CN104807239B - 4th class absorption heat pump and the 5th class absorption heat pump - Google Patents

4th class absorption heat pump and the 5th class absorption heat pump Download PDF

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Publication number
CN104807239B
CN104807239B CN201510144105.9A CN201510144105A CN104807239B CN 104807239 B CN104807239 B CN 104807239B CN 201510144105 A CN201510144105 A CN 201510144105A CN 104807239 B CN104807239 B CN 104807239B
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generator
newly
solution
increased
absorber
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CN104807239A (en
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李华玉
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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

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Sorption Type Refrigeration Machines (AREA)

Abstract

The present invention provides the four, the 5th class absorption heat pumps, belongs to UTILIZATION OF VESIDUAL HEAT IN and technical field of heat pumps.Absorber connects the second absorber through solution heat exchanger, second absorber connects generator through solution pump with the second solution heat exchanger, generator connects the second generator through the second solution heat exchanger, second generator connects absorber through the second solution pump with solution heat exchanger, generator has refrigerant steam channel to connect condenser, second generator has refrigerant steam channel to connect the second absorber, condenser is connected through the second generator and throttle valve with evaporator, evaporator has refrigerant steam channel to connect absorber, generator has driving heat medium pipeline connection outside, absorber and condenser have outside heated medium pipeline connection, evaporator is had a surplus outside heat medium pipeline connection, second absorber has cooling medium pipeline connection outside, form the 4th class absorption heat pump；Second generator is added waste heat medium pipeline and is connected with outside, forms the 5th class absorption heat pump.

Description

4th class absorption heat pump and the 5th class absorption heat pump
Technical field：
The invention belongs to absorption heat pump and technical field of waste heat utilization.
Background technology：
In absorption type heat pump technical field, there is between high temperature driven thermal medium and heated medium the temperature difference respectively as driving The first-class absorption type heat pump (Absorption Refrigerator) of the temperature difference, the temperature difference is drive between waste heat medium and cold environment (cooling medium) The second-kind absorption-type heat pump of dynamic temperature difference, and the 3rd class absorption heat pump using foregoing two kinds of temperature difference as the driving temperature difference at the same time. According to existing understanding or viewpoint, in the absorption heat pump of these three types, high temperature driven thermic load is discharged into the (cooling of cold environment Medium) in, the driving temperature difference of the temperature difference as absorption heat pump is using between high temperature driven thermal medium and cold environment (cooling medium) Unreasonable；Same reason, high temperature driven heat are cooled under heated medium temperature, and make this temperature drop as absorption The driving temperature difference of heat pump is also mysterious.
In the first-class absorption type heat pump and the 3rd class absorption heat pump that high warm load is provided, those skilled in the art Encounter such technical barrier：Using TFE-TDE pyrosols as in the absorption heat pump flow of representative, high-temperature generator discharges Refrigerant vapour and within the condenser heat release form cryogen liquid after heated medium；Refrigerant vapour latent heat is small, and cryogen liquid temperature Degree is high, and sensible heat is relatively large, this causes, and the performance index of absorption heat pump is very low, and heat utilization rate is not high so that the first kind is inhaled Receipts formula heat pump and the 3rd class absorption heat pump are subject to pole in high-temperature heat supply field or the application freezed using high warm load Big limitation.
Inventor recognizes the above problem, and have developed the technology new departure to solve the above problems, has comprising with height Two kinds of temperature drops of warm load are the 4th class absorption heat pump and the 5th class absorption heat pump of the driving temperature difference；The present invention provides utilization Second generator and the second absorber realize the 4th class absorption heat pump of more moneys and the 5th class based on the difference utilization of cryogen liquid temperature Absorption heat pump.
The content of the invention：
Present invention is primarily intended to provide the 4th class absorption heat pump and the 5th class absorption heat pump, the specific content of the invention Subitem is described below：
1. the 4th class absorption heat pump, mainly by generator, the second generator, absorber, the second absorber, condenser, Evaporator, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger are formed；Absorber has Weak solution pipeline is connected through solution heat exchanger with the second absorber, and the second absorber also has weak solution pipeline through solution pump and Two solution heat exchangers are connected with generator, and generator also has concentrated solution pipeline through the second solution heat exchanger and the second generator Connection, the second generator also have concentrated solution pipeline to be connected through the second solution pump and solution heat exchanger with absorber, and generator is also There is refrigerant steam channel to be connected with condenser, the second generator also has refrigerant steam channel to be connected with the second absorber, condenser The second generator has cryogen liquid pipeline to connect through throttle valve and evaporator again after also cryogen liquid pipeline is connected with the second generator Logical, evaporator also has refrigerant steam channel to be connected with absorber, and generator, which also has, drives heat medium pipeline to be connected with outside, absorbs Device and condenser also have heated medium pipeline connect with outside respectively, and the evaporator medium pipeline that also has surplus heat is connected with exterior, Second absorber also has cooling medium pipeline to be connected with outside, forms the 4th class absorption heat pump.
2. the 4th class absorption heat pump, it is in the 4th class absorption heat pump described in the 1st, cancels throttle valve, by the Two generators have cryogen liquid pipeline to connect with evaporator through throttle valve to be adjusted to the second generator and have cryogen liquid pipeline and evaporator Connection, forms the 4th class absorption heat pump.
3. the 4th class absorption heat pump, be in the 4th class absorption heat pump described in the 1st, the 3rd generator of increase, Second throttle, the 3rd solution pump, the 3rd solution heat exchanger and heat exchanger, the second absorber add weak solution pipeline through Three solution pumps and the 3rd solution heat exchanger are connected with the 3rd generator, and the 3rd generator also has concentrated solution pipeline through the 3rd solution Heat exchanger is connected with the second generator, is had refrigerant steam channel to connect with condenser in generator and is adjusted to generator and has cryogen The 3rd generator has cryogen liquid pipeline through heat exchanger, the second generator and again after steam channel is connected with the 3rd generator Two throttle valves are connected with evaporator, and the 3rd generator also has refrigerant steam channel to be connected with condenser, and heat exchanger, which also has, to be added Heat medium pipeline is connected with outside, forms the 4th class absorption heat pump.
