to the second generator via the second solution heat exchanger, and the second generator has a concentrated solution pipeline connected to the third generator, and the third occurs
  • the concentrated solution pipeline is connected to the absorber via the second solution pump and the solution heat exchanger, and the generator and the refrigerant vapor passage are connected to the condenser, and the condenser and the refrigerant liquid pipeline are connected to the third generator.
  • the fifth type of absorption heat pump is the fifth type of absorption heat pump according to item 1, wherein the throttle valve is eliminated, and the third generator has a refrigerant liquid line connected to the evaporator through the throttle valve. A refrigerant liquid line is connected to the evaporator for the third generator to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump is a fifth type of absorption heat pump according to the first item, wherein the fourth generator, the second throttle valve, the third solution pump, the third solution heat exchanger and the heat are added.
  • the exchanger, the second absorber is provided with a dilute solution pipeline
  • the three solution pump and the third solution heat exchanger are in communication with the fourth generator, and the fourth generator and the concentrated solution line are connected to the second generator via the third solution heat exchanger, and the generator has a refrigerant vapor channel and
  • the condenser is connected to adjust the generator to have a refrigerant vapor passage communicating with the fourth generator, and then the fourth generator is further connected to the evaporator via the heat exchanger, the third generator and the second throttle valve.
  • the fourth generator also has a refrigerant vapor passage communicating with the condenser, and the heat exchanger and the heated medium conduit communicate with the outside to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump is the fifth type of absorption heat pump according to item 1, wherein the fourth generator, the second throttle valve, the third solution heat exchanger and the heat exchanger are added,
  • the second absorber has a dilute solution line connected to the generator through the solution pump and the second solution heat exchanger to adjust the second absorber to have a dilute solution line through the solution pump, the second solution heat exchanger and the third solution heat exchanger Connected with the generator, the generator has a concentrated solution pipeline connected to the second generator via the second solution heat exchanger to adjust the generator to have a concentrated solution pipeline connected to the fourth generator via the third solution heat exchanger,
  • the four generators further have a concentrated solution pipeline communicating with the second generator via the second solution heat exchanger, and the generator has a refrigerant vapor passage communicating with the condenser to adjust the generator to have a refrigerant vapor passage communicating with the fourth generator.
  • the fourth generator further has a refrigerant liquid pipeline connected to the evaporator via the heat exchanger, the third generator and the second throttle valve, and the fourth generator further has a refrigerant vapor passage communicating with the condenser, the heat exchanger And the heated medium pipe communicates with the outside to form Five absorption heat pump.
  • the fifth type of absorption heat pump is a fifth type of absorption heat pump according to the first item, wherein the fourth generator, the second throttle valve, the third solution pump, the third solution heat exchanger and the heat are added.
  • An exchanger wherein the second absorber has a dilute solution line connected to the generator through the solution pump and the second solution heat exchanger to adjust the second absorber to have a dilute solution line through the solution pump and the second solution heat exchanger and
  • the fourth generator is connected, and the fourth generator further has a concentrated solution pipeline connected to the generator via the third solution pump and the third solution heat exchanger, and the generator has a concentrated solution pipeline through the second solution heat exchanger and the second
  • the generator is connected to adjust the generator to have a concentrated solution pipeline connected to the second generator via the third solution heat exchanger and the second solution heat exchanger, and the generator has a refrigerant vapor passage connected to the condenser to adjust the generator to have After the refrigerant vapor passage is in communication with the fourth generator, the fourth generator further has a ref
  • the fifth type of absorption heat pump is the fifth type of absorption heat pump according to item 3-5, wherein the throttle valve and the second throttle valve are eliminated, and the third generator has a refrigerant liquid pipe.
  • the passage throttle valve is connected to the evaporator to be adjusted so that the third generator has a refrigerant liquid pipeline connected with the evaporator, and the third generator has a refrigerant liquid pipeline connected to the evaporator through the second throttle valve to be adjusted to the first
  • the three generators have a refrigerant liquid line connected to the evaporator to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump is a fifth type generator, a third throttle valve, a fourth solution pump, a fourth solution heat exchanger, and a fifth type of absorption heat pump according to item 3.
  • a second heat exchanger the second absorber is provided with a dilute solution pipeline connected to the fifth generator via the fourth solution pump and the fourth solution heat exchanger, and the fifth generator has a concentrated solution pipeline through the fourth solution heat exchanger Communicating with the second generator, the fifth generator further has a refrigerant vapor passage communicating with the condenser, and the fourth generator has a refrigerant vapor passage communicating with the condenser to adjust the fourth generator to have a refrigerant vapor passage and a fifth After the generator is connected, the fifth generator further has a refrigerant liquid pipeline connected to the evaporator via the second heat exchanger, the third generator and the third throttle valve, and the fourth generator has a coolant liquid pipeline through the heat.
  • the fifth type of absorption heat pump is the fifth type of absorption heat pump of the fifth type of absorption heat pump described in item 4 a three-throttle valve, a fourth solution heat exchanger and a second heat exchanger, wherein the second absorber has a dilute solution line connected to the generator through the solution pump, the second solution heat exchanger and the third solution heat exchanger
  • the second absorber has a dilute solution line connected to the generator via the solution pump, the fourth solution heat exchanger, the second solution heat exchanger and the third solution heat exchanger
  • the fourth generator has a concentrated solution line
  • the two solution heat exchanger is connected to the second generator to be adjusted so that the fourth generator has a concentrated solution line connected to the fifth generator via the second solution heat exchanger, and the fifth generator has a concentrated solution line through the fourth solution
  • the heat exchanger is in communication with the second generator, the fifth generator further has a refrigerant vapor passage communicating with the condenser, and the fourth generator has a refrigerant vapor passage communicating with the condenser to
  • the fifth generator has a second coolant flow through the coolant line
  • the third generator and the third throttle valve are in communication with the evaporator
  • the fourth generator has a refrigerant liquid pipeline connected to the evaporator through the heat exchanger, the third generator and the second throttle valve to be adjusted to the first
  • the fourth generator has a refrigerant liquid pipeline connected to the evaporator via the fifth generator, the heat exchanger, the third generator and the second throttle valve, and the second heat exchanger and the heated medium pipeline communicate with the outside.
  • a fifth type of absorption heat pump is formed.
  • the fifth type of absorption heat pump is the fifth type of absorption heat pump according to any of the items 7-9, wherein the throttle valve, the second throttle valve and the third throttle valve are eliminated, and the third generation occurs.
  • the refrigerant liquid pipeline is connected to the evaporator through the throttle valve to be adjusted to be a third generator having a refrigerant liquid pipeline connected with the evaporator, and the third generator has a refrigerant liquid pipeline passing through the second throttle valve and
  • the evaporator is connected to adjust the third generator to have a refrigerant liquid pipeline communicating with the evaporator, and the third generator has a refrigerant liquid pipeline connected to the evaporator through the third throttle valve to be adjusted to a third generator having a refrigerant
  • the liquid line communicates with the evaporator to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump is the fifth type of absorption heat pump according to item 11, wherein the throttle valve is eliminated, and the third generator has a refrigerant liquid line connected to the evaporator through the throttle valve. A refrigerant liquid line is connected to the evaporator for the third generator to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump is the fifth type, the second throttle valve, the fourth solution pump, the fourth solution heat exchanger and the heat in the fifth type absorption heat pump according to item 11.
  • the exchanger, the third absorber is provided with a dilute solution pipeline connected to the fifth generator via the fourth solution pump and the fourth solution heat exchanger, and the fifth generator has a concentrated solution pipeline through the fourth solution heat exchanger and the third
  • the four generators are connected, and the generator has a refrigerant vapor passage connected to the condenser to adjust the generator to have a refrigerant vapor passage connected to the fifth generator, and then the fifth generator has a refrigerant liquid pipeline through the heat exchanger,
  • the third generator and the second throttle valve are in communication with the evaporator, the fifth generator and the refrigerant vapor passage are connected to the condenser, and the heat exchanger and the heated medium pipeline communicate with the outside to form a fifth type of absorption heat pump. .
  • the fifth type of absorption heat pump is the fifth type, the second throttle valve, the fourth solution pump, the fourth solution heat exchanger and the heat in the fifth type absorption heat pump according to item 11.
  • the exchanger adjusts the third absorber having a dilute solution line through the third solution pump and the third solution heat exchanger to the generator to adjust the third absorber to have a dilute solution line through the third solution pump and the third solution heat
  • the exchanger is connected to the fifth generator, and the fifth generator further has a concentrated solution pipeline connected to the generator via the fourth solution pump and the fourth solution heat exchanger, and the generator has a concentrated solution pipeline through the third solution heat exchange
  • the generator is connected to the fourth generator to adjust the generator to have a concentrated solution pipeline connected to the fourth generator via the fourth solution heat exchanger and the third solution heat exchanger, and the generator has a refrigerant vapor passage connected to the condenser.
  • the fifth generator is further connected with the refrigerant through the heat exchanger, the third generator and the second throttle valve, and the fifth generator There is also a refrigerant vapor passage communicating with the condenser, the heat exchanger There is a heating medium conduit communicating with the outside, forming a fifth type absorption heat pump.
  • the fifth type of absorption heat pump is the fifth type of absorption heat pump according to any of the items 13-16, wherein the throttle valve and the second throttle valve are eliminated, and the third generator has a refrigerant liquid pipe.
  • the passage throttle valve is connected to the evaporator to be adjusted to have a third generator
  • the refrigerant liquid pipeline is connected with the evaporator
  • the third generator has a refrigerant liquid pipeline connected to the evaporator through the second throttle valve to be adjusted to be a third generator, and the refrigerant liquid pipeline is connected with the evaporator to form a first Five types of absorption heat pumps.
  • the fifth type of absorption heat pump is the fifth type of absorption heat pump according to item 18, wherein the throttle valve is eliminated, and the new generator has a refrigerant liquid pipeline through the throttle valve and the evaporator.
  • the connection adjustment is such that the newly added generator has a refrigerant liquid line connected to the evaporator to form a fifth type of absorption heat pump.
  • the third generator has a concentrated solution pipeline connected to the newly added generator through the solution heat exchanger, and the new generator and the concentrated solution pipeline are connected to the absorber through the second solution pump and the new solution heat exchanger.
  • the generator and the refrigerant vapor passage are connected with the newly added absorber, and the third generator has a refrigerant liquid pipeline connected to the evaporator through the throttle valve to be adjusted to a third generator having a refrigerant liquid pipeline and adding After the generator is connected, the generator is added and then the refrigerant liquid pipeline is passed through the throttle valve and evaporated.
  • the third generator has a refrigerant liquid pipeline connected to the evaporator through the second throttle valve to be adjusted to a third generator.
  • the refrigerant liquid pipeline is connected with the newly added generator, and the new generator is further provided with a refrigerant.
  • the liquid pipeline communicates with the evaporator via the second throttle valve, and the newly added absorber and the cooling medium pipeline communicate with the outside to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump is to add a new generator, a new absorber, a new solution pump and a new solution heat exchange in any of the fifth type absorption heat pumps described in items 7-9.
  • the absorber has a dilute solution pipeline connected to the second absorber through the solution heat exchanger to adjust the absorber to a dilute solution pipeline, and the new solution heat exchanger is connected with the newly added absorber, and the new absorber is further added.
  • the dilute solution pipeline is connected to the second absorber through the new solution pump and the solution heat exchanger, and the third generator has a concentrated solution pipeline connected to the absorber through the second solution pump and the solution heat exchanger to adjust to the third occurrence.
  • the concentrated solution pipeline is connected to the newly added generator through the solution heat exchanger, and the new generator and the concentrated solution pipeline are connected to the absorber through the second solution pump and the newly added solution heat exchanger, and the new generator is further connected.
  • the generator has a refrigerant liquid pipeline connected to the evaporator through the throttle valve to be adjusted to a third generator.
  • the refrigerant liquid pipeline is connected with the newly added generator, and the new generator is further provided with a refrigerant liquid pipeline through the throttle valve.
  • the third generator Connected with the evaporator, the third generator has a refrigerant liquid pipeline connected to the evaporator through the second throttle valve to be adjusted to a third generator, and the refrigerant liquid pipeline is connected with the newly added generator, and then the generator is added.
  • the refrigerant liquid pipeline is connected to the evaporator through the second throttle valve, and the third generator has a refrigerant liquid pipeline connected to the evaporator through the third throttle valve to be adjusted to a third generator having a refrigerant liquid pipeline
  • the new generator is added, and the refrigerant liquid pipeline is connected to the evaporator through the third throttle valve, and the new absorber and the cooling medium pipeline communicate with the outside to form a fifth type of absorption heat pump. .
  • the fifth type of absorption heat pump is the fifth type of absorption heat pump according to item 22, wherein the throttle valve, the second throttle valve and the third throttle valve are eliminated, and the new generator has The refrigerant liquid pipeline is connected to the evaporator through the throttle valve to adjust the new generator to have a refrigerant liquid pipeline connected with the evaporator, and the newly added generator has a refrigerant liquid pipeline through the second throttle valve and the evaporator.
  • the connection adjustment is such that the newly added generator has a refrigerant liquid pipeline connected with the evaporator, and the newly added generator has a refrigerant liquid pipeline connected to the evaporator through the third throttle valve and is adjusted to be a new generator with a refrigerant liquid pipe.
  • the road is connected to the evaporator to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump is a fifth type of absorption heat pump according to item 1 or 11, adding a new generator, a new absorber, a new solution pump and a new solution heat exchanger.
  • the absorber has a dilute solution pipeline connected to the second absorber through the solution heat exchanger to adjust the absorber to a dilute solution pipeline, and the new solution heat exchanger is connected with the newly added absorber, and the new absorber is further diluted.
  • the solution pipeline is connected to the second absorber through the new solution pump and the solution heat exchanger, and the third generator has a concentrated solution pipeline connected to the absorber through the second solution pump and the solution heat exchanger to be adjusted to the third generator.
  • the concentrated solution pipeline is connected to the newly added generator through the solution heat exchanger, and the newly added generator and the concentrated solution pipeline are connected to the absorber through the second solution pump and the newly added solution heat exchanger, and the new generator is further added.
  • the refrigerant vapor passage is connected with the newly added absorber, and the newly added generator and the residual heat medium pipeline communicate with the outside, and the newly added absorber and the cooling medium pipeline communicate with the outside to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump is the fifth type of absorption heat pump according to item 24, wherein the throttle valve is eliminated, and the third generator has a refrigerant liquid line through the throttle valve and the evaporator The communication is adjusted such that the third generator has a refrigerant liquid line connected to the evaporator to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump is to add new generators, new absorbers, new solution pumps and new ones in the fifth type of absorption heat pumps described in items 3-5 and 13-16.
  • the solution heat exchanger has a dilute solution pipeline connected to the absorber through the solution heat exchanger and the second absorber to adjust the absorber to have a dilute solution pipeline connected to the newly added absorber through the new solution heat exchanger, newly added
  • the absorber further has a dilute solution pipeline connected to the second absorber through the new solution pump and the solution heat exchanger
  • the third generator has a concentrated solution pipeline connected to the absorber through the second solution pump and the solution heat exchanger.
  • the third generator has a concentrated solution pipeline connected to the newly added generator through the solution heat exchanger, and the new generator and the concentrated solution pipeline are connected to the absorber through the second solution pump and the new solution heat exchanger.
  • the generator and the refrigerant vapor channel are connected with the newly added absorber, and the new generator and the waste heat medium pipeline are connected to the outside, and the newly added absorber and the cooling medium pipeline are connected with the outside to form the fifth type of absorption type. Heat pump.
  • the fifth type of absorption heat pump is the fifth type of absorption heat pump according to item 26, wherein the throttle valve and the second throttle valve are eliminated, and the third generator has a refrigerant liquid line
  • the throttle valve is connected to the evaporator to be adjusted so that the third generator has a refrigerant liquid pipeline connected with the evaporator, and the third generator has a refrigerant liquid pipeline connected to the evaporator through the second throttle valve to be adjusted to a third occurrence.
  • the refrigerant liquid line is connected to the evaporator to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump is added to any of the fifth type of absorption heat pumps described in items 7-9.
  • the generator, the newly added absorber, the newly added solution pump and the newly added solution heat exchanger, and the dilute solution pipeline of the absorber is connected to the second absorber through the solution heat exchanger to adjust the absorber to a dilute solution pipeline through the new
  • the increasing solution heat exchanger is connected with the newly added absorber, and the new absorber and the dilute solution pipeline are connected to the second absorber through the new solution pump and the solution heat exchanger, and the third generator has a concentrated solution pipeline.
  • the second solution pump and the solution heat exchanger are connected to the absorber to be adjusted to be a third generator having a concentrated solution line connected to the new generator via the solution heat exchanger, and the new generator is further provided with a concentrated solution line through the second solution
  • the pump and the new solution heat exchanger are connected to the absorber.
  • the new generator and the refrigerant vapor channel are connected with the newly added absorber.
  • the new generator and the residual heat medium pipeline are connected to the outside, and the new absorber is added.
  • the cooling medium line communicates with the outside to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump is the fifth type of absorption heat pump according to item 28, wherein the throttle valve, the second throttle valve and the third throttle valve are eliminated, and the third generator has The refrigerant liquid pipeline is connected to the evaporator through the throttle valve to be adjusted to be a third generator having a refrigerant liquid pipeline connected to the evaporator, and the third generator has a refrigerant liquid pipeline passing through the second throttle valve and the evaporator
  • the communication is adjusted to be that the third generator has a refrigerant liquid pipeline communicating with the evaporator, and the third generator has a refrigerant liquid pipeline connected to the evaporator through the third throttle valve to be adjusted to a third generator having a refrigerant liquid pipe
  • the road is connected to the evaporator to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump is to add a new generator, a new absorber, a new solution pump and a new solution heat exchange in any of the fifth type absorption heat pumps described in items 1-17.
  • 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 absorber, and the new absorber and the dilute solution pipeline are added with a new solution pump and a new solution heat.
  • the exchanger is connected to the newly added generator, and the newly added generator and the concentrated solution pipeline are connected to the newly added absorber through the newly added solution heat exchanger, and the newly added generator and the refrigerant vapor passage are connected with the absorber.
  • the generator also has a driving heat medium pipe connected to the outside, and the newly added absorber and the heated medium pipe communicate with the outside to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump is a fifth type of absorption heat pump according to any of the items 18-29, adding a second generator, adding a second absorber, and adding a second solution pump. And adding a second solution heat exchanger, connecting the refrigerant refrigerant channel to the absorber to adjust the evaporator to have a refrigerant vapor channel and connecting with the newly added second absorber, adding a second absorber and a dilute solution
  • the pipeline is connected with the newly added second generator by adding a second solution pump and a new second solution heat exchanger, and the second generator and the concentrated solution pipeline are newly added with the second solution heat exchanger and the new
  • the second absorber is connected to connect, and the second generator and the refrigerant vapor channel are connected to the absorber, and the second generator and the driving heat medium pipeline are connected to the outside, and the second absorber is added.
  • the heating medium line communicates with the outside to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump is to add a new generator, a new absorber, a new solution pump and a new one in the fifth type of absorption heat pump described in items 1-2 and 11-12.
  • the increasing solution heat exchanger connects the generator refrigerant vapor passage to the condenser to adjust the generator to have a refrigerant vapor passage and communicates with the newly added absorber, and the newly added absorber and the dilute solution pipeline are added with the new solution pump and
  • the new solution heat exchanger is connected to the newly added generator.
  • the new generator and the concentrated solution pipeline are connected to the newly added absorber through the new solution heat exchanger.
  • the new generator also has a refrigerant vapor passage and a condenser. Connected, the new generator also drives the heat medium pipeline to communicate with the outside, and the new absorber and the heated medium pipeline communicate with the outside to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump is the fifth type of absorption heat pump according to any of the items 1-17, wherein the third generator adds a waste heat medium line to communicate with the outside to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump is the fifth type of absorption heat pump according to any of the items 24-29, wherein the third generator adds a waste heat medium line to communicate with the outside to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump is the fifth type of absorption heat pump according to any of the items 18-23, wherein the third generator and the newly added generator respectively add a waste heat medium pipeline to communicate with the outside to form a first Five types of absorption heat pumps.
  • the fifth type of absorption heat pump is the fifth type of absorption heat pump according to any of the items 18-23, wherein the third generator or the newly added generator adds a waste heat medium pipeline to communicate with the outside to form a fifth Absorption heat pump.
  • the fifth type of absorption heat pump is to add a new generator, a new absorber, a new solution pump and a new solution heat exchanger in any of the fifth type absorption heat pumps described in Item 34.
  • the evaporator has a refrigerant vapor channel and the absorber is connected to adjust the evaporator to have a refrigerant vapor channel and communicate with the newly added absorber, and the new absorber and the dilute solution pipeline are added with a new solution pump and a new solution heat exchanger.