4. the 4th class absorption heat pump, be in the 4th class absorption heat pump described in the 1st, the 3rd generator of increase, Second throttle, the 3rd solution heat exchanger and heat exchanger, have weak solution pipeline through solution pump and second by the second absorber Solution heat exchanger is connected with generator to be adjusted to the second absorber and has weak solution pipeline through solution pump, the second solution heat exchanger Connected with the 3rd solution heat exchanger with generator, there is concentrated solution pipeline to be sent out through the second solution heat exchanger and second in generator Raw device connection, which is adjusted to generator, has concentrated solution pipeline to be connected through the 3rd solution heat exchanger with the 3rd generator, the 3rd generator There is concentrated solution pipeline to be connected through the second solution heat exchanger with the second generator again, generator is had into refrigerant steam channel and condensation Device connection be adjusted to generator have refrigerant steam channel connected with the 3rd generator after the 3rd generator have cryogen liquid pipeline again Connected through heat exchanger, the second generator and second throttle with evaporator, the 3rd generator also have refrigerant steam channel with it is cold Condenser connects, and heat exchanger also has heated medium pipeline to be connected with outside, forms the 4th class absorption heat pump.
5. the 4th class absorption heat pump, be in the 4th class absorption heat pump described in the 1st, the 3rd generator of increase, Second throttle, the 3rd solution pump, the 3rd solution heat exchanger and heat exchanger, have weak solution pipeline through molten by the second absorber Liquid pump and the second solution heat exchanger are connected with generator to be adjusted to the second absorber and has weak solution pipeline through solution pump and second Solution heat exchanger is connected with the 3rd generator, and the 3rd generator has concentrated solution pipeline through the 3rd solution pump and the 3rd solution heat again Exchanger is connected with generator, has concentrated solution pipeline to connect adjustment with the second generator through the second solution heat exchanger in generator There is concentrated solution pipeline to be connected through the 3rd solution heat exchanger and the second solution heat exchanger with the second generator for generator, will send out Raw device has refrigerant steam channel to connect with condenser to be adjusted to generator and have after refrigerant steam channel connects with the 3rd generator 3rd generator has cryogen liquid pipeline to be connected through heat exchanger, the second generator and second throttle with evaporator again, the 3rd hair Raw device also has refrigerant steam channel connect with condenser, and heat exchanger also has heated medium pipeline to be connected with exterior, formation the Four class absorption heat pumps.
6. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in 3-5, cancels throttle valve And second throttle, by the second generator have cryogen liquid pipeline connected with evaporator through throttle valve be adjusted to the second generator have it is cold Agent liquid pipeline is connected with evaporator, is had cryogen liquid pipeline to be connected through second throttle with evaporator in the second generator and is adjusted to Two generators have cryogen liquid pipeline to be connected with evaporator, form the 4th class absorption heat pump.
7. the 4th class absorption heat pump, be in the 4th class absorption heat pump described in the 3rd, the 4th generator of increase, 3rd throttle valve, the 4th solution pump, the 4th solution heat exchanger and second heat exchanger, the second absorber add weak solution pipeline Connected through the 4th solution pump and the 4th solution heat exchanger with the 4th generator, the 4th generator also has concentrated solution pipeline through the 4th Solution heat exchanger is connected with the second generator, and the 4th generator also has refrigerant steam channel to be connected with condenser, by the 3rd hair Raw device has refrigerant steam channel to connect with condenser to be adjusted to the 3rd generator and have refrigerant steam channel to connect with the 4th generator The 4th generator has cryogen liquid pipeline to connect through second heat exchanger, the second generator and the 3rd throttle valve and evaporator again afterwards It is logical, there is cryogen liquid pipeline to connect adjustment with evaporator through heat exchanger, the second generator and second throttle in the 3rd generator There is cryogen liquid pipeline through the 4th generator, heat exchanger, the second generator and second throttle and evaporator for the 3rd generator Connection, second heat exchanger also have heated medium pipeline to be connected with outside, form the 4th class absorption heat pump.
8. the 4th class absorption heat pump, be in the 4th class absorption heat pump described in the 4th, the 4th generator of increase, 3rd throttle valve, the 4th solution heat exchanger and second heat exchanger, have weak solution pipeline through solution pump, by the second absorber Two solution heat exchangers and the 3rd solution heat exchanger are connected with generator to be adjusted to the second absorber and has weak solution pipeline through molten Liquid pump, the 4th solution heat exchanger, the second solution heat exchanger and the 3rd solution heat exchanger are connected with generator, by the 3rd hair Raw device has concentrated solution pipeline to connect with the second generator through the second solution heat exchanger to be adjusted to the 3rd generator and have concentrated solution pipe The second solution heat exchanger of road is connected with the 4th generator, and the 4th generator has concentrated solution pipeline through the 4th solution heat exchange again Device is connected with the second generator, and the 4th generator also has refrigerant steam channel to be connected with condenser, and the 3rd generator is had cryogen Steam channel connected with condenser be adjusted to the 3rd generator have refrigerant steam channel connected with the 4th generator after the 4th hair Raw device has cryogen liquid pipeline to be connected through second heat exchanger, the second generator and the 3rd throttle valve with evaporator again, by the 3rd hair Raw device has cryogen liquid pipeline to connect with evaporator through heat exchanger, the second generator and second throttle to be adjusted to the 3rd generator There is cryogen liquid pipeline to be connected through the 4th generator, heat exchanger, the second generator and second throttle with evaporator, the second heat is handed over Parallel operation also has heated medium pipeline to be connected with outside, forms the 4th class absorption heat pump.