  • the new generator and the concentrated solution pipeline are connected to the newly added absorber through the new solution heat exchanger, and the new generator and the refrigerant vapor passage are connected with the absorber, and the new generator is added.
  • the generator and the concentrated solution pipeline are connected to the newly added absorber through the new solution heat exchanger, and the new generator and the refrigerant vapor passage are connected with the second absorber, and the new generator and the residual heat medium pipeline are added.
  • the new absorber and the cooling medium line communicate with the outside to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump is the fifth type of absorption heat pump according to item 40, wherein the third generator adds a waste heat medium line to communicate with the outside to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump is a fifth type of absorption heat pump according to any of the items 18-23, adding a second generator, adding a second absorber, and adding a second solution pump. And adding a second solution heat exchanger, connecting the newly added generator refrigerant vapor passage with the newly added absorber to adjust the new generator with refrigerant vapor passage and adding a second absorber Passing, adding a second absorber and a dilute solution pipeline, adding a second solution pump and adding a second solution heat exchanger to connect with the newly added second generator, adding a second generator and a concentrated solution tube
  • the second solution heat exchanger added by the road is connected with the newly added second absorber, and the second generator and the refrigerant vapor channel are connected with the newly added absorber, and the second generator and the residual heat medium pipeline are newly added.
  • a new second absorber and a cooling medium line are connected to the outside to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump is the fifth type of absorption heat pump according to item 42, wherein the third generator and the newly added generator respectively add a waste heat medium pipeline to communicate with the outside to form a fifth type. Absorption heat pump.
  • the fifth type of absorption heat pump is any fifth type of absorption heat pump according to item 42, wherein the third generator or the newly added generator adds a waste heat medium pipeline to communicate with the outside to form a fifth type of absorption. Heat pump.
  • the fifth type of absorption heat pump is characterized in that in any of the fifth type absorption heat pumps described in items 24-29, a second generator is added, a second absorber is added, and a second solution pump is added. And adding a second solution heat exchanger, the newly added generator has a refrigerant vapor channel and a new absorber connected to adjust the new generator with a refrigerant vapor channel and a new second absorber to connect, adding a second The absorber and the dilute solution pipeline are connected with the newly added second generator through the addition of the second solution pump and the newly added second solution heat exchanger, and the second generator and the concentrated solution pipeline are added by the second.
  • the solution heat exchanger is connected with the newly added second absorber, and the second generator and the refrigerant vapor passage are connected with the newly added absorber, and the second generator and the residual heat medium pipeline are connected to the outside, and the new one is added.
  • the second absorber also has a cooling medium line that communicates with the outside to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump is a fifth type of absorption heat pump according to any of the items 1-2, 11-12, and 24-25, wherein the second generator has a residual heat medium pipe connected to the outside to be adjusted to
  • the third generator has a residual heat medium pipeline communicating with the outside, and after the condenser has a refrigerant liquid pipeline connected with the third generator, the third generator and the refrigerant liquid pipeline are connected to the evaporator through the throttle valve to be adjusted to After the condenser has a refrigerant liquid pipeline connected to the second generator, the second generator and the refrigerant liquid pipeline communicate with the evaporator through the throttle valve to form a fifth type absorption heat pump.
  • the third generator 3 and the second absorber 5 are combined to reduce the concentration of the solution entering the generator 1, thereby increasing the grade of the refrigerant vapor generated by the generator 1, or reducing the temperature of the generator 1 for driving the heat medium. Requirements, or the use of waste heat resources at lower temperatures.
  • the heat load in the high temperature driving heat medium is released into the refrigerant vapor by the generator 1, a part is transferred to the heated medium through the condenser 6, and the other part is radiated to the cooling by the third generator 3 and the second absorber 5.
  • the medium it is a new technology that utilizes the temperature difference of the high temperature thermal load step-by-step temperature drop to drive the temperature difference.
  • This type of absorption heat pump that drives the temperature difference at a high temperature to drive the temperature difference and simultaneously utilizes the cold environment resources is different from the existing first type of absorption heat pump, the second type of absorption heat pump, and the third type of absorption.
  • Heat pumps are of a new type; they are called the fifth type of absorption heat pumps according to the time of occurrence of the technology and the naming order.
  • Figure 1 is a schematic view showing the first structure and flow of a fifth type of absorption heat pump according to the present invention.
  • FIG 3 is a schematic view showing a third structure and flow of a fifth type of absorption heat pump according to the present invention.
  • FIG. 4 is a fourth structural and flow diagram of a fifth type of absorption heat pump according to the present invention.
  • Figure 5 is a fifth schematic diagram showing the structure and flow of a fifth type of absorption heat pump according to the present invention.
  • Figure 9 is a schematic view showing the structure and flow of a fifth type of absorption heat pump according to the present invention.
  • Figure 10 is a schematic view showing the tenth structure and flow of the fifth type of absorption heat pump according to the present invention.
  • Figure 12 is a schematic view showing the structure and flow of the fifteenth type of absorption heat pump according to the present invention.
  • Figure 14 is a schematic view showing the structure and flow of the fourth type of absorption heat pump of the fifth type according to the present invention.
  • Figure 15 is a schematic view showing the structure and flow of the fifteenth type of absorption heat pump according to the present invention.
  • Figure 18 is a schematic view showing the structure and flow of the eighth type of absorption heat pump of the fifth type according to the present invention.
  • Figure 19 is a schematic view showing the structure and flow of the 19th type of absorption heat pump according to the present invention.
  • the exchanger and the second solution heat exchanger are composed; the absorber 4 has a dilute solution line connected to the second absorber 5 via the solution heat exchanger 11, and the second absorber 5 has a dilute solution line through the solution pump 9 and
  • the second solution heat exchanger 12 is in communication with the generator 1, the generator 1 and the concentrated solution line are in communication with the second generator 2 via the second solution heat exchanger 12, and the second generator 2 has a concentrated solution line and
  • the third generator 3 is in communication, and the third generator 3 and the concentrated solution line are connected to the absorber 4 via the second solution pump 10 and the solution heat exchanger 11, and the generator 1 and the refrigerant vapor passage are connected to the condenser 6.
  • the third generator 3 has a refrigerant liquid line connected to the evaporator 7 via the throttle valve 8, and the second generator 2 and the third
  • the generator 3 also has a refrigerant vapor passage communicating with the second absorber 5, and the evaporator 7 and the refrigerant vapor passage are connected to the absorber 4.
  • the generator 1 also has a driving heat medium pipeline connected to the outside, and the absorber 4 and the condenser 6 are respectively connected to the outside by the heated medium pipeline, and the second generator 2 and the evaporator 7 respectively have a residual heat medium pipeline and Externally connected, the second absorber 5 also has a cooling medium line that communicates with the outside.
  • the dilute solution of the absorber 4 enters the second absorber 5 through the solution heat exchanger 11, absorbs the refrigerant vapor and radiates heat to the cooling medium, and the dilute solution of the second absorber 5 passes through the solution pump 9 and the
  • the two solution heat exchanger 12 enters the generator 1, drives the heat medium to flow through the generator 1, and the solution heated into the solution releases the refrigerant vapor and supplies it to the condenser 6, and the concentrated solution of the generator 1 passes through the second solution heat exchanger.
  • 12 enters the second generator 2, the residual heat medium flows through the second generator 2, and the solution heated therein releases the refrigerant vapor and is supplied to the second absorber 5, and the concentrated solution of the second generator 2 enters the third generator 3.
  • the endothermic release refrigerant vapor is supplied to the second absorber 5, and the concentrated solution of the third generator 3 enters the absorber 4 through the second solution pump 10 and the solution heat exchanger 11, absorbs the refrigerant vapor, and releases the heat.
  • the medium to be heated; the refrigerant vapor of the condenser 6 is radiated to the heated medium to form a refrigerant liquid, and the cold liquid flows through the third generator 3 to release heat, and the coolant liquid after the cooling is throttled through the throttle valve 8
  • the evaporator 7 absorbs heat into the refrigerant vapor and supplies it to the absorber 4 to form a fifth type of absorption type. Heat pump.
  • the humidifier solution is connected to the fourth generator 13 via the third solution pump 15 and the third solution heat exchanger 16, and the fourth generator 13 has a concentrated solution line through the third solution heat exchanger 16 and the first
  • the second generator 2 is connected, and the generator 1 has a refrigerant vapor passage communicating with the condenser 6 to adjust the generator 1 to have a refrigerant vapor passage communicating with the fourth generator 13 and then the fourth generator 13 has a refrigerant liquid pipeline.
  • the heat exchanger 17, the third generator 3 and the second throttle valve 14 are in communication with the evaporator 7, and the fourth generator 13 has a refrigerant vapor passage communicating with the condenser 6, and the heat exchanger 17 has a heated medium.
  • the piping is connected to the outside.
  • the refrigerant vapor generated by the generator 1 is supplied to the fourth generator 13 as a driving heat medium, and a part of the dilute solution of the second absorber 5 is introduced through the third solution pump 15 and the third solution heat exchanger 16
  • the fourth generator 13 the refrigerant vapor flows through the fourth generator 13, the solution heated therein releases the refrigerant vapor and is supplied to the condenser 6, and the concentrated solution of the fourth generator 13 passes through the third solution heat exchanger 16 Entering the second generator 2; the refrigerant vapor flowing through the fourth generator 13 is released into the refrigerant liquid, and then sequentially flows through the heat exchanger 17 and the third generator 3 and gradually releases the heat to cool down, and the cooled refrigerant liquid
  • the second throttle valve 14 is throttled into the evaporator 7 to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump shown in Figure 3 is implemented as follows:
  • the refrigerant vapor generated by the generator 1 is supplied to the fourth generator 13 to drive the heat medium, and the diluted solution of the second absorber 5 is passed through the solution pump 9, the second solution heat exchanger 12 and the third solution.
  • the heat exchanger 16 enters the generator 1, and the concentrated solution of the generator 1 enters the fourth generator 13 via the third solution heat exchanger 16, and the refrigerant vapor flows through the fourth generator 13, and the solution into which it is heated releases the refrigerant.
  • the steam is supplied to the condenser 6, and the concentrated solution of the fourth generator 13 enters the second generator 2 via the second solution heat exchanger 12; the refrigerant vapor flowing through the fourth generator 13 is discharged into the refrigerant liquid, followed by The heat exchanger 17 and the third generator 3 are passed through and gradually cooled and cooled.
  • the cooled refrigerant liquid is throttled into the evaporator 7 through the second throttle valve 14 to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump shown in Figure 4 is implemented as follows:
  • the fourth generator 13 is connected, and the fourth generator 13 has a concentrated solution line connected to the generator 1 via the third solution pump 15 and the third solution heat exchanger 16, and the generator 1 has a concentrated solution line through the second
  • the solution heat exchanger 12 is connected to the second generator 2 to be adjusted so that the generator 1 has a concentrated solution line connected to the second generator 2 via the third solution heat exchanger 16 and the second solution heat exchanger 12, and the generator 1 is
  • the refrigerant vapor passage is connected to the condenser 6 to be adjusted so that the generator 1 has a refrigerant vapor passage
  • the refrigerant vapor generated by the generator 1 is supplied to the fourth generator 13 to drive the heat medium, and the diluted solution of the second absorber 5 enters the fourth occurrence through the solution pump 9 and the second solution heat exchanger 12.
  • the refrigerant vapor flows through the fourth generator 13, and the solution heated therein releases the refrigerant vapor and is supplied to the condenser 6.
  • the concentrated solution of the fourth generator 13 passes through the third solution pump 15 and the third solution heat.
  • the exchanger 16 enters the generator 1, and the concentrated solution of the generator 1 enters the second generator 2 via the third solution heat exchanger 16 and the second solution heat exchanger 12; the refrigerant vapor flowing through the fourth generator 13 releases heat After the refrigerant liquid flows through the heat exchanger 17 and the third generator 3 in sequence, and gradually releases heat and cools, the cooled refrigerant liquid is throttled into the evaporator 7 through the second throttle valve 14 to form a fifth type of absorption type. Heat pump.
  • the fifth type of absorption heat pump shown in Figure 5 is implemented as follows:
  • a fifth generator, a third throttle valve, a fourth solution pump, a fourth solution heat exchanger and a second heat exchanger are added.
  • the second absorber 5 is provided with a dilute solution line connected to the fifth generator 18 via the fourth solution pump 20 and the fourth solution heat exchanger 21, and the fifth generator 18 has a concentrated solution line through the fourth solution heat exchanger 21
  • the fifth generator 18 also has a refrigerant vapor passage communicating with the condenser 6, which will
  • the fourth generator 13 has a refrigerant vapor passage communicating with the condenser 6 to be adjusted so that the fourth generator 13 has a refrigerant vapor passage communicating with the fifth generator 18, and then the fifth generator 18 has a refrigerant liquid pipeline through the second
  • the heat exchanger 22, the third generator 3 and the third throttle valve 19 are in communication with the evaporator 7, and the fourth generator 13 has a refrigerant liquid line through the heat exchanger 17, the third generator 3 and the
  • the refrigerant vapor and the refrigerant liquid generated by the fourth generator 13 are supplied to the fifth generator 18 to drive the heat medium, and the dilute solution of the second absorber 5 is passed through the fourth solution pump 20 and the fourth
  • the solution heat exchanger 21 enters the fifth generator 18, and the refrigerant vapor and the refrigerant liquid flow through the fifth generator 18, and the solution heated therein releases the refrigerant vapor and is supplied to the condenser 6, and the fifth generator 18
  • the concentrated solution enters the second generator 2 through the fourth solution heat exchanger 21; the refrigerant vapor flowing through the fifth generator 18 is released into the refrigerant liquid, and then flows through the second heat exchanger 22 and the third generator 3 in sequence.
  • the third throttle valve 19 is throttled into the evaporator 7, and the coolant liquid of the fourth generator 13 sequentially flows through the fifth generator 18, the heat exchanger 17, the third generator 3, and the second.
  • the throttle valve 14 enters the evaporator 7 to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump shown in Figure 6 is implemented as follows:
  • the dilute solution line is connected to the generator 1 via the solution pump 9, the second solution heat exchanger 12 and the third solution heat exchanger 16 to be adjusted to a second absorber 5 having a dilute solution line through the solution pump 9, the fourth solution
  • the heat exchanger 21, the second solution heat exchanger 12 and the third solution heat exchanger 16 are in communication with the generator 1, and the fourth generator 13 has a concentrated solution line through the second solution heat exchanger 12 and the second generator 2, the communication is adjusted so that the fourth generator 13 has a concentrated solution line connected to the fifth generator 18 via the second solution heat exchanger 12, and the fifth generator 18 has a concentrated solution line through the fourth solution heat exchanger 21 and
  • the second generator 2 is in communication, the fifth generator 18 has a refrigerant vapor passage communicating with the condenser 6, and the fourth generator 13 has
  • the fifth generator 18 After the steam passage is in communication with the fifth generator 18, the fifth generator 18 has a refrigerant liquid line through the second heat exchanger 22,
  • the generator 3 and the third throttle valve 19 are in communication with the evaporator 7, and the fourth generator 13 has a refrigerant liquid line through the heat exchanger 17, the third generator 3, and the second throttle valve 14 and the evaporator 7.
  • the communication is adjusted so that the fourth generator 13 has a refrigerant liquid line connected to the evaporator 7 via the fifth generator 18, the heat exchanger 17, the third generator 3, and the second throttle valve 14, and the second heat exchanger 22
  • the refrigerant vapor and the refrigerant liquid generated by the fourth generator 13 are supplied to the fifth generator 18 to drive the heat medium, and the dilute solution of the second absorber 5 is exchanged by the solution pump 9 and the fourth solution.
  • the second solution heat exchanger 12 and the third solution heat exchanger 16 enter the generator 1, and the concentrated solution of the generator 1 enters the fourth generator 13 via the third solution heat exchanger 16, and the fourth generator 13
  • the concentrated solution enters the fifth generator 18 via the second solution heat exchanger 12, and the refrigerant vapor and the refrigerant liquid flow through the fifth generator 18, and the solution heated into the solution releases the refrigerant vapor and supplies it to the condenser 6,
  • the concentrated solution of the five generators 18 enters the second generator 2 through the fourth solution heat exchanger 21; the refrigerant vapor flowing through the fifth generator 18 is discharged into the refrigerant liquid, and then flows through the second heat exchanger 22 and After the third generator 3 is released from the heat, the third throttle valve 19 is throttled into the e
  • the fifth type of absorption heat pump shown in Figure 7 is implemented as follows:
  • the absorber 5 has a dilute solution line connected to the fifth generator 18 via the solution pump 9 and the second solution heat exchanger 12, and the fifth generator 18 has a concentrated solution line through the fourth solution pump 20 and the fourth solution heat.
  • the exchanger 21 is in communication with the fourth generator 13, and the concentrated solution line of the generator 1 is connected to the second generator 2 via the third solution heat exchanger 16 and the second solution heat exchanger 12 to adjust the generator 1 to be rich.
  • the solution line is in communication with the second generator 2 via the third solution heat exchanger 16, the fourth solution heat exchanger 21 and the second solution heat exchanger 12, and the fifth generator 18 also has a refrigerant vapor passage and a condenser 6 Connected, the fourth generator 13 has a refrigerant vapor passage communicating with the condenser 6 to be adjusted to a fourth generator 13 having a refrigerant vapor passage communicating with the fifth generator 18, and then the fifth generator 18 has a refrigerant liquid line
  • the fourth generator is connected to the evaporator 7 via the second heat exchanger 22, the third generator 3 and the third throttle valve 19 13 having a refrigerant liquid pipeline connected to the evaporator 7 via the heat exchanger 17, the third generator 3 and the second throttle valve 14 to be adjusted to a fourth generator 13 having
  • the refrigerant vapor and the refrigerant liquid generated by the fourth generator 13 are supplied to the fifth generator 18 to drive the heat medium, and the dilute solution of the second absorber 5 is exchanged by the solution pump 9 and the second solution.
  • the device 12 enters the fifth generator 18, and the refrigerant vapor and the refrigerant liquid flow through the fifth generator 18, and the solution heated therein releases the refrigerant vapor and is supplied to the condenser 6, and the concentrated solution of the fifth generator 18 passes through
  • the fourth solution pump 20 and the fourth solution heat exchanger 21 enter the fourth generator 13, and the concentrated solution of the fourth generator 13 enters the generator 1 via the third solution pump 15 and the third solution heat exchanger 16, the generator 1
  • the concentrated solution enters the second generator 2 through the third solution heat exchanger 16, the fourth solution heat exchanger 21 and the second solution heat exchanger 12; the refrigerant vapor flowing through the fifth generator 18 is released into a refrigerant After the liquid flows through the second heat exchanger 22 and the third generator 3 in sequence, the heat is
  • the fifth type of absorption heat pump shown in Figure 8 is implemented as follows:
  • the absorber 4 has a dilute solution line through the solution heat exchanger 11 and
  • the second absorber 5 is connected, the second absorber 5 and the dilute solution line are connected to the third absorber 23 via the solution pump 9 and the second solution heat exchanger 12, and the third absorber 23 has a dilute solution line.
  • the three solution pump 15 and the third solution heat exchanger 16 are in communication with the generator 1, and the generator 1 and the concentrated solution line are in communication with the fourth generator 13 via the third solution heat exchanger 16, and the fourth generator 13 has The concentrated solution line is connected to the second generator 2 via the second solution heat exchanger 12, the second generator 2 has a concentrated solution line connected to the third generator 3, and the third generator 3 has a concentrated solution line.
  • the second solution pump 10 and the solution heat exchanger 11 are in communication with the absorber 4, and the generator 1 also has a refrigerant vapor passage and condensation.
  • the condenser 6 and the refrigerant liquid pipeline are in communication with the third generator 3, and then the third generator 3 has a refrigerant liquid pipeline connected to the evaporator 7 via the throttle valve 8, the second generator 2 and
  • the third generator 3 further has a refrigerant vapor passage communicating with the second absorber 5, and the fourth generator 13 and the refrigerant vapor passage are in communication with the third absorber 23, and the evaporator 7 also has a refrigerant vapor passage and absorption.
  • the generator 4 is connected, and the generator 1 and the fourth generator 13 further have driving heat medium pipes respectively communicating with the outside, and the absorber 4, the condenser 6 and the third absorber 23 are respectively connected to the outside by the heated medium pipe.
  • the second generator 2 and the evaporator 7 respectively have a waste heat medium line communicating with the outside, and the second absorber 5 also has a cooling medium line and Externally connected.
  • the dilute solution of the absorber 4 enters the second absorber 5 through the solution heat exchanger 11, absorbs the refrigerant vapor and radiates heat to the cooling medium, and the dilute solution of the second absorber 5 passes through the solution pump 9 and the
  • the two solution heat exchanger 12 enters the third absorber 23, absorbs the refrigerant vapor and radiates heat to the heated medium, and the dilute solution of the third absorber 23 enters the generator through the third solution pump 15 and the third solution heat exchanger 16. 1.
  • the driving heat medium flows through the generator 1, and the solution heated therein releases the refrigerant vapor and is supplied to the condenser 6.
  • the concentrated solution of the generator 1 enters the fourth generator 13 through the third solution heat exchanger 16 to drive
  • the heat medium flows through the fourth generator 13, the solution heated therein releases the refrigerant vapor and is supplied to the third absorber 23, and the concentrated solution of the fourth generator 13 enters the second generator via the second solution heat exchanger 12.
  • the residual heat medium flows through the second generator 2
  • the solution heated into it releases the refrigerant vapor and is supplied to the second absorber 5
  • the concentrated solution of the second generator 2 enters the third generator 3, and the heat is released and released.
  • the vapor is supplied to the second absorber 5, and the third generator 3 is concentrated.
  • the second solution pump 10 and the solution heat exchanger 11 enter the absorber 4, absorb the refrigerant vapor and release the heat to the heated medium; the refrigerant vapor of the condenser 6 radiates heat to the heated medium to form a refrigerant liquid, and the refrigerant liquid
  • the third generator 3 is cooled and cooled, and the coolant liquid after cooling is throttled into the evaporator 7 through the throttle valve 8, and absorbed into the refrigerant vapor and supplied to the absorber 4 to form a fifth type absorption heat pump.
  • the fifth type of absorption heat pump shown in Figure 9 is implemented as follows:
  • the auxiliary solution 23 is connected to the fifth generator 18 via the fourth solution pump 20 and the fourth solution heat exchanger 21, and the fifth generator 18 has a concentrated solution line through the fourth solution heat exchanger 21 and
  • the four generators 13 are connected, and the generator 1 has a refrigerant vapor passage communicating with the condenser 6 to adjust the generator 1 to have a refrigerant vapor passage communicating with the fifth generator 18, and then the fifth generator 18 has a refrigerant liquid line.
  • the heat exchanger 17, the third generator 3 and the second throttle valve 14 are in communication with the evaporator 7, and the fifth generator 18 has a refrigerant vapor passage communicating with the condenser 6, and the heat exchanger 17 has a heated medium.
  • the piping is connected to the outside.
  • the refrigerant vapor generated by the generator 1 is supplied to the fifth generator 18 as a driving heat medium, and a part of the diluted solution of the third absorber 23 is introduced through the fourth solution pump 20 and the fourth solution heat exchanger 21
  • the refrigerant vapor flowing through the fifth generator 18 is exothermic into a refrigerant liquid, and then sequentially flows through the heat exchanger 17 and the third generator 3 and gradually releases the heat to cool down, and the cooled refrigerant liquid
  • the second throttle valve 14 is throttled into the evaporator 7 to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump shown in Figure 10 is implemented as follows:
  • the solution line is connected to the generator 1 via the third solution pump 15 and the third solution heat exchanger 16 to adjust the third absorber 23 to have a dilute solution line through the third solution pump 15, the third solution heat exchanger 16 and the
  • the four-solution heat exchanger 21 is in communication with the generator 1, and the concentrated solution line of the generator 1 is connected to the fourth generator 13 via the third solution heat exchanger 16 to be adjusted to a generator 1 having a concentrated solution line through the fourth solution.
  • the heat exchanger 21 is in communication with the fifth generator 18, and the fifth generator 18 is further connected to the fourth generator 13 via the third solution heat exchanger 16 via the third solution heat exchanger 16 to provide refrigerant vapor passage and condensation.
  • the device 6 is connected to adjust the generator 1 to have a refrigerant vapor passage communicating with the fifth generator 18, and then the fifth generator 18 has a refrigerant liquid line through the heat exchanger 17, the third generator 3 and the second throttle valve.
  • 14 is in communication with the evaporator 7, and the fifth generator 18 has a refrigerant vapor passage communicating with the condenser 6, the fifth occurrence
  • the heater 18 also has a drive heat medium line in communication with the outside, and the heat exchanger 17 and the heated medium line communicate with the outside.
  • the refrigerant vapor generated by the driving heat medium and the generator 1 supplies a driving heat load to the fifth generator 18, and the diluted solution of the third absorber 23 passes through the third solution pump 15 and the third solution heat exchanger.
  • the 16 and fourth solution heat exchangers 21 enter the generator 1, and the concentrated solution of the generator 1 enters the fifth generator 18 via the fourth solution heat exchanger 21, and drives the heat medium and the refrigerant vapor to flow through the fifth generator 18,
  • the solution heated therein releases the refrigerant vapor and is supplied to the condenser 6, and the concentrated solution of the fifth generator 18 enters the fourth generator 13 via the third solution heat exchanger 16; the refrigerant flowing through the fifth generator 18.
  • the fifth type of absorption heat pump shown in Figure 11 is implemented as follows:
  • the absorber 23 has a dilute solution line connected to the generator 1 via the third solution pump 15 and the third solution heat exchanger 16 to adjust the third absorber 23 to have a dilute solution line through the third solution pump 15 and the third solution heat
  • the exchanger 16 is in communication with the fifth generator 18, and the fifth generator 18 has a concentrated solution line connected to the generator 1 via the fourth solution pump 20 and the fourth solution heat exchanger 21, and the generator 1 has a concentrated solution tube.
  • the third solution heat exchanger 16 communicates with the fourth generator 13 to adjust the generator 1 to have a concentrated solution line connected to the fourth generator 13 via the fourth solution heat exchanger 21 and the third solution heat exchanger 16.
  • the generator 1 has a refrigerant vapor passage communicating with the condenser 6 to adjust the generator 1 to have a refrigerant vapor passage communicating with the fifth generator 18, and then the fifth generator 18 has a refrigerant liquid pipeline passing through the heat exchanger 17,
  • the third generator 3 and the second throttle valve 14 are in communication with the evaporator 7, and the fifth generator 18 also has a refrigerant vapor passage and condensation Communication 6, heat exchanger 17 is also in communication with an external heating medium line.
  • the refrigerant vapor generated by the generator 1 is supplied to the fifth generator 18 for driving the heat medium, and the diluted solution of the third absorber 23 is passed through the third solution pump 15 and the third solution heat exchanger 16 to enter the first a five generator 18, the refrigerant vapor flows through the fifth generator 18, the solution heated therein releases the refrigerant vapor and is supplied to the condenser 6, and the concentrated solution of the fifth generator 18 passes through the fourth solution pump 20 and the fourth
  • the solution heat exchanger 21 enters the generator 1, and the concentrated solution of the generator 1 enters the fourth generator 13 through the fourth solution heat exchanger 21 and the third solution heat exchanger 16; the refrigerant vapor flowing through the fifth generator 18 After exothermic into a cold liquid, it sequentially flows through the heat exchanger 17 and the third generator 3 and gradually releases heat and cools, and the cooled refrigerant liquid is throttled into the evaporator 7 through the second throttle valve 14 to form a fifth type.
  • Absorption heat pump After exothermic into a cold liquid,
  • the fifth type of absorption heat pump shown in Figure 12 is implemented as follows:
  • the third generator 3 has a concentrated solution line connected to the newly added generator A via the solution heat exchanger 11 , and the new generator A has a concentrated solution line through the second solution pump 10 and the new solution heat exchanger D.
  • the newly added generator A and the refrigerant vapor passage are connected with the newly added absorber B, and the third generator 3 has a refrigerant liquid pipeline connected to the evaporator 7 through the throttle valve 8 to be adjusted to the first
  • the three generators 3 have a refrigerant liquid line connected with the newly added generator A, and then add a generator A and then a refrigerant liquid line through the throttle valve 8 and the evaporator 7 Pass, new absorber coolant lines B also communicates with the outside.
  • the dilute solution of the absorber 4 enters the newly added absorber B through the newly added solution heat exchanger D, and absorbs the refrigerant vapor.
  • the diluted solution of the new absorber B is added to the second absorber 5 through the new solution pump C and the solution heat exchanger 11;
  • the concentrated solution of the third generator 3 enters the new solution through the solution heat exchanger 11 Increasing generator A, absorbing heat release refrigerant vapor and supplying to newly added absorber B, adding concentrated solution of generator A to the absorber 4 through the second solution pump 10 and the new solution heat exchanger D; the condenser 6
  • the refrigerant liquid flows through the third generator 3 and the newly added generator A in sequence and gradually releases heat to cool down.
  • the coolant liquid after the cooling is throttled into the evaporator 7 through the throttle valve 8 to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump shown in Figure 13 is implemented as follows:
  • the passage solution heat exchanger 11 is connected to the second absorber 5 to be adjusted so that the absorber 4 has a dilute solution line connected to the newly added absorber B via the newly added solution heat exchanger D, and the new absorber B has a dilute solution tube.
  • the new solution pump C and the solution heat exchanger 11 are connected to the second absorber 5, and the concentrated solution line of the third generator 3 is connected to the absorber 4 through the second solution pump 10 and the solution heat exchanger 11.
  • the third generator 3 has a concentrated solution line connected to the newly added generator A via the solution heat exchanger 11 , and the new generator A has a concentrated solution line through the second solution pump 10 and the new solution heat exchanger D.
  • the newly added generator A and the refrigerant vapor passage are connected with the newly added absorber B, and the third generator 3 has a refrigerant liquid pipeline connected to the evaporator 7 through the throttle valve 8 to be adjusted to the first
  • the three generators 3 have a refrigerant liquid line connected with the newly added generator A, and then add a generator A and then a refrigerant liquid line through the throttle valve 8 and the evaporator 7 Passing, the third generator 3 has a refrigerant liquid pipeline connected to the evaporator 7 via the second throttle valve 14 to be adjusted to be a third generator 3, and the refrigerant liquid pipeline is newly connected to the new generator A.
  • the A further refrigerant liquid line is connected to the evaporator 7 via the second throttle valve 14, and the new absorber B
  • the dilute solution of the absorber 4 enters the new absorber B through the newly added solution heat exchanger D, absorbs the refrigerant vapor and releases the heat to the cooling medium, and adds the diluted solution of the absorber B through the newly added solution.
  • the pump C and the solution heat exchanger 11 enter the second absorber 5; the concentrated solution of the third generator 3 enters the new generator A, the endothermic release refrigerant vapor, and supplies the new absorber B through the solution heat exchanger 11.
  • the new concentrated solution of the generator A is introduced into the absorber 4 through the second solution pump 10 and the newly added solution heat exchanger D; the refrigerant liquid of the condenser 6 sequentially flows through the third generator 3 and the newly added generator A.
  • the heat is gradually cooled down, and the coolant liquid after the cooling is throttled into the evaporator 7 through the throttle valve 8; the coolant liquid generated by the fourth generator 13 sequentially flows through the heat exchanger 17, the third generator 3, and newly occurs.
  • the device A gradually releases heat and cools down, and the coolant liquid after the cooling is throttled into the evaporator 7 through the second throttle valve 14 to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump shown in Figure 14 is implemented as follows:
  • the passage solution heat exchanger 11 is connected to the second absorber 5 to be adjusted so that the absorber 4 has a dilute solution line connected to the newly added absorber B via the newly added solution heat exchanger D, and the new absorber B has a dilute solution tube.
  • the new solution pump C and the solution heat exchanger 11 are connected to the second absorber 5, and the concentrated solution line of the third generator 3 is connected to the absorber 4 through the second solution pump 10 and the solution heat exchanger 11.
  • the third generator 3 has a concentrated solution line connected to the newly added generator A via the solution heat exchanger 11 , and the new generator A has a concentrated solution line through the second solution pump 10 and the new solution heat exchanger D.
  • the newly added generator A and the refrigerant vapor passage are connected with the newly added absorber B, and the third generator 3 has a refrigerant liquid pipeline connected to the evaporator 7 through the throttle valve 8 to be adjusted to the first
  • the three generators 3 have a refrigerant liquid line connected with the newly added generator A, and then add a generator A and then a refrigerant liquid line through the throttle valve 8 and the evaporator 7 Passing, the third generator 3 has a refrigerant liquid pipeline connected to the evaporator 7 via the second throttle valve 14 to be adjusted to be a third generator 3, and the refrigerant liquid pipeline is newly connected to the new generator A.
  • Unit A has a refrigerant liquid line through the second throttle valve 14 is connected to the evaporator 7, and the third generator 3 has a refrigerant liquid pipeline connected to the evaporator 7 through the third throttle valve 19 to be adjusted to a third generator 3 having a refrigerant liquid pipeline and a new generator A.
  • the generator A is newly added, and the refrigerant liquid pipeline is connected to the evaporator 7 via the third throttle valve 19, and the new absorber B and the cooling medium pipeline are connected to the outside.
  • the dilute solution of the absorber 4 enters the new absorber B through the newly added solution heat exchanger D, absorbs the refrigerant vapor and releases the heat to the cooling medium, and adds the diluted solution of the absorber B through the newly added solution.
  • the pump C and the solution heat exchanger 11 enter the second absorber 5; the concentrated solution of the third generator 3 enters the new generator A, the endothermic release refrigerant vapor, and supplies the new absorber B through the solution heat exchanger 11.
  • the new concentrated solution of the generator A is introduced into the absorber 4 through the second solution pump 10 and the newly added solution heat exchanger D; the refrigerant liquid of the condenser 6 sequentially flows through the third generator 3 and the newly added generator A.
  • the coolant liquid after cooling is throttled into the evaporator 7 through the throttle valve 8; the coolant liquid generated by the fourth generator 13 sequentially flows through the fifth generator 18, the heat exchanger 17, and the third generation
  • the generator 3 and the new generator A are gradually heated and cooled, and the coolant liquid after the cooling is throttled into the evaporator 7 through the second throttle valve 14; the refrigerant liquid generated by the fifth generator 18 sequentially flows through the second heat.
  • the exchanger 22, the third generator 3 and the newly added generator A are gradually heated and cooled, and the coolant liquid after the cooling is passed through the third throttle valve 19 Into the evaporator 7, form a fifth type absorption heat pump.
  • the fifth type of absorption heat pump shown in Figure 15 is implemented as follows:
  • the third generator 3 has a concentrated solution line connected to the newly added generator A via the solution heat exchanger 11 , and the new generator A has a concentrated solution line through the second solution pump 10 and the new solution heat exchanger D.
  • the new generator A and the refrigerant vapor channel are connected with the newly added absorber B, and the new generator A and the waste heat medium pipeline are connected to the outside, and the new absorber B and the cooling medium tube are added.
  • the road is connected to the outside.
  • the dilute solution of the absorber 4 enters the new absorber B through the newly added solution heat exchanger D, absorbs the refrigerant vapor and releases the heat to the cooling medium, and adds the diluted solution of the absorber B through the newly added solution.
  • the pump C and the solution heat exchanger 11 enter the second absorber 5; the concentrated solution of the third generator 3 enters the newly added generator A through the solution heat exchanger 11, and the residual heat medium flows through the newly added generator A, and is heated into the inside.
  • the solution releases the refrigerant vapor and supplies it to the new absorber B.
  • the concentrated solution of the new generator A is introduced into the absorber 4 via the second solution pump 10 and the new solution heat exchanger D to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump shown in Figure 16 is implemented as follows:
  • the passage is connected to the absorber 4 to be adjusted so that the evaporator 7 has a refrigerant vapor passage communicating with the newly added absorber B, and the newly added absorber B and the dilute solution pipeline are connected to the new solution pump C and the new solution heat exchanger D.
  • the new generator A is connected, the new generator A and the concentrated solution pipeline are connected to the newly added absorber B via the new solution heat exchanger D, and the new generator A and the refrigerant vapor passage are connected to the absorber 4.
  • the new generator A also has a driving heat medium pipeline connected to the outside, and the newly added absorber B and the heated medium pipeline communicate with the outside.
  • the refrigerant vapor generated by the evaporator 7 enters the newly added absorber B, and the diluted solution of the newly added absorber B enters the newly added generator A through the newly added solution pump C and the newly added solution heat exchanger D,
  • the driving heat medium flows through the newly added generator A, and the solution heated into the solution releases the refrigerant vapor and supplies it to the absorber 4, and the concentrated solution of the new generator A is heated by the new solution.
  • the device D enters the new absorber B, absorbs the refrigerant vapor and radiates heat to the heated medium to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump shown in Figure 17 is implemented as follows:
  • the passage is connected to the condenser 6 to adjust the generator 1 to have a refrigerant vapor passage communicating with the newly added absorber B, and the new absorber B and the dilute solution pipeline are added by the new solution pump C and the new solution heat exchanger D.
  • the new generator A is connected, the new generator A and the concentrated solution pipeline are connected to the newly added absorber B via the new solution heat exchanger D, and the new generator A and the refrigerant vapor passage are connected to the condenser 6.
  • the new generator A also has a driving heat medium pipeline connected to the outside, and the newly added absorber B and the heated medium pipeline communicate with the outside.
  • the refrigerant vapor generated by the generator 1 enters the absorption absorber B, and the diluted solution of the new absorber B is added to the new generator A through the new solution pump C and the new solution heat exchanger D, and is driven.
  • the heat medium flows through the newly added generator A, and the solution heated into the solution releases the refrigerant vapor and supplies it to the condenser 6.
  • the newly added concentrated solution of the generator A enters the newly added absorber B through the newly added solution heat exchanger D,
  • the refrigerant vapor is absorbed and exothermic to the heated medium to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump shown in Figure 18 is implemented as follows:
  • the third generator 3 adds a waste heat medium pipeline to communicate with the outside; the refrigerant liquid and the waste heat medium jointly provide a driving heat load to the third generator 3 to form a fifth type of absorption. Heat pump.
  • the fifth type of absorption heat pump shown in Figure 19 is implemented as follows:
  • the newly added generator A and the concentrated solution pipeline are connected to the newly added absorber B via the newly added solution heat exchanger D, and the newly added generator A and the refrigerant vapor passage are connected with the second absorber 5, and newly added occurs.
  • the A and the residual heat medium pipeline communicate with the outside, and the newly added absorber B and the cooling medium pipeline communicate with the outside.
  • the refrigerant vapor generated by the second generator 2 and the third generator 3 enters the absorber B, and the diluted solution of the absorber B is newly added to the solution pump C and the new solution heat exchanger D.
  • the waste heat medium flows through the new generator A, and the solution heated into the solution releases the refrigerant vapor and supplies it to the second absorber 5, and the concentrated solution of the new generator A is heated by the new solution.
  • the device D enters the new absorber B, absorbs the refrigerant vapor and radiates heat to the cooling medium to form a fifth type of absorption heat pump.
  • the fifth type of absorption heat pump shown in Figure 20 is implemented as follows:
  • the second generator 2 has a residual heat medium pipeline connected to the outside to be adjusted so that the third generator 3 has a residual heat medium pipeline communicating with the outside, and the condenser 6 has a refrigerant.
  • the third generator 3 has a refrigerant liquid pipeline connected to the evaporator 7 via the throttle valve 8 to be adjusted to a condenser 6 having a refrigerant liquid pipeline and a second generator 2
  • the second generator 2 has a refrigerant liquid pipeline connected to the evaporator 7 via the throttle valve 8; the refrigerant liquid supplies a driving heat load to the second generator 2, and the residual heat medium supplies driving heat to the third generator 3. Load, forming a fifth type of absorption heat pump.