9. the 4th class absorption heat pump, be in the 4th class absorption heat pump described in the 5th, the 4th generator of increase, 3rd throttle valve, the 4th solution pump, the 4th solution heat exchanger and second heat exchanger, have weak solution pipeline by the second absorber Connected through solution pump and the second solution heat exchanger with the 3rd generator and be adjusted to the second absorber and have weak solution pipeline through solution Pump and the second solution heat exchanger are connected with the 4th generator, and the 4th generator has concentrated solution pipeline through the 4th solution pump and the again Four solution heat exchangers are connected with the 3rd generator, have the concentrated solution pipeline molten through the 3rd solution heat exchanger and second in generator Liquid heat exchanger is connected with the second generator to be adjusted to generator and has concentrated solution pipeline through the 3rd solution heat exchanger, the 4th solution Heat exchanger and the second solution heat exchanger are connected with the second generator, and the 4th generator also has refrigerant steam channel and condenser Connection, has refrigerant steam channel to connect with condenser in the 3rd generator and is adjusted to the 3rd generator and has refrigerant steam channel and the The 4th generator has cryogen liquid pipeline through second heat exchanger, the second generator and the 3rd throttle valve again after the connection of four generators Connected with evaporator, the 3rd generator is had into cryogen liquid pipeline through heat exchanger, the second generator and second throttle and evaporation Device connection, which is adjusted to the 3rd generator, has cryogen liquid pipeline through the 4th generator, heat exchanger, the second generator and the second throttling Valve is connected with evaporator, and second heat exchanger also has heated medium pipeline to be connected with outside, forms the 4th class absorption heat pump.
10. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in 7-9, cancels throttling Valve, second throttle and the 3rd throttle valve, have cryogen liquid pipeline to be connected through throttle valve with evaporator in the second generator and are adjusted to Second generator has cryogen liquid pipeline to be connected with evaporator, and the second generator is had cryogen liquid pipeline through second throttle and evaporation Device connection, which is adjusted to the second generator, has cryogen liquid pipeline to be connected with evaporator, and the second generator is had cryogen liquid pipeline through the 3rd Throttle valve is connected with evaporator to be adjusted to the second generator and has cryogen liquid pipeline to be connected with evaporator, forms the 4th kind absorption type heat Pump.
11. the 4th class absorption heat pump, mainly by generator, the second generator, absorber, the second absorber, condenser, Evaporator, throttle valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, the 3rd generator, the 3rd Solution pump, the 3rd solution heat exchanger and the 3rd absorber are formed；Absorber have weak solution pipeline through solution heat exchanger with Second absorber connects, and the second absorber also has weak solution pipeline through solution pump and the second solution heat exchanger and the 3rd absorber Connection, the 3rd absorber also have weak solution pipeline to be connected through the 3rd solution pump and the 3rd solution heat exchanger with generator, occur Device also has concentrated solution pipeline to be connected through the 3rd solution heat exchanger with the 3rd generator, and the 3rd generator also has concentrated solution pipeline warp Second solution heat exchanger is connected with the second generator, and the second generator also has concentrated solution pipeline through the second solution pump and solution heat Exchanger is connected with absorber, and generator also has refrigerant steam channel to be connected with condenser, and the second generator also has refrigerant vapour Passage is connected with the second absorber, and the 3rd generator also has refrigerant steam channel to be connected with the 3rd absorber, and condenser is also cold The second generator has cryogen liquid pipeline to be connected through throttle valve with evaporator again after agent liquid pipeline is connected with the second generator, evaporation Device also has refrigerant steam channel to be connected with absorber, and generator and the 3rd generator also have driving heat medium pipeline and outside respectively Connection, absorber, condenser and the 3rd absorber also have heated medium pipeline to be connected with outside respectively, and evaporator also has surplus heat Medium pipeline is connected with outside, and the second absorber also has cooling medium pipeline to be connected with outside, forms the 4th class absorption heat pump.
, will 12. the 4th class absorption heat pump, is in the 4th class absorption heat pump described in the 11st, cancels throttle valve Second generator have cryogen liquid pipeline connected through throttle valve with evaporator be adjusted to the second generator have cryogen liquid pipeline with evaporation Device connects, and forms the 4th class absorption heat pump.
13. the 4th class absorption heat pump, is in the 4th class absorption heat pump described in the 11st, increase the 4th occurs Device, second throttle, the 4th solution pump, the 4th solution heat exchanger and heat exchanger, the 3rd absorber add weak solution pipeline Connected through the 4th solution pump and the 4th solution heat exchanger with the 4th generator, the 4th generator also has concentrated solution pipeline through the 4th Generator is connected with the 3rd generator, is had refrigerant steam channel to connect with condenser in generator and is adjusted to generator and has cryogen steaming The 4th generator has cryogen liquid pipeline through heat exchanger, the second generator and second again after vapour passage is connected with the 4th generator Throttle valve is connected with evaporator, and the 4th generator also has refrigerant steam channel to be connected with condenser, and heat exchanger, which also has, to be heated Medium pipeline is connected with outside, forms the 4th class absorption heat pump.
14. the 4th class absorption heat pump, is in the 4th class absorption heat pump described in the 11st, increase the 4th occurs Device, second throttle, the 4th solution heat exchanger and heat exchanger, have weak solution pipeline through the 3rd solution pump by the 3rd absorber Connected with the 3rd solution heat exchanger with generator and be adjusted to the 3rd absorber and have weak solution pipeline through the 3rd solution pump, the 3rd molten Liquid heat exchanger and the 4th solution heat exchanger are connected with generator, and generator is had concentrated solution pipeline through the 3rd solution heat exchange Device is connected with the 3rd generator to be adjusted to generator and has concentrated solution pipeline to be connected through the 4th solution heat exchanger with the 4th generator, 4th generator has concentrated solution pipeline to be connected through the 3rd solution heat exchanger with the 3rd generator again, and generator is had refrigerant vapour Passage connected with condenser be adjusted to generator have refrigerant steam channel connected with the 4th generator after the 4th generator have again Cryogen liquid pipeline is connected through heat exchanger, the second generator and second throttle with evaporator, and the 4th generator also has cryogen steaming Vapour passage is connected with condenser, and heat exchanger also has heated medium pipeline to be connected with outside, forms the 4th class absorption heat pump.