Abstract

一种第五类吸收式热泵。吸收器（4）经溶液热交换器（11）连通第二吸收器（5），第二吸收器（5）经溶液泵（9）和第二溶液热交换器（12）连通发生器（1），发生器（1）经第二溶液热交换器（12）连通第二发生器（2），第二发生器（2）连通第三发生器（3），第三发生器（3）经第二溶液泵（10）和溶液热交换器（11）连通吸收器（4），发生器（1）有冷剂蒸汽通道连通冷凝器（6），第二发生器（2）和第三发生器（3）有冷剂蒸汽通道连通第二吸收器（5），冷凝器（6）有冷剂液管路经第三发生器（3）和节流阀（8）连通蒸发器（7），蒸发器（7）有冷剂蒸汽通道连通吸收器（4），发生器（1）有驱动热介质管路、吸收器（4）和冷凝器（6）有被加热介质管路、第二吸收器（5）有冷却介质管路分别与外部连通，蒸发器（7）、第二发生器（2）和第三发生器（3）有余热介质管路与外部连通，形成第五类吸收式热泵。

Description

第五类吸收式热泵 技术领域：
本发明属于吸收式热泵和余热利用技术领域。
背景技术：
在吸收式热泵技术领域，已出现三大类吸收式热泵，分别是以高温驱动热介质与被加热介质之间温差为驱动温差的第一类吸收式热泵，以余热介质与冷环境(冷却介质)之间温差为驱动温差的第二类吸收式热泵，以及同时以前述两种温差为驱动温差的第三类吸收式热泵。根据已有的认识或观点，这三种类型的吸收式热泵中，将高温驱动热释放到冷环境(冷却介质)中是不合理的，至今尚未有技术人员提出相关的吸收式热泵流程。
在提供高温热负荷的第三类吸收式热泵中，本领域技术人员遇到了技术难题：以TFE-TDE高温溶液为代表的吸收式热泵流程中，冷剂蒸汽潜热较小，高温发生器释放冷剂蒸汽并在冷凝器中放热于被加热介质之后形成的冷剂液温度高、流量大，显热较大；这导致吸收式热泵的性能指数很低，对高品位热能的利用不充分，影响对余热的有效利用，使得第三类吸收式热泵在高温供热领域的应用受到影响。
发明人认识到上述问题，并开发出了解决上述问题的技术新方案，开发出包含余热介质与冷环境(冷却介质)之间温差为驱动温差，加上以高温热负荷两种不同温降为驱动温差的第五类吸收式热泵；本发明提供利用第三发生器和第二吸收器实现冷剂液温差利用为基础的系列第五类吸收式热泵。
发明内容：
本发明主要目的是要提供第五类吸收式热泵，具体发明内容分项阐述如下：
1.第五类吸收式热泵，主要由发生器、第二发生器、第三发生器、吸收器、第二吸收器、冷凝器、蒸发器、节流阀、溶液泵、第二溶液泵、溶液热交换器和第二溶液热交换器所组成；吸收器有稀溶液管路经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溶液泵和第二溶液热交换器与发生器连通，发生器还有浓溶液管路经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溶液热交换器与吸收器连通，发生器还有冷剂蒸汽通道与冷凝器连通，冷凝器还有冷剂液管路与第三发生器连通之后第三发生器再有冷剂液管路经节流阀与蒸发器连通，第二发生器和第三发生器还分别有冷剂蒸汽通道与第二吸收器连通，蒸发器还有冷剂蒸汽通道与吸收器连通，发生器还有驱动热介质管路与外部连通，吸收器和冷凝器还分别有被加热介质管路与外部连通，第二发生器和蒸发器还分别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，形成第五类吸收式热泵。
2.第五类吸收式热泵，是在第1项所述的第五类吸收式热泵中，取消节流阀，将第三发生器有冷剂液管路经节流阀与蒸发器连通调整为第三发生器有冷剂液管路与蒸发器连通，形成第五类吸收式热泵。
3.第五类吸收式热泵，是在第1项所述的第五类吸收式热泵中，增加第四发生器、第二节流阀、第三溶液泵、第三溶液热交换器和热交换器，第二吸收器增设稀溶液管路经第 三溶液泵和第三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热交换器与第二发生器连通，将发生器有冷剂蒸汽通道与冷凝器连通调整为发生器有冷剂蒸汽通道与第四发生器连通之后第四发生器再有冷剂液管路经热交换器、第三发生器和第二节流阀与蒸发器连通，第四发生器还有冷剂蒸汽通道与冷凝器连通，热交换器还有被加热介质管路与外部连通，形成第五类吸收式热泵。
4.第五类吸收式热泵，是在第1项所述的第五类吸收式热泵中，增加第四发生器、第二节流阀、第三溶液热交换器和热交换器，将第二吸收器有稀溶液管路经溶液泵和第二溶液热交换器与发生器连通调整为第二吸收器有稀溶液管路经溶液泵、第二溶液热交换器和第三溶液热交换器与发生器连通，将发生器有浓溶液管路经第二溶液热交换器与第二发生器连通调整为发生器有浓溶液管路经第三溶液热交换器与第四发生器连通，第四发生器再有浓溶液管路经第二溶液热交换器与第二发生器连通，将发生器有冷剂蒸汽通道与冷凝器连通调整为发生器有冷剂蒸汽通道与第四发生器连通之后第四发生器再有冷剂液管路经热交换器、第三发生器和第二节流阀与蒸发器连通，第四发生器还有冷剂蒸汽通道与冷凝器连通，热交换器还有被加热介质管路与外部连通，形成第五类吸收式热泵。
5.第五类吸收式热泵，是在第1项所述的第五类吸收式热泵中，增加第四发生器、第二节流阀、第三溶液泵、第三溶液热交换器和热交换器，将第二吸收器有稀溶液管路经溶液泵和第二溶液热交换器与发生器连通调整为第二吸收器有稀溶液管路经溶液泵和第二溶液热交换器与第四发生器连通，第四发生器再有浓溶液管路经第三溶液泵和第三溶液热交换器与发生器连通，将发生器有浓溶液管路经第二溶液热交换器与第二发生器连通调整为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第二发生器连通，将发生器有冷剂蒸汽通道与冷凝器连通调整为发生器有冷剂蒸汽通道与第四发生器连通之后第四发生器再有冷剂液管路经热交换器、第三发生器和第二节流阀与蒸发器连通，第四发生器还有冷剂蒸汽通道与冷凝器连通，热交换器还有被加热介质管路与外部连通，形成第五类吸收式热泵。
6.第五类吸收式热泵，是在第3-5项所述的任一第五类吸收式热泵中，取消节流阀和第二节流阀，将第三发生器有冷剂液管路经节流阀与蒸发器连通调整为第三发生器有冷剂液管路与蒸发器连通，将第三发生器有冷剂液管路经第二节流阀与蒸发器连通调整为第三发生器有冷剂液管路与蒸发器连通，形成第五类吸收式热泵。
7.第五类吸收式热泵，是在第3项所述的第五类吸收式热泵中，增加第五发生器、第三节流阀，第四溶液泵、第四溶液热交换器和第二热交换器，第二吸收器增设稀溶液管路经第四溶液泵和第四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四溶液热交换器与第二发生器连通，第五发生器还有冷剂蒸汽通道与冷凝器连通，将第四发生器有冷剂蒸汽通道与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之后第五发生器再有冷剂液管路经第二热交换器、第三发生器和第三节流阀与蒸发器连通，将第四发生器有冷剂液管路经热交换器、第三发生器和第二节流阀与蒸发器连通调整为第四发生器有冷剂液管路经第五发生器、热交换器、第三发生器和第二节流阀与蒸发器连通，第二热交换器还有被加热介质管路与外部连通，形成第五类吸收式热泵。
8.第五类吸收式热泵，是在第4项所述的第五类吸收式热泵中，增加第五发生器、第 三节流阀、第四溶液热交换器和第二热交换器，将第二吸收器有稀溶液管路经溶液泵、第二溶液热交换器和第三溶液热交换器与发生器连通调整为第二吸收器有稀溶液管路经溶液泵、第四溶液热交换器、第二溶液热交换器和第三溶液热交换器与发生器连通，将第四发生器有浓溶液管路经第二溶液热交换器与第二发生器连通调整为第四发生器有浓溶液管路经第二溶液热交换器与第五发生器连通，第五发生器再有浓溶液管路经第四溶液热交换器与第二发生器连通，第五发生器还有冷剂蒸汽通道与冷凝器连通，将第四发生器有冷剂蒸汽通道与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之后第五发生器再有冷剂液管路经第二热交换器、第三发生器和第三节流阀与蒸发器连通，将第四发生器有冷剂液管路经热交换器、第三发生器和第二节流阀与蒸发器连通调整为第四发生器有冷剂液管路经第五发生器、热交换器、第三发生器和第二节流阀与蒸发器连通，第二热交换器还有被加热介质管路与外部连通，形成第五类吸收式热泵。
9.第五类吸收式热泵，是在第5项所述的第五类吸收式热泵中，增加第五发生器、第三节流阀，第四溶液泵、第四溶液热交换器和第二热交换器，将第二吸收器有稀溶液管路经溶液泵和第二溶液热交换器与第四发生器连通调整为第二吸收器有稀溶液管路经溶液泵和第二溶液热交换器与第五发生器连通，第五发生器再有浓溶液管路经第四溶液泵和第四溶液热交换器与第四发生器连通，将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第二发生器连通调整为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第二发生器连通，第五发生器还有冷剂蒸汽通道与冷凝器连通，将第四发生器有冷剂蒸汽通道与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之后第五发生器再有冷剂液管路经第二热交换器、第三发生器和第三节流阀与蒸发器连通，将第四发生器有冷剂液管路经热交换器、第三发生器和第二节流阀与蒸发器连通调整为第四发生器有冷剂液管路经第五发生器、热交换器、第三发生器和第二节流阀与蒸发器连通，第二热交换器还有被加热介质管路与外部连通，形成第五类吸收式热泵。
10.第五类吸收式热泵，是在第7-9项所述的任一第五类吸收式热泵中，取消节流阀、第二节流阀和第三节流阀，将第三发生器有冷剂液管路经节流阀与蒸发器连通调整为第三发生器有冷剂液管路与蒸发器连通，将第三发生器有冷剂液管路经第二节流阀与蒸发器连通调整为第三发生器有冷剂液管路与蒸发器连通，将第三发生器有冷剂液管路经第三节流阀与蒸发器连通调整为第三发生器有冷剂液管路与蒸发器连通，形成第五类吸收式热泵。
11.第五类吸收式热泵，主要由发生器、第二发生器、第三发生器、吸收器、第二吸收器、冷凝器、蒸发器、节流阀、溶液泵、第二溶液泵、溶液热交换器、第二溶液热交换器、第四发生器、第三溶液泵、第三溶液热交换器和第三吸收器所组成；吸收器有稀溶液管路经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溶液泵和第二溶液热交换器与第三吸收器连通，第三吸收器还有稀溶液管路经第三溶液泵和第三溶液热交换器与发生器连通，发生器还有浓溶液管路经第三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第二发生器连通，第二发生器还有浓溶液管路与第三发生器连通，第三发生器还有浓溶液管路经第二溶液泵和溶液热交换器与吸收器连通，发生器还有冷剂蒸汽通道与冷凝器连通，冷凝器还有冷剂液管路与第三发生器连通之后第三发生器再有冷剂液管路经节流阀与蒸发器连通，第二发生器和第三发生器还分别有 冷剂蒸汽通道与第二吸收器连通，第四发生器还有冷剂蒸汽通道与第三吸收器连通，蒸发器还有冷剂蒸汽通道与吸收器连通，发生器和第四发生器还分别有驱动热介质管路与外部连通，吸收器、冷凝器和第三吸收器还分别有被加热介质管路与外部连通，第二发生器和蒸发器还分别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，形成第五类吸收式热泵。
12.第五类吸收式热泵，是在第11项所述的第五类吸收式热泵中，取消节流阀，将第三发生器有冷剂液管路经节流阀与蒸发器连通调整为第三发生器有冷剂液管路与蒸发器连通，形成第五类吸收式热泵。
13.第五类吸收式热泵，是在第11项所述的第五类吸收式热泵中，增加第五发生器、第二节流阀、第四溶液泵、第四溶液热交换器和热交换器，第三吸收器增设稀溶液管路经第四溶液泵和第四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四溶液热交换器与第四发生器连通，将发生器有冷剂蒸汽通道与冷凝器连通调整为发生器有冷剂蒸汽通道与第五发生器连通之后第五发生器再有冷剂液管路经热交换器、第三发生器和第二节流阀与蒸发器连通，第五发生器还有冷剂蒸汽通道与冷凝器连通，热交换器还有被加热介质管路与外部连通，形成第五类吸收式热泵。
14.第五类吸收式热泵，是在第11项所述的第五类吸收式热泵中，增加第五发生器、第二节流阀、第四溶液热交换器和热交换器，将第三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发生器连通调整为第三吸收器有稀溶液管路经第三溶液泵、第三溶液热交换器和第四溶液热交换器与发生器连通，将发生器有浓溶液管路经第三溶液热交换器与第四发生器连通调整为发生器有浓溶液管路经第四溶液热交换器与第五发生器连通，第五发生器再有浓溶液管路经第三溶液热交换器与第四发生器连通，将发生器有冷剂蒸汽通道与冷凝器连通调整为发生器有冷剂蒸汽通道与第五发生器连通之后第五发生器再有冷剂液管路经热交换器、第三发生器和第二节流阀与蒸发器连通，第五发生器还有冷剂蒸汽通道与冷凝器连通，热交换器还有被加热介质管路与外部连通，形成第五类吸收式热泵。
15.第五类吸收式热泵，是在第11项所述的第五类吸收式热泵中，增加第五发生器、第二节流阀、第四溶液泵、第四溶液热交换器和热交换器，将第三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发生器连通调整为第三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第五发生器连通，第五发生器再有浓溶液管路经第四溶液泵和第四溶液热交换器与发生器连通，将发生器有浓溶液管路经第三溶液热交换器与第四发生器连通调整为发生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四发生器连通，将发生器有冷剂蒸汽通道与冷凝器连通调整为发生器有冷剂蒸汽通道与第五发生器连通之后第五发生器再有冷剂液管路经热交换器、第三发生器和第二节流阀与蒸发器连通，第五发生器还有冷剂蒸汽通道与冷凝器连通，热交换器还有被加热介质管路与外部连通，形成第五类吸收式热泵。
16.第五类吸收式热泵，是在第13-15项所述的任一第五类吸收式热泵中，第五发生器增设驱动热介质管路与外部连通，形成第五类吸收式热泵。
17.第五类吸收式热泵，是在第13-16项所述的任一第五类吸收式热泵中，取消节流阀和第二节流阀，将第三发生器有冷剂液管路经节流阀与蒸发器连通调整为第三发生器有 冷剂液管路与蒸发器连通，将第三发生器有冷剂液管路经第二节流阀与蒸发器连通调整为第三发生器有冷剂液管路与蒸发器连通，形成第五类吸收式热泵。
18.第五类吸收式热泵，是在第1或第11项所述的第五类吸收式热泵中，增加新增发生器、新增吸收器、新增溶液泵和新增溶液热交换器，将吸收器有稀溶液管路经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器连通，新增吸收器再有稀溶液管路经新增溶液泵和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二溶液泵和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溶液热交换器与新增发生器连通，新增发生器再有浓溶液管路经第二溶液泵和新增溶液热交换器与吸收器连通，新增发生器还有冷剂蒸汽通道与新增吸收器连通，将第三发生器有冷剂液管路经节流阀与蒸发器连通调整为第三发生器有冷剂液管路与新增发生器连通之后新增发生器再有冷剂液管路经节流阀与蒸发器连通，新增吸收器还有冷却介质管路与外部连通，形成第五类吸收式热泵。
19.第五类吸收式热泵，是在第18项所述的任一第五类吸收式热泵中，取消节流阀，将新增发生器有冷剂液管路经节流阀与蒸发器连通调整为新增发生器有冷剂液管路与蒸发器连通，形成第五类吸收式热泵。
20.第五类吸收式热泵，是在第3-5、13-16项所述的任一第五类吸收式热泵中，增加新增发生器、新增吸收器、新增溶液泵和新增溶液热交换器，将吸收器有稀溶液管路经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器连通，新增吸收器再有稀溶液管路经新增溶液泵和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二溶液泵和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溶液热交换器与新增发生器连通，新增发生器再有浓溶液管路经第二溶液泵和新增溶液热交换器与吸收器连通，新增发生器还有冷剂蒸汽通道与新增吸收器连通，将第三发生器有冷剂液管路经节流阀与蒸发器连通调整为第三发生器有冷剂液管路与新增发生器连通之后新增发生器再有冷剂液管路经节流阀与蒸发器连通，将第三发生器有冷剂液管路经第二节流阀与蒸发器连通调整为第三发生器有冷剂液管路与新增发生器连通之后新增发生器再有冷剂液管路经第二节流阀与蒸发器连通，新增吸收器还有冷却介质管路与外部连通，形成第五类吸收式热泵。
21.第五类吸收式热泵，是在第20项所述的任一第五类吸收式热泵中，取消节流阀和第二节流阀，将新增发生器有冷剂液管路经节流阀与蒸发器连通调整为新增发生器有冷剂液管路与蒸发器连通，将新增发生器有冷剂液管路经第二节流阀与蒸发器连通调整为新增发生器有冷剂液管路与蒸发器连通，形成第五类吸收式热泵。
22.第五类吸收式热泵，是在第7-9项所述的任一第五类吸收式热泵中，增加新增发生器、新增吸收器、新增溶液泵和新增溶液热交换器，将吸收器有稀溶液管路经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器连通，新增吸收器再有稀溶液管路经新增溶液泵和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二溶液泵和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溶液热交换器与新增发生器连通，新增发生器再有浓溶液管路经第二溶液泵和新增溶液热交换器与吸收器连通，新增发生器还有冷剂蒸汽通道与新增吸收器连通，将第三 发生器有冷剂液管路经节流阀与蒸发器连通调整为第三发生器有冷剂液管路与新增发生器连通之后新增发生器再有冷剂液管路经节流阀与蒸发器连通，将第三发生器有冷剂液管路经第二节流阀与蒸发器连通调整为第三发生器有冷剂液管路与新增发生器连通之后新增发生器再有冷剂液管路经第二节流阀与蒸发器连通，将第三发生器有冷剂液管路经第三节流阀与蒸发器连通调整为第三发生器有冷剂液管路与新增发生器连通之后新增发生器再有冷剂液管路经第三节流阀与蒸发器连通，新增吸收器还有冷却介质管路与外部连通，形成第五类吸收式热泵。
23.第五类吸收式热泵，是在第22项所述的任一第五类吸收式热泵中，取消节流阀、第二节流阀和第三节流阀，将新增发生器有冷剂液管路经节流阀与蒸发器连通调整为新增发生器有冷剂液管路与蒸发器连通，将新增发生器有冷剂液管路经第二节流阀与蒸发器连通调整为新增发生器有冷剂液管路与蒸发器连通，将新增发生器有冷剂液管路经第三节流阀与蒸发器连通调整为新增发生器有冷剂液管路与蒸发器连通，形成第五类吸收式热泵。