15. the 4th class absorption heat pump, is in the 4th class absorption heat pump described in the 11st, increase the 4th occurs Device, second throttle, the 4th solution pump, the 4th solution heat exchanger and heat exchanger, have weak solution pipeline by the 3rd absorber Connected through the 3rd solution pump and the 3rd solution heat exchanger with generator and be adjusted to the 3rd absorber and have weak solution pipeline through the 3rd Solution pump and the 3rd solution heat exchanger are connected with the 4th generator, and the 4th generator also has concentrated solution pipeline through the 4th solution pump Connected with the 4th solution heat exchanger with generator, there is concentrated solution pipeline to be sent out through the 3rd solution heat exchanger and the 3rd in generator Raw device connection, which is adjusted to generator, has concentrated solution pipeline to be sent out through the 4th solution heat exchanger and the 3rd solution heat exchanger and the 3rd Raw device connection, has refrigerant steam channel connect with condenser in generator and is adjusted to generator and has refrigerant steam channel and the 4th to send out The 4th generator has cryogen liquid pipeline through heat exchanger, the second generator and second throttle and evaporator again after raw device connection Connection, the 4th generator also have refrigerant steam channel to be connected with condenser, and heat exchanger also has heated medium pipeline and outside Connection, forms the 4th class absorption heat pump.
16. the 4th class absorption heat pump, is the 4th hair in any 4th class absorption heat pump described in 13-15 Raw device is added driving heat medium pipeline and is connected with outside, forms the 4th class absorption heat pump.
17. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in 13-16, cancels section Valve and second throttle are flowed, has cryogen liquid pipeline to be connected through throttle valve with evaporator in the second generator and is adjusted to the second generator There is cryogen liquid pipeline to be connected with evaporator, there is cryogen liquid pipeline to connect adjustment with evaporator through second throttle in the second generator There is cryogen liquid pipeline to be connected with evaporator for the second generator, form the 4th class absorption heat pump.
18. the 4th class absorption heat pump, is in the 4th class absorption heat pump described in the 1st or the 11st, increase is newly-increased Generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, have weak solution pipeline to be handed over through solution heat absorber Parallel operation is connected with the second absorber to be adjusted to absorber and has weak solution pipeline to connect through newly-increased solution heat exchanger and newly-increased absorber Logical, newly-increased absorber has weak solution pipeline to be connected through newly-increased solution pump and solution heat exchanger with the second absorber again, by second Generator have concentrated solution pipeline connected through the second solution pump and solution heat exchanger with absorber be adjusted to the second generator have it is dense Solution line is connected through solution heat exchanger with newly-increased generator, newly-increased generator have concentrated solution pipeline through the second solution pump again and Newly-increased solution heat exchanger is connected with absorber, and newly-increased generator also has refrigerant steam channel to be connected with newly-increased absorber, by the Two generators have cryogen liquid pipeline to connect with evaporator through throttle valve to be adjusted to the second generator and have cryogen liquid pipeline and new additional issue Newly-increased generator has cryogen liquid pipeline to be connected through throttle valve with evaporator again after raw device connection, and newly-increased absorber, which also has to cool down, to be situated between Matter pipeline is connected with outside, forms the 4th class absorption heat pump.
19. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in the 18th, cancels throttling Valve, by newly-increased generator have cryogen liquid pipeline connected with evaporator through throttle valve be adjusted to newly-increased generator have cryogen liquid pipeline with Evaporator connects, and forms the 4th class absorption heat pump.
20. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in 3-5,13-16, increases Add newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, absorber is had into weak solution pipeline through molten Liquid heat exchanger is connected with the second absorber to be adjusted to absorber and has weak solution pipeline to be inhaled through newly-increased solution heat exchanger with newly-increased Device connection is received, newly-increased absorber has weak solution pipeline to be connected through newly-increased solution pump and solution heat exchanger with the second absorber again, There is concentrated solution pipeline to be connected through the second solution pump and solution heat exchanger with absorber in the second generator and be adjusted to the second generation Device has concentrated solution pipeline to be connected through solution heat exchanger with newly-increased generator, and newly-increased generator has the concentrated solution pipeline molten through second again Liquid pump and newly-increased solution heat exchanger are connected with absorber, and newly-increased generator also has refrigerant steam channel to connect with newly-increased absorber It is logical, by the second generator have cryogen liquid pipeline connected with evaporator through throttle valve be adjusted to the second generator have cryogen liquid pipeline and Newly-increased generator has cryogen liquid pipeline to be connected through throttle valve with evaporator again after newly-increased generator connection, and the second generator is had Cryogen liquid pipeline is connected through second throttle with evaporator to be adjusted to the second generator and has cryogen liquid pipeline and newly-increased generator to connect Newly-increased generator has cryogen liquid pipeline to be connected through second throttle with evaporator again after logical, increases absorber newly and also cools down medium Pipeline is connected with outside, forms the 4th class absorption heat pump.
21. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in the 20th, cancels throttle valve And second throttle, by newly-increased generator have cryogen liquid pipeline connected with evaporator through throttle valve be adjusted to newly-increased generator have it is cold Agent liquid pipeline is connected with evaporator, is had cryogen liquid pipeline to be connected through second throttle with evaporator in newly-increased generator and is adjusted to new Increasing generator has cryogen liquid pipeline to be connected with evaporator, forms the 4th class absorption heat pump.
22. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in 7-9, increase is newly-increased Generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, have weak solution pipeline to be handed over through solution heat absorber Parallel operation is connected with the second absorber to be adjusted to absorber and has weak solution pipeline to connect through newly-increased solution heat exchanger and newly-increased absorber Logical, newly-increased absorber has weak solution pipeline to be connected through newly-increased solution pump and solution heat exchanger with the second absorber again, by second Generator have concentrated solution pipeline connected through the second solution pump and solution heat exchanger with absorber be adjusted to the second generator have it is dense Solution line is connected through solution heat exchanger with newly-increased generator, newly-increased generator have concentrated solution pipeline through the second solution pump again and Newly-increased solution heat exchanger is connected with absorber, and newly-increased generator also has refrigerant steam channel to be connected with newly-increased absorber, by the Two generators have cryogen liquid pipeline to connect with evaporator through throttle valve to be adjusted to the second generator and have cryogen liquid pipeline and new additional issue Newly-increased generator has cryogen liquid pipeline to be connected through throttle valve with evaporator again after raw device connection, and the second generator is had cryogen liquid Pipeline is connected through second throttle with evaporator to be adjusted to the second generator and has after cryogen liquid pipeline connects with newly-increased generator Newly-increased generator has cryogen liquid pipeline to be connected through second throttle with evaporator again, and the second generator is had cryogen liquid pipeline through Three throttle valves are connected with evaporator to be adjusted to the second generator and has cryogen liquid pipeline is newly-increased after being connected with newly-increased generator to occur Device has cryogen liquid pipeline to be connected through the 3rd throttle valve with evaporator again, and newly-increased absorber also has cooling medium pipeline to connect with outside It is logical, form the 4th class absorption heat pump.
23. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in the 22nd, cancels throttling Valve, second throttle and the 3rd throttle valve, have cryogen liquid pipeline to be connected through throttle valve with evaporator in newly-increased generator and are adjusted to Newly-increased generator has cryogen liquid pipeline to be connected with evaporator, and newly-increased generator is had cryogen liquid pipeline through second throttle and evaporation Device connection, which is adjusted to newly-increased generator, has cryogen liquid pipeline to be connected with evaporator, and newly-increased generator is had cryogen liquid pipeline through the 3rd Throttle valve is connected with evaporator to be adjusted to newly-increased generator and has cryogen liquid pipeline connect with evaporator, and the 4th kind absorption type of formation is warm Pump.
24. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in 1-17, increase is newly-increased Generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, have refrigerant steam channel and absorber by evaporator Connection, which is adjusted to evaporator, has refrigerant steam channel to be connected with newly-increased absorber, and newly-increased absorber also has weak solution pipeline through newly-increased Solution pump and newly-increased solution heat exchanger are connected with newly-increased generator, and newly-increased generator also has concentrated solution pipeline through new solubilization liquid heat Exchanger is connected with newly-increased absorber, and newly-increased generator also has refrigerant steam channel to be connected with absorber, and newly-increased generator also has Driving heat medium pipeline is connected with outside, and newly-increased absorber also has heated medium pipeline to be connected with outside, is formed the 4th class and is inhaled Receipts formula heat pump.
25. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in 18-23, increase is new Increase the second generator, newly-increased second absorber, newly-increased second solution pump and newly-increased second solution heat exchanger, evaporator is had cold Agent steam channel is connected with absorber to be adjusted to evaporator and has refrigerant steam channel connect with newly-increased second absorber, and newly-increased second Absorber also has weak solution pipeline to connect through newly-increased second solution pump and newly-increased second solution heat exchanger with newly-increased second generator Logical, newly-increased second generator also has concentrated solution pipeline to be connected through newly-increased second solution heat exchanger with newly-increased second absorber, newly Increasing the second generator also has refrigerant steam channel to be connected with absorber, increase newly the second generator also have drive heat medium pipeline with it is outer Portion connects, and newly-increased second absorber also has heated medium pipeline to be connected with outside, forms the 4th class absorption heat pump.
26. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in 1-2,11-12, increases Add newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, by generator have refrigerant steam channel with Condenser connection, which is adjusted to generator, has refrigerant steam channel to be connected with newly-increased absorber, and newly-increased absorber also has weak solution pipeline Connected through newly-increased solution pump and newly-increased solution heat exchanger with newly-increased generator, newly-increased generator also has concentrated solution pipeline through newly-increased Solution heat exchanger is connected with newly-increased absorber, and newly-increased generator also has refrigerant steam channel to be connected with condenser, is increased newly and is occurred Device, which also has, drives heat medium pipeline connect with exterior, and newly-increased absorber also has heated medium pipeline to be connected with exterior, formation the Four class absorption heat pumps.
27. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in 18-19, increase is new Increase the second generator, newly-increased second absorber, newly-increased second solution pump and newly-increased second solution heat exchanger, generator is had cold Agent steam channel is connected with condenser to be adjusted to generator and has refrigerant steam channel connect with newly-increased second absorber, and newly-increased second Absorber also has weak solution pipeline to connect through newly-increased second solution pump and newly-increased second solution heat exchanger with newly-increased second generator Logical, newly-increased second generator also has concentrated solution pipeline to be connected through newly-increased second solution heat exchanger with newly-increased second absorber, newly Increasing the second generator also has refrigerant steam channel to be connected with condenser, increase newly the second generator also have drive heat medium pipeline with it is outer Portion connects, and newly-increased second absorber also has heated medium pipeline to be connected with outside, forms the 4th class absorption heat pump.
28. the 4th class absorption heat pump, is in the 4th class absorption heat pump described in the 1st or the 11st, cancels second The cooling medium pipeline that absorber is connected with outside, has cryogen liquid pipeline to connect tune with evaporator through throttle valve in the second generator Whole is that the second generator has cryogen liquid pipeline to be connected through throttle valve and the second absorber with evaporator, forms the 4th kind absorption type heat Pump.
29. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in 3-5,13-16, takes Disappear the cooling medium pipeline that the second absorber is connected with outside, and the second generator is had cryogen liquid pipeline through throttle valve and evaporator Connection, which is adjusted to the second generator, has cryogen liquid pipeline to be connected through throttle valve and the second absorber with evaporator, by the second generator There is cryogen liquid pipeline to connect with evaporator through second throttle to be adjusted to the second generator and have cryogen liquid pipeline through second throttle Connected with the second absorber with evaporator, form the 4th class absorption heat pump.
30. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in 3-5,13-16, takes Disappear the cooling medium pipeline that the second absorber is connected with outside, and the second generator is had cryogen liquid pipeline through throttle valve and evaporator Connection, which is adjusted to the second generator, has cryogen liquid pipeline to be connected through throttle valve and the second absorber with evaporator, or second is occurred Device have cryogen liquid pipeline connected through second throttle with evaporator be adjusted to the second generator have cryogen liquid pipeline through second throttling Valve and the second absorber are connected with evaporator, form the 4th class absorption heat pump.
31. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in 7-9, cancels second Absorber and the exterior cooling medium pipeline connected, and carry out the one-out-three in following Adjusted Option, three select two or three to select three, obtain To the 4th class absorption heat pump：Adjusted Option one, is to have cryogen liquid pipeline to be connected through throttle valve with evaporator in the second generator Being adjusted to the second generator has cryogen liquid pipeline to be connected through throttle valve and the second absorber with evaporator；Adjusted Option two, be by Second generator have cryogen liquid pipeline connected through second throttle with evaporator be adjusted to the second generator have cryogen liquid pipeline warp Second throttle and the second absorber are connected with evaporator；Adjusted Option three, is that the second generator is had cryogen liquid pipeline through Three throttle valves are connected with evaporator to be adjusted to the second generator and has cryogen liquid pipeline through the 3rd throttle valve and the second absorber with steaming Send out device connection.
32. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in the 18th, cancels second and inhale The cooling medium pipeline that device is connected with outside is received, cancels the cooling medium pipeline that newly-increased absorber is connected with outside, will newly issue additional Raw device has cryogen liquid pipeline to connect to be adjusted to increase generator newly with evaporator through throttle valve and have cryogen liquid pipeline through throttle valve, second Absorber and newly-increased absorber are connected with evaporator, form the 4th class absorption heat pump.
33. the 4th class absorption heat pump, is in any 4th kind absorption type described in the 1st, 3-5,7-9,11,13-16 In heat pump, cancel the cooling medium pipeline that the second absorber is connected with outside, have technical measures 1. --- increase circulating pump, circulation Pump has circulatory mediator pipeline to be sequentially communicated the second absorber and the finisher of evaporator circulatory mediator pipeline and circulating pump again Shape and composition circulation loop are connected, forms the 4th class absorption heat pump；Separately there are technical measures 2. --- increase intermediate heat exchanger, Intermediate heat exchanger connects the second absorber and evaporator, forms the 4th class absorption heat pump.
34. the 4th class absorption heat pump, is the increase in any 4th class absorption heat pump described in the 18th, 20,22 Circulating pump, cancels the cooling medium pipeline that the second absorber is connected with outside, cancels the cooling that newly-increased absorber is connected with outside Medium pipeline, circulating pump have the finisher that circulatory mediator pipeline is sequentially communicated newly-increased absorber, the second absorber and evaporator Connect shape with circulating pump by circulatory mediator pipeline again and form circulation loop, form the 4th class absorption heat pump.
35. the 5th class absorption heat pump, is in the 4th class absorption heat pump described in the 1st or the 11st, increase is newly-increased Generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, have weak solution pipeline to be handed over through solution heat absorber Parallel operation is connected with the second absorber to be adjusted to absorber and has weak solution pipeline to connect through newly-increased solution heat exchanger and newly-increased absorber Logical, newly-increased absorber has weak solution pipeline to be connected through newly-increased solution pump and solution heat exchanger with the second absorber again, by second Generator have concentrated solution pipeline connected through the second solution pump and solution heat exchanger with absorber be adjusted to the second generator have it is dense Solution line is connected through solution heat exchanger with newly-increased generator, newly-increased generator have concentrated solution pipeline through the second solution pump again and Newly-increased solution heat exchanger is connected with absorber, and newly-increased generator also has refrigerant steam channel to be connected with newly-increased absorber, is increased newly The generator medium pipeline that also has surplus heat connect with outside, and newly-increased absorber, which also has, to be cooled down medium pipeline and connected with exterior, formation the Five class absorption heat pumps.
36. the 5th class absorption heat pump, is in any 4th class absorption heat pump described in the 35th, cancels throttling Valve, by the second generator have cryogen liquid pipeline connected with evaporator through throttle valve be adjusted to the second generator have cryogen liquid pipeline with Evaporator connects, and forms the 5th class absorption heat pump.
37. the 5th class absorption heat pump, is in any 4th class absorption heat pump described in 3-5,13-16, increases Add newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, absorber is had into weak solution pipeline through molten Liquid heat exchanger is connected with the second absorber to be adjusted to absorber and has weak solution pipeline to be inhaled through newly-increased solution heat exchanger with newly-increased Device connection is received, newly-increased absorber has weak solution pipeline to be connected through newly-increased solution pump and solution heat exchanger with the second absorber again, There is concentrated solution pipeline to be connected through the second solution pump and solution heat exchanger with absorber in the second generator and be adjusted to the second generation Device has concentrated solution pipeline to be connected through solution heat exchanger with newly-increased generator, and newly-increased generator has the concentrated solution pipeline molten through second again Liquid pump and newly-increased solution heat exchanger are connected with absorber, and newly-increased generator also has refrigerant steam channel to connect with newly-increased absorber Logical, the newly-increased generator medium pipeline that also has surplus heat connect with exterior, and newly-increased absorber also has cooling medium pipeline to be connected with exterior, Form the 4th class absorption heat pump.
38. the 5th class absorption heat pump, is in any 5th class absorption heat pump described in the 37th, cancels throttle valve And second throttle, by the second generator have cryogen liquid pipeline connected with evaporator through throttle valve be adjusted to the second generator have it is cold Agent liquid pipeline is connected with evaporator, is had cryogen liquid pipeline to be connected through second throttle with evaporator in the second generator and is adjusted to Two generators have cryogen liquid pipeline to be connected with evaporator, form the 5th class absorption heat pump.
39. the 5th class absorption heat pump, is in any 4th class absorption heat pump described in 7-9, increase is newly-increased Generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, have weak solution pipeline to be handed over through solution heat absorber Parallel operation is connected with the second absorber to be adjusted to absorber and has weak solution pipeline to connect through newly-increased solution heat exchanger and newly-increased absorber Logical, newly-increased absorber has weak solution pipeline to be connected through newly-increased solution pump and solution heat exchanger with the second absorber again, by second Generator have concentrated solution pipeline connected through the second solution pump and solution heat exchanger with absorber be adjusted to the second generator have it is dense Solution line is connected through solution heat exchanger with newly-increased generator, newly-increased generator have concentrated solution pipeline through the second solution pump again and Newly-increased solution heat exchanger is connected with absorber, and newly-increased generator also has refrigerant steam channel to be connected with newly-increased absorber, is increased newly The generator medium pipeline that also has surplus heat connect with outside, and newly-increased absorber, which also has, to be cooled down medium pipeline and connected with exterior, formation the Five class absorption heat pumps.
40. the 5th class absorption heat pump, is in any 5th class absorption heat pump described in the 39th, cancels throttling Valve, second throttle and the 3rd throttle valve, have cryogen liquid pipeline to be connected through throttle valve with evaporator in the second generator and are adjusted to Second generator has cryogen liquid pipeline to be connected with evaporator, and the second generator is had cryogen liquid pipeline through second throttle and evaporation Device connection, which is adjusted to the second generator, has cryogen liquid pipeline to be connected with evaporator, and the second generator is had cryogen liquid pipeline through the 3rd Throttle valve is connected with evaporator to be adjusted to the second generator and has cryogen liquid pipeline to be connected with evaporator, forms the 5th kind absorption type heat Pump.
41. the 5th class absorption heat pump, is in any 4th class absorption heat pump described in 1-17,28-34 Two generators are added waste heat medium pipeline and are connected with outside, form the 5th class absorption heat pump.
42. the 5th class absorption heat pump, is the second hair in any 4th class absorption heat pump described in 18-23 Raw device and newly-increased generator are added waste heat medium pipeline and are connected with outside respectively, form the 5th class absorption heat pump.
43. the 5th class absorption heat pump, is the second hair in any 4th class absorption heat pump described in 18-23 Raw device or newly-increased generator are added waste heat medium pipeline and are connected with outside, form the 5th class absorption heat pump.
44. the 5th class absorption heat pump, is in any 5th class absorption heat pump described in the 41st, increases new additional issue Raw device, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, have refrigerant steam channel to connect with absorber evaporator Logical to be adjusted to evaporator and have refrigerant steam channel connect with newly-increased absorber, newly-increased absorber also has weak solution pipeline through newly solubilized Liquid pump and newly-increased solution heat exchanger are connected with newly-increased generator, and newly-increased generator also has concentrated solution pipeline to be handed over through new solubilization liquid heat Parallel operation is connected with newly-increased absorber, and newly-increased generator also has refrigerant steam channel to be connected with absorber, increases generator newly and also has drive Dynamic heat medium pipeline is connected with outside, and newly-increased absorber also has heated medium pipeline to be connected with outside, is formed the 5th class and is absorbed Formula heat pump.
45. the 5th class absorption heat pump, be in any 5th class absorption heat pump described in 35-38,42-43, Newly-increased second generator of increase, newly-increased second absorber, newly-increased second solution pump and newly-increased second solution heat exchanger, will evaporate Device has refrigerant steam channel to connect with absorber to be adjusted to evaporator and have refrigerant steam channel to connect with newly-increased second absorber, newly Increase the second absorber and also have weak solution pipeline through newly-increased second solution pump and newly-increased second solution heat exchanger and newly-increased second hair Raw device connection, newly-increased second generator also have concentrated solution pipeline to connect through newly-increased second solution heat exchanger and newly-increased second absorber Logical, newly-increased second generator also has refrigerant steam channel to be connected with absorber, increases the second generator newly and also has driving thermal medium pipe Road is connected with outside, and newly-increased second absorber also has heated medium pipeline to be connected with outside, forms the 5th class absorption heat pump.
46. the 5th class absorption heat pump, is in any 4th class absorption heat pump described in 1-17, increase is newly-increased Generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, have refrigerant steam channel and the by the second generator The connection of two absorbers, which is adjusted to the second generator, has refrigerant steam channel to be connected with newly-increased absorber, and newly-increased absorber also has dilute molten Liquid pipeline is connected through newly-increased solution pump and newly-increased solution heat exchanger with newly-increased generator, and newly-increased generator also has concentrated solution pipeline Connected through newly-increased solution heat exchanger with newly-increased absorber, newly-increased generator also has refrigerant steam channel to connect with the second absorber Logical, the newly-increased generator medium pipeline that also has surplus heat connect with exterior, and newly-increased absorber also has cooling medium pipeline to be connected with exterior, Form the 5th class absorption heat pump.
47. the 5th class absorption heat pump, is in any 5th class absorption heat pump described in 35-40, increase is new Increase the second generator, newly-increased second absorber, newly-increased second solution pump and newly-increased second solution heat exchanger, by newly-increased generator There is refrigerant steam channel to connect with newly-increased absorber to be adjusted to newly-increased generator and have refrigerant steam channel and newly-increased second absorber Connection, increases the second absorber newly and also has weak solution pipeline through newly-increased second solution pump and newly-increased second solution heat exchanger with increasing newly Second generator connects, and newly-increased second generator also has concentrated solution pipeline to be inhaled through newly-increased second solution heat exchanger with newly-increased second Device connection is received, newly-increased second generator also has refrigerant steam channel to be connected with newly-increased absorber, and newly-increased second generator is also had a surplus Heat medium pipeline is connected with outside, and newly-increased second absorber also has cooling medium pipeline to be connected with outside, is formed the 5th class and is absorbed Formula heat pump.
48. the 5th class absorption heat pump, is the second hair in any 5th class absorption heat pump described in 45-47 Raw device is added waste heat medium pipeline and is connected with outside, forms the 5th class absorption heat pump.
49. the 5th class absorption heat pump, is in any 4th class absorption heat pump described in 18-23, increase is new Increase the second generator, newly-increased second absorber, newly-increased second solution pump and newly-increased second solution heat exchanger, by newly-increased generator There is refrigerant steam channel to connect with newly-increased absorber to be adjusted to newly-increased generator and have refrigerant steam channel and newly-increased second absorber Connection, increases the second absorber newly and also has weak solution pipeline through newly-increased second solution pump and newly-increased second solution heat exchanger with increasing newly Second generator connects, and newly-increased second generator also has concentrated solution pipeline to be inhaled through newly-increased second solution heat exchanger with newly-increased second Device connection is received, newly-increased second generator also has refrigerant steam channel to be connected with newly-increased absorber, and newly-increased second generator is also had a surplus Heat medium pipeline is connected with outside, and newly-increased second absorber also has cooling medium pipeline to be connected with outside, is formed the 5th class and is absorbed Formula heat pump.
50. the 5th class absorption heat pump, is the second generator in any 5th class absorption heat pump described in the 49th Waste heat medium pipeline is added respectively with newly-increased generator to connect with outside, forms the 5th class absorption heat pump.