24.第五类吸收式热泵，是在第1或第11项所述的第五类吸收式热泵中，增加新增发生器、新增吸收器、新增溶液泵和新增溶液热交换器，将吸收器有稀溶液管路经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器连通，新增吸收器再有稀溶液管路经新增溶液泵和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二溶液泵和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溶液热交换器与新增发生器连通，新增发生器再有浓溶液管路经第二溶液泵和新增溶液热交换器与吸收器连通，新增发生器还有冷剂蒸汽通道与新增吸收器连通，新增发生器还有余热介质管路与外部连通，新增吸收器还有冷却介质管路与外部连通，形成第五类吸收式热泵。
25.第五类吸收式热泵，是在第24项所述的任一第五类吸收式热泵中，取消节流阀，将第三发生器有冷剂液管路经节流阀与蒸发器连通调整为第三发生器有冷剂液管路与蒸发器连通，形成第五类吸收式热泵。
26.第五类吸收式热泵，是在第3-5、13-16项所述的任一第五类吸收式热泵中，增加新增发生器、新增吸收器、新增溶液泵和新增溶液热交换器，将吸收器有稀溶液管路经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器连通，新增吸收器再有稀溶液管路经新增溶液泵和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二溶液泵和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溶液热交换器与新增发生器连通，新增发生器再有浓溶液管路经第二溶液泵和新增溶液热交换器与吸收器连通，新增发生器还有冷剂蒸汽通道与新增吸收器连通，新增发生器还有余热介质管路与外部连通，新增吸收器还有冷却介质管路与外部连通，形成第五类吸收式热泵。
27.第五类吸收式热泵，是在第26项所述的任一第五类吸收式热泵中，取消节流阀和第二节流阀，将第三发生器有冷剂液管路经节流阀与蒸发器连通调整为第三发生器有冷剂液管路与蒸发器连通，将第三发生器有冷剂液管路经第二节流阀与蒸发器连通调整为第三发生器有冷剂液管路与蒸发器连通，形成第五类吸收式热泵。
28.第五类吸收式热泵，是在第7-9项所述的任一第五类吸收式热泵中，增加新增发 生器、新增吸收器、新增溶液泵和新增溶液热交换器，将吸收器有稀溶液管路经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器连通，新增吸收器再有稀溶液管路经新增溶液泵和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二溶液泵和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溶液热交换器与新增发生器连通，新增发生器再有浓溶液管路经第二溶液泵和新增溶液热交换器与吸收器连通，新增发生器还有冷剂蒸汽通道与新增吸收器连通，新增发生器还有余热介质管路与外部连通，新增吸收器还有冷却介质管路与外部连通，形成第五类吸收式热泵。
29.第五类吸收式热泵，是在第28项所述的任一第五类吸收式热泵中，取消节流阀、第二节流阀和第三节流阀，将第三发生器有冷剂液管路经节流阀与蒸发器连通调整为第三发生器有冷剂液管路与蒸发器连通，将第三发生器有冷剂液管路经第二节流阀与蒸发器连通调整为第三发生器有冷剂液管路与蒸发器连通，将第三发生器有冷剂液管路经第三节流阀与蒸发器连通调整为第三发生器有冷剂液管路与蒸发器连通，形成第五类吸收式热泵。
30.第五类吸收式热泵，是在第1-17项所述的任一第五类吸收式热泵中，增加新增发生器、新增吸收器、新增溶液泵和新增溶液热交换器，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器连通，新增吸收器还有稀溶液管路经新增溶液泵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热交换器与新增吸收器连通，新增发生器还有冷剂蒸汽通道与吸收器连通，新增发生器还有驱动热介质管路与外部连通，新增吸收器还有被加热介质管路与外部连通，形成第五类吸收式热泵。
31.第五类吸收式热泵，是在第18-29项所述的任一第五类吸收式热泵中，增加新增第二发生器、新增第二吸收器、新增第二溶液泵和新增第二溶液热交换器，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第二吸收器连通，新增第二吸收器还有稀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新增第二吸收器连通，新增第二发生器还有冷剂蒸汽通道与吸收器连通，新增第二发生器还有驱动热介质管路与外部连通，新增第二吸收器还有被加热介质管路与外部连通，形成第五类吸收式热泵。
32.第五类吸收式热泵，是在第1-2、11-12项所述的任一第五类吸收式热泵中，增加新增发生器、新增吸收器、新增溶液泵和新增溶液热交换器，将发生器有冷剂蒸汽通道与冷凝器连通调整为发生器有冷剂蒸汽通道与新增吸收器连通，新增吸收器还有稀溶液管路经新增溶液泵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热交换器与新增吸收器连通，新增发生器还有冷剂蒸汽通道与冷凝器连通，新增发生器还有驱动热介质管路与外部连通，新增吸收器还有被加热介质管路与外部连通，形成第五类吸收式热泵。
33.第五类吸收式热泵，是在第18-19、24-25项所述的任一第五类吸收式热泵中，增加新增第二发生器、新增第二吸收器、新增第二溶液泵和新增第二溶液热交换器，将发生器有冷剂蒸汽通道与冷凝器连通调整为发生器有冷剂蒸汽通道与新增第二吸收器连通，新增第二吸收器还有稀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新增第二吸收器连通，新增第二发生器还有冷剂蒸汽通道与冷凝器连通，新增第二发生器还有驱动热介质管路与外部连通，新增第二吸收器还有被加热介质管路与外部连通，形成第五类吸收式热泵。
34.第五类吸收式热泵，是在第1-17项所述的任一第五类吸收式热泵中，第三发生器增设余热介质管路与外部连通，形成第五类吸收式热泵。
35.第五类吸收式热泵，是在第24-29项所述的任一第五类吸收式热泵中，第三发生器增设余热介质管路与外部连通，形成第五类吸收式热泵。
36.第五类吸收式热泵，是在第18-23项所述的任一第五类吸收式热泵中，第三发生器和新增发生器分别增设余热介质管路与外部连通，形成第五类吸收式热泵。
37.第五类吸收式热泵，是在第18-23项所述的任一第五类吸收式热泵中，第三发生器或新增发生器增设余热介质管路与外部连通，形成第五类吸收式热泵。
38.第五类吸收式热泵，是在第34项所述的任一第五类吸收式热泵中，增加新增发生器、新增吸收器、新增溶液泵和新增溶液热交换器，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器连通，新增吸收器还有稀溶液管路经新增溶液泵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热交换器与新增吸收器连通，新增发生器还有冷剂蒸汽通道与吸收器连通，新增发生器还有驱动热介质管路与外部连通，新增吸收器还有被加热介质管路与外部连通，形成第五类吸收式热泵。
39.第五类吸收式热泵，是在第35-37项所述的任一第五类吸收式热泵中，增加新增第二发生器、新增第二吸收器、新增第二溶液泵和新增第二溶液热交换器，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第二吸收器连通，新增第二吸收器还有稀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新增第二吸收器连通，新增第二发生器还有冷剂蒸汽通道与吸收器连通，新增第二发生器还有驱动热介质管路与外部连通，新增第二吸收器还有被加热介质管路与外部连通，形成第五类吸收式热泵。
40.第五类吸收式热泵，是在第1-17项所述的任一第五类吸收式热泵中，增加新增发生器、新增吸收器、新增溶液泵和新增溶液热交换器，将第二发生器有冷剂蒸汽通道与第二吸收器连通调整为第二发生器有冷剂蒸汽通道与新增吸收器连通，将第三发生器有冷剂蒸汽通道与第二吸收器连通调整为第三发生器有冷剂蒸汽通道与新增吸收器连通，新增吸收器还有稀溶液管路经新增溶液泵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热交换器与新增吸收器连通，新增发生器还有冷剂蒸汽通道与第二吸收器连通，新增发生器还有余热介质管路与外部连通，新增吸收器还有冷却介质管路与外部连通，形成第五类吸收式热泵。
41.第五类吸收式热泵，是在第40项所述的任一第五类吸收式热泵中，第三发生器增设余热介质管路与外部连通，形成第五类吸收式热泵。
42.第五类吸收式热泵，是在第18-23项所述的任一第五类吸收式热泵中，增加新增第二发生器、新增第二吸收器、新增第二溶液泵和新增第二溶液热交换器，将新增发生器有冷剂蒸汽通道与新增吸收器连通调整为新增发生器有冷剂蒸汽通道与新增第二吸收器连 通，新增第二吸收器还有稀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新增第二吸收器连通，新增第二发生器还有冷剂蒸汽通道与新增吸收器连通，新增第二发生器还有余热介质管路与外部连通，新增第二吸收器还有冷却介质管路与外部连通，形成第五类吸收式热泵。
43.第五类吸收式热泵，是在第42项所述的任一第五类吸收式热泵中，第三发生器和新增发生器分别增设余热介质管路与外部连通，形成第五类吸收式热泵。
44.第五类吸收式热泵，是在第42项所述的任一第五类吸收式热泵中，第三发生器或新增发生器增设余热介质管路与外部连通，形成第五类吸收式热泵。
45.第五类吸收式热泵，是在第24-29项所述的任一第五类吸收式热泵中，增加新增第二发生器、新增第二吸收器、新增第二溶液泵和新增第二溶液热交换器，将新增发生器有冷剂蒸汽通道与新增吸收器连通调整为新增发生器有冷剂蒸汽通道与新增第二吸收器连通，新增第二吸收器还有稀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新增第二吸收器连通，新增第二发生器还有冷剂蒸汽通道与新增吸收器连通，新增第二发生器还有余热介质管路与外部连通，新增第二吸收器还有冷却介质管路与外部连通，形成第五类吸收式热泵。
46.第五类吸收式热泵，是在第45项所述的任一第五类吸收式热泵中，第三发生器增设余热介质管路与外部连通，形成第五类吸收式热泵。
第五类吸收式热泵，是在第1-2、11-12、24-25项所述的任一第五类吸收式热泵中，将第二发生器有余热介质管路与外部连通调整为第三发生器有余热介质管路与外部连通，将冷凝器有冷剂液管路与第三发生器连通之后第三发生器再有冷剂液管路经节流阀与蒸发器连通调整为冷凝器有冷剂液管路与第二发生器连通之后第二发生器再有冷剂液管路经节流阀与蒸发器连通，形成第五类吸收式热泵。
下面结合图1所示第五类吸收式热泵来进一步说明本发明的实质。在图1所示第五类吸收式热泵中：
(1)冷凝器6的冷剂液流经第三发生器3并放热于溶液，第二吸收器5吸收第三发生器3产生的冷剂蒸汽并放热于冷却介质，将带来如下效果：
①减少了由高温冷剂液带入到蒸发器7中的热负荷，减少了对余热利用的负面影响。
②第三发生器3和第二吸收器5结合，降低了进入发生器1的溶液浓度，则提高了发生器1产生的冷剂蒸汽的品位，或是降低发生器1对驱动热介质温度的要求，或是实现对更低温度的余热资源的利用。
③当环境(冷却介质)介质温度较低时，能够有效利用冷剂液与冷却介质之间的温差，提高驱动热负荷和余热负荷的利用率。
④高温驱动热介质中的热负荷通过发生器1释放到冷剂蒸汽中，一部分通过冷凝器6转移到被加热介质中，另一部分通过第三发生器3和第二吸收器5放热于冷却介质中，属于以高温热负荷分步温降为驱动温差的温差利用新技术。
(2)余热介质流经第二发生器2产生的冷剂蒸汽提供给第二吸收器5，被溶液吸收并放热 于冷却介质，实现余热介质与冷环境(冷却介质)之间温差的利用。
这种以高温驱动热的分步温降为驱动温差和同时实现对冷环境资源利用的吸收式热泵，不同于现有的第一类吸收式热泵、第二类吸收式热泵和第三类吸收式热泵，属于新的类型；按照技术出现的时间及考虑命名顺序，称之为第五类吸收式热泵。
附图说明：
图1是依据本发明所提供的第五类吸收式热泵第1种结构与流程示意图。
图2是依据本发明所提供的第五类吸收式热泵第2种结构与流程示意图。
图3是依据本发明所提供的第五类吸收式热泵第3种结构与流程示意图。
图4是依据本发明所提供的第五类吸收式热泵第4种结构与流程示意图。
图5是依据本发明所提供的第五类吸收式热泵第5种结构与流程示意图。
图6是依据本发明所提供的第五类吸收式热泵第6种结构与流程示意图。
图7是依据本发明所提供的第五类吸收式热泵第7种结构与流程示意图。
图8是依据本发明所提供的第五类吸收式热泵第8种结构与流程示意图。
图9是依据本发明所提供的第五类吸收式热泵第9种结构与流程示意图。
图10是依据本发明所提供的第五类吸收式热泵第10种结构与流程示意图。
图11是依据本发明所提供的第五类吸收式热泵第11种结构与流程示意图。
图12是依据本发明所提供的第五类吸收式热泵第12种结构与流程示意图。
图13是依据本发明所提供的第五类吸收式热泵第13种结构与流程示意图。
图14是依据本发明所提供的第五类吸收式热泵第14种结构与流程示意图。
图15是依据本发明所提供的第五类吸收式热泵第15种结构与流程示意图。
图16是依据本发明所提供的第五类吸收式热泵第16种结构与流程示意图。
图17是依据本发明所提供的第五类吸收式热泵第17种结构与流程示意图。
图18是依据本发明所提供的第五类吸收式热泵第18种结构与流程示意图。
图19是依据本发明所提供的第五类吸收式热泵第19种结构与流程示意图。
图20是依据本发明所提供的第五类吸收式热泵第20种结构与流程示意图。
图中，1-发生器，2-第二发生器，3-第三发生器，4-吸收器，5-第二吸收器，6-冷凝器，7-蒸发器，8-节流阀，9-溶液泵，10-第二溶液泵，11-溶液热交换器，12-第二溶液热交换器，13-第四发生器，14-第二节流阀，15-第三溶液泵，16-第三溶液热交换器，17-热交换器，18-第五发生器，19-第三节流阀，20-第四溶液泵，21-第四溶液热交换器，22-第二热交换器，23-第三吸收器；A-新增发生器，B-新增吸收器，C-新增溶液泵，D-新增溶液热交换器。
这里要说明的是：以附图1所示第五类吸收式热泵为例，冷剂液管路中设置的节流阀8，可用重力压降替代；当冷却介质温度较低，流经第三发生器3的冷剂液温度降温至蒸发器7内部的蒸发温度时，不设置节流阀8，而将动力压差用于第三发生器3内部热交换器管路中。
具体实施方式：
首先要说明的是，在结构和流程的表述上，非必要情况下不重复进行；对显而易见的流程不作表述。下面结合附图和实例来详细描述本发明。
图1所示的第五类吸收式热泵是这样实现的：
(1)结构上，它主要由发生器、第二发生器、第三发生器、吸收器、第二吸收器、冷凝器、蒸发器、节流阀、溶液泵、第二溶液泵、溶液热交换器和第二溶液热交换器所组成；吸收器4有稀溶液管路经溶液热交换器11与第二吸收器5连通，第二吸收器5还有稀溶液管路经溶液泵9和第二溶液热交换器12与发生器1连通，发生器1还有浓溶液管路经第二溶液热交换器12与第二发生器2连通，第二发生器2还有浓溶液管路与第三发生器3连通，第三发生器3还有浓溶液管路经第二溶液泵10和溶液热交换器11与吸收器4连通，发生器1还有冷剂蒸汽通道与冷凝器6连通，冷凝器6还有冷剂液管路与第三发生器3连通之后第三发生器3再有冷剂液管路经节流阀8与蒸发器7连通，第二发生器2和第三发生器3还分别有冷剂蒸汽通道与第二吸收器5连通，蒸发器7还有冷剂蒸汽通道与吸收器4连通，发生器1还有驱动热介质管路与外部连通，吸收器4和冷凝器6还分别有被加热介质管路与外部连通，第二发生器2和蒸发器7还分别有余热介质管路与外部连通，第二吸收器5还有冷却介质管路与外部连通。
(2)流程上，吸收器4的稀溶液经溶液热交换器11进入第二吸收器5、吸收冷剂蒸汽并放热于冷却介质，第二吸收器5的稀溶液经溶液泵9和第二溶液热交换器12进入发生器1，驱动热介质流经发生器1、加热进入其内的溶液释放冷剂蒸汽并向冷凝器6提供，发生器1的浓溶液经第二溶液热交换器12进入第二发生器2，余热介质流经第二发生器2、加热进入其内的溶液释放冷剂蒸汽并向第二吸收器5提供，第二发生器2的浓溶液进入第三发生器3、吸热释放冷剂蒸汽并向第二吸收器5提供，第三发生器3的浓溶液经第二溶液泵10和溶液热交换器11进入吸收器4、吸收冷剂蒸汽并放热于被加热介质；冷凝器6的冷剂蒸汽放热于被加热介质成冷剂液，冷剂液流经第三发生器3放热降温，降温之后的冷剂液经节流阀8节流进入蒸发器7、吸热成冷剂蒸汽并向吸收器4提供，形成第五类吸收式热泵。
图2所示的第五类吸收式热泵是这样实现的：
(1)结构上，在图1所示第五类吸收式热泵中，增加第四发生器、第二节流阀、第三溶液泵、第三溶液热交换器和热交换器，第二吸收器5增设稀溶液管路经第三溶液泵15和第三溶液热交换器16与第四发生器13连通，第四发生器13还有浓溶液管路经第三溶液热交换器16与第二发生器2连通，将发生器1有冷剂蒸汽通道与冷凝器6连通调整为发生器1有冷剂蒸汽通道与第四发生器13连通之后第四发生器13再有冷剂液管路经热交换器17、第三发生器3和第二节流阀14与蒸发器7连通，第四发生器13还有冷剂蒸汽通道与冷凝器6连通，热交换器17还有被加热介质管路与外部连通。
(2)流程上，发生器1产生的冷剂蒸汽提供给第四发生器13作驱动热介质，第二吸收器5的部分稀溶液经第三溶液泵15和第三溶液热交换器16进入第四发生器13，冷剂蒸汽流经第四发生器13、加热进入其内的溶液释放冷剂蒸汽并向冷凝器6提供，第四发生器13的浓溶液经第三溶液热交换器16进入第二发生器2；流经第四发生器13的冷剂蒸汽放热成冷剂液之后依次流经热交换器17和第三发生器3并逐步放热降温，降温后的冷剂液经第二节流阀14节流进入蒸发器7，形成第五类吸收式热泵。
图3所示的第五类吸收式热泵是这样实现的：
(1)结构上，在图1所示第五类吸收式热泵中，增加第四发生器、第二节流阀、第三溶液热交换器和热交换器，将第二吸收器5有稀溶液管路经溶液泵9和第二溶液热交换器12 与发生器1连通调整为第二吸收器5有稀溶液管路经溶液泵9、第二溶液热交换器12和第三溶液热交换器16与发生器1连通，将发生器1有浓溶液管路经第二溶液热交换器12与第二发生器2连通调整为发生器1有浓溶液管路经第三溶液热交换器16与第四发生器13连通，第四发生器13再有浓溶液管路经第二溶液热交换器12与第二发生器2连通，将发生器1有冷剂蒸汽通道与冷凝器6连通调整为发生器1有冷剂蒸汽通道与第四发生器13连通之后第四发生器13再有冷剂液管路经热交换器17、第三发生器3和第二节流阀14与蒸发器7连通，第四发生器13还有冷剂蒸汽通道与冷凝器6连通，热交换器17还有被加热介质管路与外部连通。
(2)流程上，发生器1产生的冷剂蒸汽提供给第四发生器13作驱动热介质，第二吸收器5的稀溶液经溶液泵9、第二溶液热交换器12和第三溶液热交换器16进入发生器1，发生器1的浓溶液经第三溶液热交换器16进入第四发生器13，冷剂蒸汽流经第四发生器13、加热进入其内的溶液释放冷剂蒸汽并向冷凝器6提供，第四发生器13的浓溶液经第二溶液热交换器12进入第二发生器2；流经第四发生器13的冷剂蒸汽放热成冷剂液之后依次流经热交换器17和第三发生器3并逐步放热降温，降温后的冷剂液经第二节流阀14节流进入蒸发器7，形成第五类吸收式热泵。
图4所示的第五类吸收式热泵是这样实现的：
(1)结构上，在图1所示第五类吸收式热泵中，增加第四发生器、第二节流阀、第三溶液泵、第三溶液热交换器和热交换器，将第二吸收器5有稀溶液管路经溶液泵9和第二溶液热交换器12与发生器1连通调整为第二吸收器5有稀溶液管路经溶液泵9和第二溶液热交换器12与第四发生器13连通，第四发生器13再有浓溶液管路经第三溶液泵15和第三溶液热交换器16与发生器1连通，将发生器1有浓溶液管路经第二溶液热交换器12与第二发生器2连通调整为发生器1有浓溶液管路经第三溶液热交换器16和第二溶液热交换器12与第二发生器2连通，将发生器1有冷剂蒸汽通道与冷凝器6连通调整为发生器1有冷剂蒸汽通道与第四发生器13连通之后第四发生器13再有冷剂液管路经热交换器17、第三发生器3和第二节流阀14与蒸发器7连通，第四发生器13还有冷剂蒸汽通道与冷凝器6连通，热交换器17还有被加热介质管路与外部连通。
(2)流程上，发生器1产生的冷剂蒸汽提供给第四发生器13作驱动热介质，第二吸收器5的稀溶液经溶液泵9和第二溶液热交换器12进入第四发生器13，冷剂蒸汽流经第四发生器13、加热进入其内的溶液释放冷剂蒸汽并向冷凝器6提供，第四发生器13的浓溶液经第三溶液泵15和第三溶液热交换器16进入发生器1，发生器1的浓溶液经第三溶液热交换器16和第二溶液热交换器12进入第二发生器2；流经第四发生器13的冷剂蒸汽放热成冷剂液之后依次流经热交换器17和第三发生器3并逐步放热降温，降温后的冷剂液经第二节流阀14节流进入蒸发器7，形成第五类吸收式热泵。
图5所示的第五类吸收式热泵是这样实现的：
(1)结构上，在图2所示第五类吸收式热泵中，增加第五发生器、第三节流阀，第四溶液泵、第四溶液热交换器和第二热交换器，第二吸收器5增设稀溶液管路经第四溶液泵20和第四溶液热交换器21与第五发生器18连通，第五发生器18还有浓溶液管路经第四溶液热交换器21与第二发生器2连通，第五发生器18还有冷剂蒸汽通道与冷凝器6连通，将 第四发生器13有冷剂蒸汽通道与冷凝器6连通调整为第四发生器13有冷剂蒸汽通道与第五发生器18连通之后第五发生器18再有冷剂液管路经第二热交换器22、第三发生器3和第三节流阀19与蒸发器7连通，将第四发生器13有冷剂液管路经热交换器17、第三发生器3和第二节流阀14与蒸发器7连通调整为第四发生器13有冷剂液管路经第五发生器18、热交换器17、第三发生器3和第二节流阀14与蒸发器7连通，第二热交换器22还有被加热介质管路与外部连通。
(2)流程上，第四发生器13产生的冷剂蒸汽和冷剂液提供给第五发生器18作驱动热介质，第二吸收器5的部分稀溶液经第四溶液泵20和第四溶液热交换器21进入第五发生器18，冷剂蒸汽和冷剂液流经第五发生器18、加热进入其内的溶液释放冷剂蒸汽并向冷凝器6提供，第五发生器18的浓溶液经第四溶液热交换器21进入第二发生器2；流经第五发生器18的冷剂蒸汽放热成冷剂液之后依次流经第二热交换器22和第三发生器3放热降温之后再经第三节流阀19节流进入蒸发器7，第四发生器13的冷剂液依次流经第五发生器18、热交换器17、第三发生器3和第二节流阀14进入蒸发器7，形成第五类吸收式热泵。
图6所示的第五类吸收式热泵是这样实现的：
(1)结构上，在图3所示第五类吸收式热泵中，增加第五发生器、第三节流阀、第四溶液热交换器和第二热交换器，将第二吸收器5有稀溶液管路经溶液泵9、第二溶液热交换器12和第三溶液热交换器16与发生器1连通调整为第二吸收器5有稀溶液管路经溶液泵9、第四溶液热交换器21、第二溶液热交换器12和第三溶液热交换器16与发生器1连通，将第四发生器13有浓溶液管路经第二溶液热交换器12与第二发生器2连通调整为第四发生器13有浓溶液管路经第二溶液热交换器12与第五发生器18连通，第五发生器18再有浓溶液管路经第四溶液热交换器21与第二发生器2连通，第五发生器18还有冷剂蒸汽通道与冷凝器6连通，将第四发生器13有冷剂蒸汽通道与冷凝器6连通调整为第四发生器13有冷剂蒸汽通道与第五发生器18连通之后第五发生器18再有冷剂液管路经第二热交换器22、第三发生器3和第三节流阀19与蒸发器7连通，将第四发生器13有冷剂液管路经热交换器17、第三发生器3和第二节流阀14与蒸发器7连通调整为第四发生器13有冷剂液管路经第五发生器18、热交换器17、第三发生器3和第二节流阀14与蒸发器7连通，第二热交换器22还有被加热介质管路与外部连通。
(2)流程上，第四发生器13产生的冷剂蒸汽和冷剂液提供给第五发生器18作驱动热介质，第二吸收器5的稀溶液经溶液泵9、第四溶液热交换器21、第二溶液热交换器12和第三溶液热交换器16进入发生器1，发生器1的浓溶液经第三溶液热交换器16进入第四发生器13，第四发生器13的浓溶液经第二溶液热交换器12进入第五发生器18，冷剂蒸汽和冷剂液流经第五发生器18、加热进入其内的溶液释放冷剂蒸汽并向冷凝器6提供，第五发生器18的浓溶液经第四溶液热交换器21进入第二发生器2；流经第五发生器18的冷剂蒸汽放热成冷剂液之后依次流经第二热交换器22和第三发生器3放热降温之后再经第三节流阀19节流进入蒸发器7，第四发生器13的冷剂液依次流经第五发生器18、热交换器17、第三发生器3和第二节流阀14进入蒸发器7，形成第五类吸收式热泵。
图7所示的第五类吸收式热泵是这样实现的：
(1)结构上，在图4所示第五类吸收式热泵中，增加第五发生器、第三节流阀，第四溶 液泵、第四溶液热交换器和第二热交换器，将第二吸收器5有稀溶液管路经溶液泵9和第二溶液热交换器12与第四发生器13连通调整为第二吸收器5有稀溶液管路经溶液泵9和第二溶液热交换器12与第五发生器18连通，第五发生器18再有浓溶液管路经第四溶液泵20和第四溶液热交换器21与第四发生器13连通，将发生器1有浓溶液管路经第三溶液热交换器16和第二溶液热交换器12与第二发生器2连通调整为发生器1有浓溶液管路经第三溶液热交换器16、第四溶液热交换器21和第二溶液热交换器12与第二发生器2连通，第五发生器18还有冷剂蒸汽通道与冷凝器6连通，将第四发生器13有冷剂蒸汽通道与冷凝器6连通调整为第四发生器13有冷剂蒸汽通道与第五发生器18连通之后第五发生器18再有冷剂液管路经第二热交换器22、第三发生器3和第三节流阀19与蒸发器7连通，将第四发生器13有冷剂液管路经热交换器17、第三发生器3和第二节流阀14与蒸发器7连通调整为第四发生器13有冷剂液管路经第五发生器18、热交换器17、第三发生器3和第二节流阀14与蒸发器7连通，第二热交换器22还有被加热介质管路与外部连通。
(2)流程上，第四发生器13产生的冷剂蒸汽和冷剂液提供给第五发生器18作驱动热介质，第二吸收器5的稀溶液经溶液泵9和第二溶液热交换器12进入第五发生器18，冷剂蒸汽和冷剂液流经第五发生器18、加热进入其内的溶液释放冷剂蒸汽并向冷凝器6提供，第五发生器18的浓溶液经第四溶液泵20和第四溶液热交换器21进入第四发生器13，第四发生器13的浓溶液经第三溶液泵15和第三溶液热交换器16进入发生器1，发生器1的浓溶液经第三溶液热交换器16、第四溶液热交换器21和第二溶液热交换器12进入第二发生器2；流经第五发生器18的冷剂蒸汽放热成冷剂液之后依次流经第二热交换器22和第三发生器3放热降温之后再经第三节流阀19节流进入蒸发器7，第四发生器13的冷剂液依次流经第五发生器18、热交换器17、第三发生器3和第二节流阀14进入蒸发器7，形成第五类吸收式热泵。
图8所示的第五类吸收式热泵是这样实现的：
(1)结构上，它主要由发生器、第二发生器、第三发生器、吸收器、第二吸收器、冷凝器、蒸发器、节流阀、溶液泵、第二溶液泵、溶液热交换器、第二溶液热交换器、第四发生器、第三溶液泵、第三溶液热交换器和第三吸收器所组成；吸收器4有稀溶液管路经溶液热交换器11与第二吸收器5连通，第二吸收器5还有稀溶液管路经溶液泵9和第二溶液热交换器12与第三吸收器23连通，第三吸收器23还有稀溶液管路经第三溶液泵15和第三溶液热交换器16与发生器1连通，发生器1还有浓溶液管路经第三溶液热交换器16与第四发生器13连通，第四发生器13还有浓溶液管路经第二溶液热交换器12与第二发生器2连通，第二发生器2还有浓溶液管路与第三发生器3连通，第三发生器3还有浓溶液管路经第二溶液泵10和溶液热交换器11与吸收器4连通，发生器1还有冷剂蒸汽通道与冷凝器6连通，冷凝器6还有冷剂液管路与第三发生器3连通之后第三发生器3再有冷剂液管路经节流阀8与蒸发器7连通，第二发生器2和第三发生器3还分别有冷剂蒸汽通道与第二吸收器5连通，第四发生器13还有冷剂蒸汽通道与第三吸收器23连通，蒸发器7还有冷剂蒸汽通道与吸收器4连通，发生器1和第四发生器13还分别有驱动热介质管路与外部连通，吸收器4、冷凝器6和第三吸收器23还分别有被加热介质管路与外部连通，第二发生器2和蒸发器7还分别有余热介质管路与外部连通，第二吸收器5还有冷却介质管路与 外部连通。
(2)流程上，吸收器4的稀溶液经溶液热交换器11进入第二吸收器5、吸收冷剂蒸汽并放热于冷却介质，第二吸收器5的稀溶液经溶液泵9和第二溶液热交换器12进入第三吸收器23、吸收冷剂蒸汽并放热于被加热介质，第三吸收器23的稀溶液经第三溶液泵15和第三溶液热交换器16进入发生器1，驱动热介质流经发生器1、加热进入其内的溶液释放冷剂蒸汽并向冷凝器6提供，发生器1的浓溶液经第三溶液热交换器16进入第四发生器13，驱动热介质流经第四发生器13、加热进入其内的溶液释放冷剂蒸汽并向第三吸收器23提供，第四发生器13的浓溶液经第二溶液热交换器12进入第二发生器2，余热介质流经第二发生器2、加热进入其内的溶液释放冷剂蒸汽并向第二吸收器5提供，第二发生器2的浓溶液进入第三发生器3、吸热释放冷剂蒸汽并向第二吸收器5提供，第三发生器3的浓溶液经第二溶液泵10和溶液热交换器11进入吸收器4、吸收冷剂蒸汽并放热于被加热介质；冷凝器6的冷剂蒸汽放热于被加热介质成冷剂液，冷剂液流经第三发生器3放热降温，降温之后的冷剂液经节流阀8节流进入蒸发器7、吸热成冷剂蒸汽并向吸收器4提供，形成第五类吸收式热泵。
图9所示的第五类吸收式热泵是这样实现的：
(1)结构上，在图8所示第五类吸收式热泵中，增加第五发生器、第二节流阀、第四溶液泵、第四溶液热交换器和热交换器，第三吸收器23增设稀溶液管路经第四溶液泵20和第四溶液热交换器21与第五发生器18连通，第五发生器18还有浓溶液管路经第四溶液热交换器21与第四发生器13连通，将发生器1有冷剂蒸汽通道与冷凝器6连通调整为发生器1有冷剂蒸汽通道与第五发生器18连通之后第五发生器18再有冷剂液管路经热交换器17、第三发生器3和第二节流阀14与蒸发器7连通，第五发生器18还有冷剂蒸汽通道与冷凝器6连通，热交换器17还有被加热介质管路与外部连通。
(2)流程上，发生器1产生的冷剂蒸汽提供给第五发生器18作驱动热介质，第三吸收器23的部分稀溶液经第四溶液泵20和第四溶液热交换器21进入第五发生器18，冷剂蒸汽流经第五发生器18、加热进入其内的溶液释放冷剂蒸汽并向冷凝器6提供，第五发生器18的浓溶液经第四溶液热交换器21进入第四发生器13；流经第五发生器18的冷剂蒸汽放热成冷剂液之后依次流经热交换器17和第三发生器3并逐步放热降温，降温后的冷剂液经第二节流阀14节流进入蒸发器7，形成第五类吸收式热泵。
图10所示的第五类吸收式热泵是这样实现的：
(1)结构上，在图8所示第五类吸收式热泵中，增加第五发生器、第二节流阀、第四溶液热交换器和热交换器，将第三吸收器23有稀溶液管路经第三溶液泵15和第三溶液热交换器16与发生器1连通调整为第三吸收器23有稀溶液管路经第三溶液泵15、第三溶液热交换器16和第四溶液热交换器21与发生器1连通，将发生器1有浓溶液管路经第三溶液热交换器16与第四发生器13连通调整为发生器1有浓溶液管路经第四溶液热交换器21与第五发生器18连通，第五发生器18再有浓溶液管路经第三溶液热交换器16与第四发生器13连通，将发生器1有冷剂蒸汽通道与冷凝器6连通调整为发生器1有冷剂蒸汽通道与第五发生器18连通之后第五发生器18再有冷剂液管路经热交换器17、第三发生器3和第二节流阀14与蒸发器7连通，第五发生器18还有冷剂蒸汽通道与冷凝器6连通，第五发生 器18还有驱动热介质管路与外部连通，热交换器17还有被加热介质管路与外部连通。
(2)流程上，驱动热介质和发生器1产生的冷剂蒸汽向第五发生器18提供驱动热负荷，第三吸收器23的稀溶液经第三溶液泵15、第三溶液热交换器16和第四溶液热交换器21进入发生器1，发生器1的浓溶液经第四溶液热交换器21进入第五发生器18，驱动热介质和冷剂蒸汽流经第五发生器18、加热进入其内的溶液释放冷剂蒸汽并向冷凝器6提供，第五发生器18的浓溶液经第三溶液热交换器16进入第四发生器13；流经第五发生器18的冷剂蒸汽放热成冷剂液之后依次流经热交换器17和第三发生器3并逐步放热降温，降温后的冷剂液经第二节流阀14节流进入蒸发器7，形成第五类吸收式热泵。
图11所示的第五类吸收式热泵是这样实现的：
(1)结构上，在图8所示第五类吸收式热泵中，增加第五发生器、第二节流阀、第四溶液泵、第四溶液热交换器和热交换器，将第三吸收器23有稀溶液管路经第三溶液泵15和第三溶液热交换器16与发生器1连通调整为第三吸收器23有稀溶液管路经第三溶液泵15和第三溶液热交换器16与第五发生器18连通，第五发生器18再有浓溶液管路经第四溶液泵20和第四溶液热交换器21与发生器1连通，将发生器1有浓溶液管路经第三溶液热交换器16与第四发生器13连通调整为发生器1有浓溶液管路经第四溶液热交换器21和第三溶液热交换器16与第四发生器13连通，将发生器1有冷剂蒸汽通道与冷凝器6连通调整为发生器1有冷剂蒸汽通道与第五发生器18连通之后第五发生器18再有冷剂液管路经热交换器17、第三发生器3和第二节流阀14与蒸发器7连通，第五发生器18还有冷剂蒸汽通道与冷凝器6连通，热交换器17还有被加热介质管路与外部连通。
(2)流程上，发生器1产生的冷剂蒸汽提供给第五发生器18作驱动热介质，第三吸收器23的稀溶液经第三溶液泵15和第三溶液热交换器16进入第五发生器18，冷剂蒸汽流经第五发生器18、加热进入其内的溶液释放冷剂蒸汽并向冷凝器6提供，第五发生器18的浓溶液经第四溶液泵20和第四溶液热交换器21进入发生器1，发生器1的浓溶液经第四溶液热交换器21和第三溶液热交换器16进入第四发生器13；流经第五发生器18的冷剂蒸汽放热成冷剂液之后依次流经热交换器17和第三发生器3并逐步放热降温，降温后的冷剂液经第二节流阀14节流进入蒸发器7，形成第五类吸收式热泵。
图12所示的第五类吸收式热泵是这样实现的：
(1)结构上，在图1所示第五类吸收式热泵中，增加新增发生器、新增吸收器、新增溶液泵和新增溶液热交换器，将吸收器4有稀溶液管路经溶液热交换器11与第二吸收器5连通调整为吸收器4有稀溶液管路经新增溶液热交换器D与新增吸收器B连通，新增吸收器B再有稀溶液管路经新增溶液泵C和溶液热交换器11与第二吸收器5连通，将第三发生器3有浓溶液管路经第二溶液泵10和溶液热交换器11与吸收器4连通调整为第三发生器3有浓溶液管路经溶液热交换器11与新增发生器A连通，新增发生器A再有浓溶液管路经第二溶液泵10和新增溶液热交换器D与吸收器4连通，新增发生器A还有冷剂蒸汽通道与新增吸收器B连通，将第三发生器3有冷剂液管路经节流阀8与蒸发器7连通调整为第三发生器3有冷剂液管路与新增发生器A连通之后新增发生器A再有冷剂液管路经节流阀8与蒸发器7连通，新增吸收器B还有冷却介质管路与外部连通。
(2)流程上，吸收器4的稀溶液经新增溶液热交换器D进入新增吸收器B、吸收冷剂蒸汽 并放热于冷却介质，新增吸收器B的稀溶液经新增溶液泵C和溶液热交换器11进入第二吸收器5；第三发生器3的浓溶液经溶液热交换器11进入新增发生器A、吸热释放冷剂蒸汽并向新增吸收器B提供，新增发生器A的浓溶液经第二溶液泵10和新增溶液热交换器D进入吸收器4；冷凝器6的冷剂液依次流经第三发生器3和新增发生器A并逐步放热降温，降温之后的冷剂液经节流阀8节流进入蒸发器7，形成第五类吸收式热泵。
图13所示的第五类吸收式热泵是这样实现的：
(1)结构上，在图2所示第五类吸收式热泵中，增加新增发生器、新增吸收器、新增溶液泵和新增溶液热交换器，将吸收器4有稀溶液管路经溶液热交换器11与第二吸收器5连通调整为吸收器4有稀溶液管路经新增溶液热交换器D与新增吸收器B连通，新增吸收器B再有稀溶液管路经新增溶液泵C和溶液热交换器11与第二吸收器5连通，将第三发生器3有浓溶液管路经第二溶液泵10和溶液热交换器11与吸收器4连通调整为第三发生器3有浓溶液管路经溶液热交换器11与新增发生器A连通，新增发生器A再有浓溶液管路经第二溶液泵10和新增溶液热交换器D与吸收器4连通，新增发生器A还有冷剂蒸汽通道与新增吸收器B连通，将第三发生器3有冷剂液管路经节流阀8与蒸发器7连通调整为第三发生器3有冷剂液管路与新增发生器A连通之后新增发生器A再有冷剂液管路经节流阀8与蒸发器7连通，将第三发生器3有冷剂液管路经第二节流阀14与蒸发器7连通调整为第三发生器3有冷剂液管路与新增发生器A连通之后新增发生器A再有冷剂液管路经第二节流阀14与蒸发器7连通，新增吸收器B还有冷却介质管路与外部连通。
(2)流程上，吸收器4的稀溶液经新增溶液热交换器D进入新增吸收器B、吸收冷剂蒸汽并放热于冷却介质，新增吸收器B的稀溶液经新增溶液泵C和溶液热交换器11进入第二吸收器5；第三发生器3的浓溶液经溶液热交换器11进入新增发生器A、吸热释放冷剂蒸汽并向新增吸收器B提供，新增发生器A的浓溶液经第二溶液泵10和新增溶液热交换器D进入吸收器4；冷凝器6的冷剂液依次流经第三发生器3和新增发生器A并逐步放热降温，降温之后的冷剂液经节流阀8节流进入蒸发器7；第四发生器13产生的冷剂液依次流经热交换器17、第三发生器3和新增发生器A并逐步放热降温，降温之后的冷剂液经第二节流阀14节流进入蒸发器7，形成第五类吸收式热泵。
图14所示的第五类吸收式热泵是这样实现的：
(1)结构上，在图5所示第五类吸收式热泵中，增加新增发生器、新增吸收器、新增溶液泵和新增溶液热交换器，将吸收器4有稀溶液管路经溶液热交换器11与第二吸收器5连通调整为吸收器4有稀溶液管路经新增溶液热交换器D与新增吸收器B连通，新增吸收器B再有稀溶液管路经新增溶液泵C和溶液热交换器11与第二吸收器5连通，将第三发生器3有浓溶液管路经第二溶液泵10和溶液热交换器11与吸收器4连通调整为第三发生器3有浓溶液管路经溶液热交换器11与新增发生器A连通，新增发生器A再有浓溶液管路经第二溶液泵10和新增溶液热交换器D与吸收器4连通，新增发生器A还有冷剂蒸汽通道与新增吸收器B连通，将第三发生器3有冷剂液管路经节流阀8与蒸发器7连通调整为第三发生器3有冷剂液管路与新增发生器A连通之后新增发生器A再有冷剂液管路经节流阀8与蒸发器7连通，将第三发生器3有冷剂液管路经第二节流阀14与蒸发器7连通调整为第三发生器3有冷剂液管路与新增发生器A连通之后新增发生器A再有冷剂液管路经第二节流阀 14与蒸发器7连通，将第三发生器3有冷剂液管路经第三节流阀19与蒸发器7连通调整为第三发生器3有冷剂液管路与新增发生器A连通之后新增发生器A再有冷剂液管路经第三节流阀19与蒸发器7连通，新增吸收器B还有冷却介质管路与外部连通。
(2)流程上，吸收器4的稀溶液经新增溶液热交换器D进入新增吸收器B、吸收冷剂蒸汽并放热于冷却介质，新增吸收器B的稀溶液经新增溶液泵C和溶液热交换器11进入第二吸收器5；第三发生器3的浓溶液经溶液热交换器11进入新增发生器A、吸热释放冷剂蒸汽并向新增吸收器B提供，新增发生器A的浓溶液经第二溶液泵10和新增溶液热交换器D进入吸收器4；冷凝器6的冷剂液依次流经第三发生器3和新增发生器A并逐步放热降温，降温之后的冷剂液经节流阀8节流进入蒸发器7；第四发生器13产生的冷剂液依次流经第五发生器18、热交换器17、第三发生器3和新增发生器A并逐步放热降温，降温之后的冷剂液经第二节流阀14节流进入蒸发器7；第五发生器18产生的冷剂液依次流经第二热交换器22、第三发生器3和新增发生器A并逐步放热降温，降温之后的冷剂液经第三节流阀19节流进入蒸发器7，形成第五类吸收式热泵。
图15所示的第五类吸收式热泵是这样实现的：
(1)结构上，在图1所示第五类吸收式热泵中，增加新增发生器、新增吸收器、新增溶液泵和新增溶液热交换器，将吸收器4有稀溶液管路经溶液热交换器11与第二吸收器5连通调整为吸收器4有稀溶液管路经新增溶液热交换器D与新增吸收器B连通，新增吸收器B再有稀溶液管路经新增溶液泵C和溶液热交换器11与第二吸收器5连通，将第三发生器3有浓溶液管路经第二溶液泵10和溶液热交换器11与吸收器4连通调整为第三发生器3有浓溶液管路经溶液热交换器11与新增发生器A连通，新增发生器A再有浓溶液管路经第二溶液泵10和新增溶液热交换器D与吸收器4连通，新增发生器A还有冷剂蒸汽通道与新增吸收器B连通，新增发生器A还有余热介质管路与外部连通，新增吸收器B还有冷却介质管路与外部连通。
(2)流程上，吸收器4的稀溶液经新增溶液热交换器D进入新增吸收器B、吸收冷剂蒸汽并放热于冷却介质，新增吸收器B的稀溶液经新增溶液泵C和溶液热交换器11进入第二吸收器5；第三发生器3的浓溶液经溶液热交换器11进入新增发生器A，余热介质流经新增发生器A、加热进入其内的溶液释放冷剂蒸汽并向新增吸收器B提供，新增发生器A的浓溶液经第二溶液泵10和新增溶液热交换器D进入吸收器4，形成第五类吸收式热泵。
图16所示的第五类吸收式热泵是这样实现的：
(1)结构上，在图1所示第五类吸收式热泵中，增加新增发生器、新增吸收器、新增溶液泵和新增溶液热交换器，将蒸发器7有冷剂蒸汽通道与吸收器4连通调整为蒸发器7有冷剂蒸汽通道与新增吸收器B连通，新增吸收器B还有稀溶液管路经新增溶液泵C和新增溶液热交换器D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D与新增吸收器B连通，新增发生器A还有冷剂蒸汽通道与吸收器4连通，新增发生器A还有驱动热介质管路与外部连通，新增吸收器B还有被加热介质管路与外部连通。
(2)流程上，蒸发器7产生的冷剂蒸汽进入新增吸收器B，新增吸收器B的稀溶液经新增溶液泵C和新增溶液热交换器D进入新增发生器A，驱动热介质流经新增发生器A、加热进入其内的溶液释放冷剂蒸汽并向吸收器4提供，新增发生器A的浓溶液经新增溶液热交换 器D进入新增吸收器B、吸收冷剂蒸汽并放热于被加热介质，形成第五类吸收式热泵。
图17所示的第五类吸收式热泵是这样实现的：
(1)结构上，在图1所示第五类吸收式热泵中，增加新增发生器、新增吸收器、新增溶液泵和新增溶液热交换器，将发生器1有冷剂蒸汽通道与冷凝器6连通调整为发生器1有冷剂蒸汽通道与新增吸收器B连通，新增吸收器B还有稀溶液管路经新增溶液泵C和新增溶液热交换器D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D与新增吸收器B连通，新增发生器A还有冷剂蒸汽通道与冷凝器6连通，新增发生器A还有驱动热介质管路与外部连通，新增吸收器B还有被加热介质管路与外部连通。
(2)流程上，发生器1产生的冷剂蒸汽进入增吸收器B，新增吸收器B的稀溶液经新增溶液泵C和新增溶液热交换器D进入新增发生器A，驱动热介质流经新增发生器A、加热进入其内的溶液释放冷剂蒸汽并向冷凝器6提供，新增发生器A的浓溶液经新增溶液热交换器D进入新增吸收器B、吸收冷剂蒸汽并放热于被加热介质，形成第五类吸收式热泵。
图18所示的第五类吸收式热泵是这样实现的：
在图1所示第五类吸收式热泵中，第三发生器3增设余热介质管路与外部连通；冷剂液和余热介质共同向第三发生器3提供驱动热负荷，形成第五类吸收式热泵。
图19所示的第五类吸收式热泵是这样实现的：
(1)结构上，在图1所示第五类吸收式热泵中，增加新增发生器、新增吸收器、新增溶液泵和新增溶液热交换器，将第二发生器2有冷剂蒸汽通道与第二吸收器5连通调整为第二发生器2有冷剂蒸汽通道与新增吸收器B连通，将第三发生器3有冷剂蒸汽通道与第二吸收器5连通调整为第三发生器3有冷剂蒸汽通道与新增吸收器B连通，新增吸收器B还有稀溶液管路经新增溶液泵C和新增溶液热交换器D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D与新增吸收器B连通，新增发生器A还有冷剂蒸汽通道与第二吸收器5连通，新增发生器A还有余热介质管路与外部连通，新增吸收器B还有冷却介质管路与外部连通。
(2)流程上，第二发生器2和第三发生器3产生的冷剂蒸汽进入增吸收器B，新增吸收器B的稀溶液经新增溶液泵C和新增溶液热交换器D进入新增发生器A，余热介质流经新增发生器A、加热进入其内的溶液释放冷剂蒸汽并向第二吸收器5提供，新增发生器A的浓溶液经新增溶液热交换器D进入新增吸收器B、吸收冷剂蒸汽并放热于冷却介质，形成第五类吸收式热泵。
图20所示的第五类吸收式热泵是这样实现的：
在图1所示第五类吸收式热泵中，将第二发生器2有余热介质管路与外部连通调整为第三发生器3有余热介质管路与外部连通，将冷凝器6有冷剂液管路与第三发生器3连通之后第三发生器3再有冷剂液管路经节流阀8与蒸发器7连通调整为冷凝器6有冷剂液管路与第二发生器2连通之后第二发生器2再有冷剂液管路经节流阀8与蒸发器7连通；冷剂液向第二发生器2提供驱动热负荷，余热介质向第三发生器3提供驱动热负荷，形成第五类吸收式热泵。
本发明技术可以实现的效果——本发明所提出的第五类吸收式热泵，具有如下效果和优势：
(1)提出了温差利用的新思路、新概念和新技术，将推动吸收式热泵技术的进一步发展和应用。
(2)能够很好地解决高温冷剂液对余热利用程度的负面影响，尤其是对以TFE-TDE溶液为典型代表的吸收式热泵流程，能够显著提高吸收式热泵的性能指数和余热利用率。
(3)将温差利用程度扩展到低温冷环境，进一步提高了温差利用水平，并对因冷剂液向环境释放热能所带来的性能指数降低起到抑制和弥补作用。
(4)能够降低对驱动热介质温度要求，或提高余热利用的程度，或能够利用更低温度的余热资源。
(5)给出多种具体技术方案，能够应对众多不同的实际状况，有较宽的适用范围。
(6)丰富了吸收式热泵的类型，扩展了吸收式热泵的应用范围，有利于更好地采用吸收式热泵来实现温差的充分利用。

Claims (47)

  1. 第五类吸收式热泵，主要由发生器、第二发生器、第三发生器、吸收器、第二吸收器、冷凝器、蒸发器、节流阀、溶液泵、第二溶液泵、溶液热交换器和第二溶液热交换器所组成；吸收器(4)有稀溶液管路经溶液热交换器(11)与第二吸收器(5)连通，第二吸收器(5)还有稀溶液管路经溶液泵(9)和第二溶液热交换器(12)与发生器(1)连通，发生器(1)还有浓溶液管路经第二溶液热交换器(12)与第二发生器(2)连通，第二发生器(2)还有浓溶液管路与第三发生器(3)连通，第三发生器(3)还有浓溶液管路经第二溶液泵(10)和溶液热交换器(11)与吸收器(4)连通，发生器(1)还有冷剂蒸汽通道与冷凝器(6)连通，冷凝器(6)还有冷剂液管路与第三发生器(3)连通之后第三发生器(3)再有冷剂液管路经节流阀(8)与蒸发器(7)连通，第二发生器(2)和第三发生器(3)还分别有冷剂蒸汽通道与第二吸收器(5)连通，蒸发器(7)还有冷剂蒸汽通道与吸收器(4)连通，发生器(1)还有驱动热介质管路与外部连通，吸收器(4)和冷凝器(6)还分别有被加热介质管路与外部连通，第二发生器(2)和蒸发器(7)还分别有余热介质管路与外部连通，第二吸收器(5)还有冷却介质管路与外部连通，形成第五类吸收式热泵。
  2. 第五类吸收式热泵，是在权利要求1所述的第五类吸收式热泵中，取消节流阀，将第三发生器(3)有冷剂液管路经节流阀(8)与蒸发器(7)连通调整为第三发生器(3)有冷剂液管路与蒸发器(7)连通，形成第五类吸收式热泵。
  3. 第五类吸收式热泵，是在权利要求1所述的第五类吸收式热泵中，增加第四发生器、第二节流阀、第三溶液泵、第三溶液热交换器和热交换器，第二吸收器(5)增设稀溶液管路经第三溶液泵(15)和第三溶液热交换器(16)与第四发生器(13)连通，第四发生器(13)还有浓溶液管路经第三溶液热交换器(16)与第二发生器(2)连通，将发生器(1)有冷剂蒸汽通道与冷凝器(6)连通调整为发生器(1)有冷剂蒸汽通道与第四发生器(13)连通之后第四发生器(13)再有冷剂液管路经热交换器(17)、第三发生器(3)和第二节流阀(14)与蒸发器(7)连通，第四发生器(13)还有冷剂蒸汽通道与冷凝器(6)连通，热交换器(17)还有被加热介质管路与外部连通，形成第五类吸收式热泵。
  4. 第五类吸收式热泵，是在权利要求1所述的第五类吸收式热泵中，增加第四发生器、第二节流阀、第三溶液热交换器和热交换器，将第二吸收器(5)有稀溶液管路经溶液泵(9)和第二溶液热交换器(12)与发生器(1)连通调整为第二吸收器(5)有稀溶液管路经溶液泵(9)、第二溶液热交换器(12)和第三溶液热交换器(16)与发生器(1)连通，将发生器(1)有浓溶液管路经第二溶液热交换器(12)与第二发生器(2)连通调整为发生器(1)有浓溶液管路经第三溶液热交换器(16)与第四发生器(13)连通，第四发生器(13)再有浓溶液管路经第二溶液热交换器(12)与第二发生器(2)连通，将发生器(1)有冷剂蒸汽通道与冷凝器(6)连通调整为发生器(1)有冷剂蒸汽通道与第四发生器(13)连通之后第四发生器(13)再有冷剂液管路经热交换器(17)、第三发生器(3)和第二节流阀(14)与蒸发器(7)连通，第四发生器(13)还有冷剂蒸汽通道与冷凝器(6)连通，热交换器(17)还有被加热介质管路与外部连通，形成第五类吸收式热泵。
  5. 第五类吸收式热泵，是在权利要求1所述的第五类吸收式热泵中，增加第四发生器、第二节流阀、第三溶液泵、第三溶液热交换器和热交换器，将第二吸收器(5)有稀溶液管路经溶液泵(9)和第二溶液热交换器(12)与发生器(1)连通调整为第二吸收器(5)有 稀溶液管路经溶液泵(9)和第二溶液热交换器(12)与第四发生器(13)连通，第四发生器(13)再有浓溶液管路经第三溶液泵(15)和第三溶液热交换器(16)与发生器(1)连通，将发生器(1)有浓溶液管路经第二溶液热交换器(12)与第二发生器(2)连通调整为发生器(1)有浓溶液管路经第三溶液热交换器(16)和第二溶液热交换器(12)与第二发生器(2)连通，将发生器(1)有冷剂蒸汽通道与冷凝器(6)连通调整为发生器(1)有冷剂蒸汽通道与第四发生器(13)连通之后第四发生器(13)再有冷剂液管路经热交换器(17)、第三发生器(3)和第二节流阀(14)与蒸发器(7)连通，第四发生器(13)还有冷剂蒸汽通道与冷凝器(6)连通，热交换器(17)还有被加热介质管路与外部连通，形成第五类吸收式热泵。
  6. 第五类吸收式热泵，是在权利要求3-5所述的任一第五类吸收式热泵中，取消节流阀和第二节流阀，将第三发生器(3)有冷剂液管路经节流阀(8)与蒸发器(7)连通调整为第三发生器(3)有冷剂液管路与蒸发器(7)连通，将第三发生器(3)有冷剂液管路经第二节流阀(14)与蒸发器(7)连通调整为第三发生器(3)有冷剂液管路与蒸发器(7)连通，形成第五类吸收式热泵。
  7. 第五类吸收式热泵，是在权利要求3所述的第五类吸收式热泵中，增加第五发生器、第三节流阀，第四溶液泵、第四溶液热交换器和第二热交换器，第二吸收器(5)增设稀溶液管路经第四溶液泵(20)和第四溶液热交换器(21)与第五发生器(18)连通，第五发生器(18)还有浓溶液管路经第四溶液热交换器(21)与第二发生器(2)连通，第五发生器(18)还有冷剂蒸汽通道与冷凝器(6)连通，将第四发生器(13)有冷剂蒸汽通道与冷凝器(6)连通调整为第四发生器(13)有冷剂蒸汽通道与第五发生器(18)连通之后第五发生器(18)再有冷剂液管路经第二热交换器(22)、第三发生器(3)和第三节流阀(19)与蒸发器(7)连通，将第四发生器(13)有冷剂液管路经热交换器(17)、第三发生器(3)和第二节流阀(14)与蒸发器(7)连通调整为第四发生器(13)有冷剂液管路经第五发生器(18)、热交换器(17)、第三发生器(3)和第二节流阀(14)与蒸发器(7)连通，第二热交换器(22)还有被加热介质管路与外部连通，形成第五类吸收式热泵。
  8. 第五类吸收式热泵，是在权利要求4所述的第五类吸收式热泵中，增加第五发生器、第三节流阀、第四溶液热交换器和第二热交换器，将第二吸收器(5)有稀溶液管路经溶液泵(9)、第二溶液热交换器(12)和第三溶液热交换器(16)与发生器(1)连通调整为第二吸收器(5)有稀溶液管路经溶液泵(9)、第四溶液热交换器(21)、第二溶液热交换器(12)和第三溶液热交换器(16)与发生器(1)连通，将第四发生器(13)有浓溶液管路经第二溶液热交换器(12)与第二发生器(2)连通调整为第四发生器(13)有浓溶液管路经第二溶液热交换器(12)与第五发生器(18)连通，第五发生器(18)再有浓溶液管路经第四溶液热交换器(21)与第二发生器(2)连通，第五发尘器(18)还有冷剂蒸汽通道与冷凝器(6)连通，将第四发生器(13)有冷剂蒸汽通道与冷凝器(6)连通调整为第四发生器(13)有冷剂蒸汽通道与第五发生器(18)连通之后第五发生器(18)再有冷剂液管路经第二热交换器(22)、第三发生器(3)和第三节流阀(19)与蒸发器(7)连通，将第四发生器(13)有冷剂液管路经热交换器(17)、第三发生器(3)和第二节流阀(14)与蒸发器(7)连通调整为第四发生器(13)有冷剂液管路经第五发生器(18)、热交换器 (17)、第三发生器(3)和第二节流阀(14)与蒸发器(7)连通，第二热交换器(22)还有被加热介质管路与外部连通，形成第五类吸收式热泵。
  9. 第五类吸收式热泵，是在权利要求5所述的第五类吸收式热泵中，增加第五发生器、第三节流阀，第四溶液泵、第四溶液热交换器和第二热交换器，将第二吸收器(5)有稀溶液管路经溶液泵(9)和第二溶液热交换器(12)与第四发生器(13)连通调整为第二吸收器(5)有稀溶液管路经溶液泵(9)和第二溶液热交换器(12)与第五发生器(18)连通，第五发生器(18)再有浓溶液管路经第四溶液泵(20)和第四溶液热交换器(21)与第四发生器(13)连通，将发生器(1)有浓溶液管路经第三溶液热交换器(16)和第二溶液热交换器(12)与第二发生器(2)连通调整为发生器(l)有浓溶液管路经第三溶液热交换器(16)、第四溶液热交换器(21)和第二溶液热交换器(12)与第二发生器(2)连通，第五发生器(18)还有冷剂蒸汽通道与冷凝器(6)连通，将第四发生器(13)有冷剂蒸汽通道与冷凝器(6)连通调整为第四发生器(13)有冷剂蒸汽通道与第五发生器(18)连通之后第五发生器(18)再有冷剂液管路经第二热交换器(22)、第三发生器(3)和第三节流阀(19)与蒸发器(7)连通，将第四发生器(13)有冷剂液管路经热交换器(17)、第三发生器(3)和第二节流阀(14)与蒸发器(7)连通调整为第四发生器(13)有冷剂液管路经第五发生器(18)、热交换器(17)、第三发生器(3)和第二节流阀(14)与蒸发器(7)连通，第二热交换器(22)还有被加热介质管路与外部连通，形成第五类吸收式热泵。
  10. 第五类吸收式热泵，是在权利要求7-9所述的任一第五类吸收式热泵中，取消节流阀、第二节流阀和第三节流阀，将第三发生器(3)有冷剂液管路经节流阀(8)与蒸发器(7)连通调整为第三发生器(3)有冷剂液管路与蒸发器(7)连通，将第三发生器(3)有冷剂液管路经第二节流阀(14)与蒸发器(7)连通调整为第三发生器(3)有冷剂液管路与蒸发器(7)连通，将第三发生器(3)有冷剂液管路经第三节流阀(19)与蒸发器(7)连通调整为第三发生器(3)有冷剂液管路与蒸发器(7)连通，形成第五类吸收式热泵。
  11. 第五类吸收式热泵，主要由发生器、第二发生器、第三发生器、吸收器、第二吸收器、冷凝器、蒸发器、节流阀、溶液泵、第二溶液泵、溶液热交换器、第二溶液热交换器、第四发生器、第三溶液泵、第三溶液热交换器和第三吸收器所组成；吸收器(4)有稀溶液管路经溶液热交换器(11)与第二吸收器(5)连通，第二吸收器(5)还有稀溶液管路经溶液泵(9)和第二溶液热交换器(12)与第三吸收器(23)连通，第三吸收器(23)还有稀溶液管路经第三溶液泵(15)和第三溶液热交换器(16)与发生器(1)连通，发生器(1)还有浓溶液管路经第三溶液热交换器(16)与第四发生器(13)连通，第四发生器(13)还有浓溶液管路经第二溶液热交换器(12)与第二发生器(2)连通，第二发生器(2)还有浓溶液管路与第三发生器(3)连通，第三发生器(3)还有浓溶液管路经第二溶液泵(10)和溶液热交换器(11)与吸收器(4)连通，发生器(1)还有冷剂蒸汽通道与冷凝器(6)连通，冷凝器(6)还有冷剂液管路与第三发生器(3)连通之后第三发生器(3)再有冷剂液管路经节流阀(8)与蒸发器(7)连通，第二发生器(2)和第三发生器(3)还分别有冷剂蒸汽通道与第二吸收器(5)连通，第四发生器(13)还有冷剂蒸汽通道与第三吸收器(23)连通，蒸发器(7)还有冷剂蒸汽通道与吸收器(4)连通，发生器(1)和第四发生器(13)还分别有驱动热介质管路与外部连通，吸收器(4)、冷凝器(6)和第三 吸收器(23)还分别有被加热介质管路与外部连通，第二发生器(2)和蒸发器(7)还分别有余热介质管路与外部连通，第二吸收器(5)还有冷却介质管路与外部连通，形成第五类吸收式热泵。
  12. 第五类吸收式热泵，是在权利要求11所述的第五类吸收式热泵中，取消节流阀，将第三发生器(3)有冷剂液管路经节流阀(8)与蒸发器(7)连通调整为第三发生器(3)有冷剂液管路与蒸发器(7)连通，形成第五类吸收式热泵。
  13. 第五类吸收式热泵，是在权利要求11所述的第五类吸收式热泵中，增加第五发生器、第二节流阀、第四溶液泵、第四溶液热交换器和热交换器，第三吸收器(23)增设稀溶液管路经第四溶液泵(20)和第四溶液热交换器(21)与第五发生器(18)连通，第五发生器(18)还有浓溶液管路经第四溶液热交换器(21)与第四发生器(13)连通，将发生器(1)有冷剂蒸汽通道与冷凝器(6)连通调整为发生器(1)有冷剂蒸汽通道与第五发生器(18)连通之后第五发生器(18)再有冷剂液管路经热交换器(17)、第三发生器(3)和第二节流阀(14)与蒸发器(7)连通，第五发生器(18)还有冷剂蒸汽通道与冷凝器(6)连通，热交换器(17)还有被加热介质管路与外部连通，形成第五类吸收式热泵。
  14. 第五类吸收式热泵，是在权利要求11所述的第五类吸收式热泵中，增加第五发生器、第二节流阀、第四溶液热交换器和热交换器，将第三吸收器(23)有稀溶液管路经第三溶液泵(15)和第三溶液热交换器(16)与发生器(1)连通调整为第三吸收器(23)有稀溶液管路经第三溶液泵(15)、第三溶液热交换器(16)和第四溶液热交换器(21)与发尘器(1)连通，将发生器(1)有浓溶液管路经第三溶液热交换器(16)与第四发生器(13)连通调整为发生器(1)有浓溶液管路经第四溶液热交换器(21)与第五发生器(18)连通，第五发生器(18)再有浓溶液管路经第三溶液热交换器(16)与第四发生器(13)连通，将发生器(1)有冷剂蒸汽通道与冷凝器(6)连通调整为发生器(1)有冷剂蒸汽通道与第五发生器(18)连通之后第五发生器(18)再有冷剂液管路经热交换器(17)、第三发生器(3)和第二节流阀(14)与蒸发器(7)连通，第五发生器(18)还有冷剂蒸汽通道与冷凝器(6)连通，热交换器(17)还有被加热介质管路与外部连通，形成第五类吸收式热泵。
  15. 第五类吸收式热泵，是在权利要求11所述的第五类吸收式热泵中，增加第五发生器、第二节流阀、第四溶液泵、第四溶液热交换器和热交换器，将第三吸收器(23)有稀溶液管路经第三溶液泵(15)和第三溶液热交换器(16)与发生器(1)连通调整为第三吸收器(23)有稀溶液管路经第三溶液泵(15)和第三溶液热交换器(16)与第五发生器(18)连通，第五发生器(18)再有浓溶液管路经第四溶液泵(20)和第四溶液热交换器(21)与发生器(1)连通，将发生器(1)有浓溶液管路经第三溶液热交换器(16)与第四发生器(13)连通调整为发生器(1)有浓溶液管路经第四溶液热交换器(21)和第三溶液热交换器(16)与第四发生器(13)连通，将发生器(1)有冷剂蒸汽通道与冷凝器(6)连通调整为发生器(1)有冷剂蒸汽通道与第五发生器(18)连通之后第五发生器(18)再有冷剂液管路经热交换器(17)、第三发生器(3)和第二节流阀(14)与蒸发器(7)连通，第五发生器(18)还有冷剂蒸汽通道与冷凝器(6)连通，热交换器(17)还有被加热介质管路与外部连通，形成第五类吸收式热泵。
  16. 第五类吸收式热泵，是在权利要求13-15所述的任一第五类吸收式热泵中，第五 发生器(18)增设驱动热介质管路与外部连通，形成第五类吸收式热泵。
  17. 第五类吸收式热泵，是在权利要求13-16所述的任一第五类吸收式热泵中，取消节流阀和第二节流阀，将第三发生器(3)有冷剂液管路经节流阀(8)与蒸发器(7)连通调整为第三发生器(3)有冷剂液管路与蒸发器(7)连通，将第三发生器(3)有冷剂液管路经第二节流阀(14)与蒸发器(7)连通调整为第三发生器(3)有冷剂液管路与蒸发器(7)连通，形成第五类吸收式热泵。
  18. 第五类吸收式热泵，是在权利要求1或权利要求11所述的第五类吸收式热泵中，增加新增发生器、新增吸收器、新增溶液泵和新增溶液热交换器，将吸收器(4)有稀溶液管路经溶液热交换器(11)与第二吸收器(5)连通调整为吸收器(4)有稀溶液管路经新增溶液热交换器(D)与新增吸收器(B)连通，新增吸收器(B)再有稀溶液管路经新增溶液泵(C)和溶液热交换器(11)与第二吸收器(5)连通，将第三发生器(3)有浓溶液管路经第二溶液泵(10)和溶液热交换器(11)与吸收器(4)连通调整为第三发生器(3)有浓溶液管路经溶液热交换器(11)与新增发生器(A)连通，新增发生器(A)再有浓溶液管路经第二溶液泵(10)和新增溶液热交换器(D)与吸收器(4)连通，新增发生器(A)还有冷剂蒸汽通道与新增吸收器(B)连通，将第三发生器(3)有冷剂液管路经节流阀(8)与蒸发器(7)连通调整为第三发生器(3)有冷剂液管路与新增发生器(A)连通之后新增发生器(A)再有冷剂液管路经节流阀(8)与蒸发器(7)连通，新增吸收器(B)还有冷却介质管路与外部连通，形成第五类吸收式热泵。
  19. 第五类吸收式热泵，是在权利要求18所述的任一第五类吸收式热泵中，取消节流阀，将新增发生器(A)有冷剂液管路经节流阀(8)与蒸发器(7)连通调整为新增发生器(A)有冷剂液管路与蒸发器(7)连通，形成第五类吸收式热泵。
  20. 第五类吸收式热泵，是在权利要求3-5、13-16所述的任一第五类吸收式热泵中，增加新增发生器、新增吸收器、新增溶液泵和新增溶液热交换器，将吸收器(4)有稀溶液管路经溶液热交换器(11)与第二吸收器(5)连通调整为吸收器(4)有稀溶液管路经新增溶液热交换器(D)与新增吸收器(B)连通，新增吸收器(B)再有稀溶液管路经新增溶液泵(C)和溶液热交换器(11)与第二吸收器(5)连通，将第三发生器(3)有浓溶液管路经第二溶液泵(10)和溶液热交换器(11)与吸收器(4)连通调整为第三发生器(3)有浓溶液管路经溶液热交换器(11)与新增发生器(A)连通，新增发生器(A)再有浓溶液管路经第二溶液泵(1O)和新增溶液热交换器(D)与吸收器(4)连通，新增发生器(A)还有冷剂蒸汽通道与新增吸收器(B)连通，将第三发生器(3)有冷剂液管路经节流阀(8)与蒸发器(7)连通调整为第三发生器(3)有冷剂液管路与新增发生器(A)连通之后新增发生器(A)再有冷剂液管路经节流阀(8)与蒸发器(7)连通，将第三发生器(3)有冷剂液管路经第二节流阀(14)与蒸发器(7)连通调整为第三发生器(3)有冷剂液管路与新增发生器(A)连通之后新增发生器(A)再有冷剂液管路经第二节流阀(14)与蒸发器(7)连通，新增吸收器(B)还有冷却介质管路与外部连通，形成第五类吸收式热泵。
  21. 第五类吸收式热泵，是在权利要求20所述的任一第五类吸收式热泵中，取消节流阀和第二节流阀，将新增发生器(A)有冷剂液管路经节流阀(8)与蒸发器(7)连通调整为新增发生器(A)有冷剂液管路与蒸发器(7)连通，将新增发生器(A)有冷剂液管路经 第二节流阀(14)与蒸发器(7)连通调整为新增发生器(A)有冷剂液管路与蒸发器(7)连通，形成第五类吸收式热泵。
  22. 第五类吸收式热泵，是在权利要求7-9所述的任一第五类吸收式热泵中，增加新增发生器、新增吸收器、新增溶液泵和新增溶液热交换器，将吸收器(4)有稀溶液管路经溶液热交换器(11)与第二吸收器(5)连通调整为吸收器(4)有稀溶液管路经新增溶液热交换器(D)与新增吸收器(B)连通，新增吸收器(B)再有稀溶液管路经新增溶液泵(C)和溶液热交换器(11)与第二吸收器(5)连通，将第三发生器(3)有浓溶液管路经第二溶液泵(10)和溶液热交换器(11)与吸收器(4)连通调整为第三发生器(3)有浓溶液管路经溶液热交换器(11)与新增发生器(A)连通，新增发生器(A)再有浓溶液管路经第二溶液泵(1O)和新增溶液热交换器(D)与吸收器(4)连通，新增发生器(A)还有冷剂蒸汽通道与新增吸收器(B)连通，将第三发生器(3)有冷剂液管路经节流阀(8)与蒸发器(7)连通调整为第三发生器(3)有冷剂液管路与新增发生器(A)连通之后新增发生器(A)再有冷剂液管路经节流阀(8)与蒸发器(7)连通，将第三发生器(3)有冷剂液管路经第二节流阀(14)与蒸发器(7)连通调整为第三发生器(3)有冷剂液管路与新增发生器(A)连通之后新增发生器(A)再有冷剂液管路经第二节流阀(14)与蒸发器(7)连通，将第三发生器(3)有冷剂液管路经第三节流阀(19)与蒸发器(7)连通调整为第三发生器(3)有冷剂液管路与新增发生器(A)连通之后新增发生器(A)再有冷剂液管路经第三节流阀(19)与蒸发器(7)连通，新增吸收器(B)还有冷却介质管路与外部连通，形成第五类吸收式热泵。
  23. 第五类吸收式热泵，是在权利要求22所述的任一第五类吸收式热泵中，取消节流阀、第二节流阀和第三节流阀，将新增发生器(A)有冷剂液管路经节流阀(8)与蒸发器(7)连通调整为新增发生器(A)有冷剂液管路与蒸发器(7)连通，将新增发生器(A)有冷剂液管路经第二节流阀(14)与蒸发器(7)连通调整为新增发生器(A)有冷剂液管路与蒸发器(7)连通，将新增发生器(A)有冷剂液管路经第三节流阀(19)与蒸发器(7)连通调整为新增发生器(A)有冷剂液管路与蒸发器(7)连通，形成第五类吸收式热泵。
  24. 第五类吸收式热泵，是在权利要求l或权利要求11所述的第五类吸收式热泵中，增加新增发生器、新增吸收器、新增溶液泵和新增溶液热交换器，将吸收器(4)有稀溶液管路经溶液热交换器(11)与第二吸收器(5)连通调整为吸收器(4)有稀溶液管路经新增溶液热交换器(D)与新增吸收器(B)连通，新增吸收器(B)再有稀溶液管路经新增溶液泵(C)和溶液热交换器(11)与第二吸收器(5)连通，将第三发生器(3)有浓溶液管路经第二溶液泵(10)和溶液热交换器(11)与吸收器(4)连通调整为第三发生器(3)有浓溶液管路经溶液热交换器(11)与新增发生器(A)连通，新增发生器(A)再有浓溶液管路经第二溶液泵(10)和新增溶液热交换器(D)与吸收器(4)连通，新增发生器(A)还有冷剂蒸汽通道与新增吸收器(B)连通，新增发生器(A)还有余热介质管路与外部连通，新增吸收器(B)还有冷却介质管路与外部连通，形成第五类吸收式热泵。
  25. 第五类吸收式热泵，是在权利要求24所述的任一第五类吸收式热泵中，取消节流阀，将第三发生器(3)有冷剂液管路经节流阀(8)与蒸发器(7)连通调整为第三发生器(3)有冷剂液管路与蒸发器(7)连通，形成第五类吸收式热泵。
  26. 第五类吸收式热泵，是在权利要求3-5、13-16所述的任一第五类吸收式热泵中，增加新增发生器、新增吸收器、新增溶液泵和新增溶液热交换器，将吸收器(4)有稀溶液管路经溶液热交换器(11)与第二吸收器(5)连通调整为吸收器(4)有稀溶液管路经新增溶液热交换器(D)与新增吸收器(B)连通，新增吸收器(B)再有稀溶液管路经新增溶液泵(C)和溶液热交换器(11)与第二吸收器(5)连通，将第三发生器(3)有浓溶液管路经第二溶液泵(10)和溶液热交换器(11)与吸收器(4)连通调整为第三发生器(3)有浓溶液管路经溶液热交换器(11)与新增发生器(A)连通，新增发生器(A)再有浓溶液管路经第二溶液泵(10)和新增溶液热交换器(D)与吸收器(4)连通，新增发生器(A)还有冷剂蒸汽通道与新增吸收器(B)连通，新增发生器(A)还有余热介质管路与外部连通，新增吸收器(B)还有冷却介质管路与外部连通，形成第五类吸收式热泵。
  27. 第五类吸收式热泵，是在权利要求26所述的任一第五类吸收式热泵中，取消节流阀和第二节流阀，将第三发生器(3)有冷剂液管路经节流阀(8)与蒸发器(7)连通调整为第三发生器(3)有冷剂液管路与蒸发器(7)连通，将第三发生器(3)有冷剂液管路经第二节流阀(14)与蒸发器(7)连通调整为第三发尘器(3)有冷剂液管路与蒸发器(7)连通，形成第五类吸收式热泵。
  28. 第五类吸收式热泵，是在权利要求7-9所述的任一第五类吸收式热泵中，增加新增发生器、新增吸收器、新增溶液泵和新增溶液热交换器，将吸收器(4)有稀溶液管路经溶液热交换器(11)与第二吸收器(5)连通调整为吸收器(4)有稀溶液管路经新增溶液热交换器(D)与新增吸收器(B)连通，新增吸收器(B)再有稀溶液管路经新增溶液泵(C)和溶液热交换器(11)与第二吸收器(5)连通，将第三发生器(3)有浓溶液管路经第二溶液泵(10)和溶液热交换器(11)与吸收器(4)连通调整为第三发生器(3)有浓溶液管路经溶液热交换器(11)与新增发生器(A)连通，新增发生器(A)再有浓溶液管路经第二溶液泵(10)和新增溶液热交换器(D)与吸收器(4)连通，新增发生器(A)还有冷剂蒸汽通道与新增吸收器(B)连通，新增发生器(A)还有余热介质管路与外部连通，新增吸收器(B)还有冷却介质管路与外部连通，形成第五类吸收式热泵。
  29. 第五类吸收式热泵，是在权利要求28所述的任一第五类吸收式热泵中，取消节流阀、第二节流阀和第三节流阀，将第三发生器(3)有冷剂液管路经节流阀(8)与蒸发器(7)连通调整为第三发生器(3)有冷剂液管路与蒸发器(7)连通，将第三发生器(3)有冷剂液管路经第二节流阀(14)与蒸发器(7)连通调整为第三发生器(3)有冷剂液管路与蒸发器(7)连通，将第三发生器(3)有冷剂液管路经第三节流阀(19)与蒸发器(7)连通调整为第三发生器(3)有冷剂液管路与蒸发器(7)连通，形成第五类吸收式热泵。
  30. 第五类吸收式热泵，是在权利要求1-17所述的任一第五类吸收式热泵中，增加新增发生器、新增吸收器、新增溶液泵和新增溶液热交换器，将蒸发器(7)有冷剂蒸汽通道与吸收器(4)连通调整为蒸发器(7)有冷剂蒸汽通道与新增吸收器(B)连通，新增吸收器(B)还有稀溶液管路经新增溶液泵(C)和新增溶液热交换器(D)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(D)与新增吸收器(B)连通，新增发生器(A)还有冷剂蒸汽通道与吸收器(4)连通，新增发生器(A)还有驱动热介质管路与外部连通，新增吸收器(B)还有被加热介质管路与外部连通，形成第五类吸收式热泵。
  31. 第五类吸收式热泵，是在权利要求18-29所述的任一第五类吸收式热泵中，增加新增第二发生器、新增第二吸收器、新增第二溶液泵和新增第二溶液热交换器，将蒸发器(7)有冷剂蒸汽通道与吸收器(4)连通调整为蒸发器(7)有冷剂蒸汽通道与新增第二吸收器连通，新增第二吸收器还有稀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新增第二吸收器连通，新增第二发生器还有冷剂蒸汽通道与吸收器(4)连通，新增第二发生器还有驱动热介质管路与外部连通，新增第二吸收器还有被加热介质管路与外部连通，形成第五类吸收式热泵。
  32. 第五类吸收式热泵，是在权利要求1-2、11-12所述的任一第五类吸收式热泵中，增加新增发生器、新增吸收器、新增溶液泵和新增溶液热交换器，将发生器(1)有冷剂蒸汽通道与冷凝器(6)连通调整为发生器(1)有冷剂蒸汽通道与新增吸收器(B)连通，新增吸收器(B)还有稀溶液管路经新增溶液泵(C)和新增溶液热交换器(D)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(D)与新增吸收器(B)连通，新增发生器(A)还有冷剂蒸汽通道与冷凝器(6)连通，新增发生器(A)还有驱动热介质管路与外部连通，新增吸收器(B)还有被加热介质管路与外部连通，形成第五类吸收式热泵。
  33. 第五类吸收式热泵，是在权利要求18-19、24-25所述的任一第五类吸收式热泵中，增加新增第二发生器、新增第二吸收器、新增第二溶液泵和新增第二溶液热交换器，将发生器(1)有冷剂蒸汽通道与冷凝器(6)连通调整为发生器(1)有冷剂蒸汽通道与新增第二吸收器连通，新增第二吸收器还有稀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新增第二吸收器连通，新增第二发生器还有冷剂蒸汽通道与冷凝器(6)连通，新增第二发生器还有驱动热介质管路与外部连通，新增第二吸收器还有被加热介质管路与外部连通，形成第五类吸收式热泵。
  34. 第五类吸收式热泵，是在权利要求1-17所述的任一第五类吸收式热泵中，第三发生器(3)增设余热介质管路与外部连通，形成第五类吸收式热泵。
  35. 第五类吸收式热泵，是在权利要求24-29所述的任一第五类吸收式热泵中，第三发生器(3)增设余热介质管路与外部连通，形成第五类吸收式热泵。
  36. 第五类吸收式热泵，是在权利要求18-23所述的任一第五类吸收式热泵中，第三发生器(3)和新增发生器(A)分别增设余热介质管路与外部连通，形成第五类吸收式热泵。
  37. 第五类吸收式热泵，是在权利要求18-23所述的任一第五类吸收式热泵中，第三发生器(3)或新增发生器(A)增设余热介质管路与外部连通，形成第五类吸收式热泵。
  38. 第五类吸收式热泵，是在权利要求34所述的任一第五类吸收式热泵中，增加新增发生器、新增吸收器、新增溶液泵和新增溶液热交换器，将蒸发器(7)有冷剂蒸汽通道与吸收器(4)连通调整为蒸发器(7)有冷剂蒸汽通道与新增吸收器(B)连通，新增吸收器(B)还有稀溶液管路经新增溶液泵(C)和新增溶液热交换器(D)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(D)与新增吸收器(B)连通，新增发生器(A)还有冷剂蒸汽通道与吸收器(4)连通，新增发生器(A)还有驱动热介质管 路与外部连通，新增吸收器(B)还有被加热介质管路与外部连通，形成第五类吸收式热泵。
  39. 第五类吸收式热泵，是在权利要求35-37所述的任一第五类吸收式热泵中，增加新增第二发生器、新增第二吸收器、新增第二溶液泵和新增第二溶液热交换器，将蒸发器(7)有冷剂蒸汽通道与吸收器(4)连通调整为蒸发器(7)有冷剂蒸汽通道与新增第二吸收器连通，新增第二吸收器还有稀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新增第二吸收器连通，新增第二发生器还有冷剂蒸汽通道与吸收器(4)连通，新增第二发生器还有驱动热介质管路与外部连通，新增第二吸收器还有被加热介质管路与外部连通，形成第五类吸收式热泵。
  40. 第五类吸收式热泵，是在权利要求1-17所述的任一第五类吸收式热泵中，增加新增发生器、新增吸收器、新增溶液泵和新增溶液热交换器，将第二发生器(2)有冷剂蒸汽通道与第二吸收器(5)连通调整为第二发生器(2)有冷剂蒸汽通道与新增吸收器(B)连通，将第三发生器(3)有冷剂蒸汽通道与第二吸收器(5)连通调整为第三发生器(3)有冷剂蒸汽通道与新增吸收器(B)连通，新增吸收器(B)还有稀溶液管路经新增溶液泵(C)和新增溶液热交换器(D)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(D)与新增吸收器(B)连通，新增发生器(A)还有冷剂蒸汽通道与第二吸收器(5)连通，新增发生器(A)还有余热介质管路与外部连通，新增吸收器(B)还有冷却介质管路与外部连通，形成第五类吸收式热泵。
  41. 第五类吸收式热泵，是在权利要求40所述的任一第五类吸收式热泵中，第三发生器(3)增设余热介质管路与外部连通，形成第五类吸收式热泵。
  42. 第五类吸收式热泵，是在权利要求18-23所述的任一第五类吸收式热泵中，增加新增第二发生器、新增第二吸收器、新增第二溶液泵和新增第二溶液热交换器，将新增发生器(A)有冷剂蒸汽通道与新增吸收器(B)连通调整为新增发生器(A)有冷剂蒸汽通道与新增第二吸收器连通，新增第二吸收器还有稀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新增第二吸收器连通，新增第二发生器还有冷剂蒸汽通道与新增吸收器(B)连通，新增第二发生器还有余热介质管路与外部连通，新增第二吸收器还有冷却介质管路与外部连通，形成第五类吸收式热泵。
  43. 第五类吸收式热泵，是在权利要求42所述的任一第五类吸收式热泵中，第三发生器(3)和新增发生器(A)分别增设余热介质管路与外部连通，形成第五类吸收式热泵。
  44. 第五类吸收式热泵，是在权利要求42所述的任一第五类吸收式热泵中，第三发生器(3)或新增发生器(A)增设余热介质管路与外部连通，形成第五类吸收式热泵。
  45. 第五类吸收式热泵，是在权利要求24-29所述的任一第五类吸收式热泵中，增加新增第二发生器、新增第二吸收器、新增第二溶液泵和新增第二溶液热交换器，将新增发生器(A)有冷剂蒸汽通道与新增吸收器(B)连通调整为新增发生器(A)有冷剂蒸汽通道与新增第二吸收器连通，新增第二吸收器还有稀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新增第二吸收器连通，新增第二发生器还有冷剂蒸汽通道与新增吸收器(B)连通， 新增第二发生器还有余热介质管路与外部连通，新增第二吸收器还有冷却介质管路与外部连通，形成第五类吸收式热泵。
  46. 第五类吸收式热泵，是在权利要求45所述的任一第五类吸收式热泵中，第三发生器(3)增设余热介质管路与外部连通，形成第五类吸收式热泵。
  47. 第五类吸收式热泵，是在权利要求1-2、11-12、24-25所述的任一第五类吸收式热泵中，将第二发生器(2)有余热介质管路与外部连通调整为第三发生器(3)有余热介质管路与外部连通，将冷凝器(6)有冷剂液管路与第三发生器(3)连通之后第三发生器(3)再有冷剂液管路经节流阀(8)与蒸发器(7)连通调整为冷凝器(6)有冷剂液管路与第二发生器(2)连通之后第二发生器(2)再有冷剂液管路经节流阀(8)与蒸发器(7)连通，形成第五类吸收式热泵。
PCT/CN2015/000204 2014-03-27 2015-03-25 第五类吸收式热泵 WO2015143927A1 (zh)

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