51. the 5th class absorption heat pump, is the second generator in any 5th class absorption heat pump described in the 49th Or newly-increased generator is added waste heat medium pipeline and is connected with outside, forms the 5th class absorption heat pump.
Come furtherly by taking the 5th class absorption heat pump shown in the 4th class absorption heat pump shown in Fig. 1 and Figure 17 as an example below Bright essence of the invention：
(1) high temperature driven heat is transferred to by generator 1 in the refrigerant vapour that it is discharged, will wherein by condenser 5 A part of heat transfer is into heated medium, so as to fulfill the utilization of the temperature difference between high temperature driven thermal medium and heated medium； Since the latent heat of high-temperature medium is relatively small, then cause the sensible heat containing relative abundance in the cryogen liquid of condenser 5, take directly Technological means through throttle valve 7 throttling into evaporator 6 will cause being greatly lowered for UTILIZATION OF VESIDUAL HEAT IN amount.
(2) in Fig. 1, the sensible heat in cryogen liquid is delivered in cooling medium by the second generator 2 and the second absorber 4, Second of temperature drop of part high temperature driven heat is played a role --- reduce into generator 1 solution concentration or improve into Enter the solution concentration of absorber 3.
(3) in Figure 17, cryogen liquid stream in solution and makes it discharge low pressure refrigerant vapour to second through 2 heat release of the second generator Absorber 4 provides, and cryogen liquid is so high again through flowing through the heat absorption of the second absorber 4 and part vaporization after 7 reducing pressure by regulating flow of throttle valve Temperature driving heat is cooled to evaporating temperature again；This temperature difference plays a role --- reduce into generator 1 solution concentration or carry The solution concentration into absorber 3 is risen, this temperature difference also belongs to the driving temperature difference.
Such two kinds of temperature drops using high temperature driven heat is the driving temperature difference, including can realize what cold environmental resource was utilized Absorption heat pump, different from existing first-class absorption type heat pump, second-kind absorption-type heat pump and the 3rd class absorption heat pump, belongs to In new type；The time occurred according to technology and consideration naming order, two kinds of temperature drops using high temperature driven heat are referred to as driving temperature The absorption heat pump of difference be the 4th class absorption heat pump, claim to increase on the basis of the 4th class absorption heat pump more than hot and cold environment it Between the temperature difference be drive the temperature difference absorption heat pump be the 5th class absorption heat pump.
Brief description of the drawings：
Fig. 1 is according to the 4th class absorption heat pump the 1st kind of structure and flow diagram provided by the present invention.
Fig. 2 is according to the 4th class absorption heat pump the 2nd kind of structure and flow diagram provided by the present invention.
Fig. 3 is according to the 4th class absorption heat pump the 3rd kind of structure and flow diagram provided by the present invention.
Fig. 4 is according to the 4th class absorption heat pump the 4th kind of structure and flow diagram provided by the present invention.
Fig. 5 is according to the 4th class absorption heat pump the 5th kind of structure and flow diagram provided by the present invention.
Fig. 6 is according to the 4th class absorption heat pump the 6th kind of structure and flow diagram provided by the present invention.
Fig. 7 is according to the 4th class absorption heat pump the 7th kind of structure and flow diagram provided by the present invention.
Fig. 8 is according to the 4th class absorption heat pump the 8th kind of structure and flow diagram provided by the present invention.
Fig. 9 is according to the 4th class absorption heat pump the 9th kind of structure and flow diagram provided by the present invention.
Figure 10 is according to the 4th class absorption heat pump the 10th kind of structure and flow diagram provided by the present invention.
Figure 11 is according to the 4th class absorption heat pump the 11st kind of structure and flow diagram provided by the present invention.
Figure 12 is according to the 4th class absorption heat pump the 12nd kind of structure and flow diagram provided by the present invention.
Figure 13 is according to the 4th class absorption heat pump the 13rd kind of structure and flow diagram provided by the present invention.
Figure 14 is according to the 4th class absorption heat pump the 14th kind of structure and flow diagram provided by the present invention.
Figure 15 is according to the 4th class absorption heat pump the 15th kind of structure and flow diagram provided by the present invention.
Figure 16 is according to the 4th class absorption heat pump the 16th kind of structure and flow diagram provided by the present invention.
Figure 17 is according to the 4th class absorption heat pump the 17th kind of structure and flow diagram provided by the present invention.
Figure 18 is according to the 4th class absorption heat pump the 18th kind of structure and flow diagram provided by the present invention.
Figure 19 is according to the 5th class absorption heat pump the 1st kind of structure and flow diagram provided by the present invention.
Figure 20 is according to the 5th class absorption heat pump the 2nd kind of structure and flow diagram provided by the present invention.
Figure 21 is according to the 5th class absorption heat pump the 3rd kind of structure and flow diagram provided by the present invention.
In figure, 1- generators, the second generators of 2-, 3- absorbers, the second absorbers of 4-, 5- condensers, 6- evaporators, 7- Throttle valve, 8- solution pumps, the second solution pumps of 9-, 10- solution heat exchangers, the second solution heat exchangers of 11-, 12- the 3rd occur Device, 13- second throttle, the 3rd solution pumps of 14-, the 3rd solution heat exchangers of 15-, 16- heat exchangers, the 4th generators of 17-, The 3rd throttle valves of 18-, the 4th solution pumps of 19-, the 4th solution heat exchangers of 20-, 21- second heat exchangers, 22- the 3rd absorb Device；A- increases generator newly, and B- increases absorber newly, and C- increases solution pump newly, and D- increases solution heat exchanger, E- circulating pumps newly.
To note here is that：
(1) by taking the 4th class absorption heat pump shown in attached drawing 1 as an example, the throttle valve 7 that is set in cryogen liquid pipeline can use gravity Pressure drop substitutes；When coolant temperature is relatively low, the cryogen liquid temperature degree for flowing through the second generator 2 is cooled to steaming inside evaporator 6 When sending out temperature, throttle valve 7 is not provided with, and power pressure difference is used in 2 inner heat exchanger pipeline of the second generator.
(2) by taking the 4th class absorption heat pump shown in Figure 17 as an example, for freeze occasion when, flow through evaporator 6 waste heat be situated between Matter is traditionally referred to as traditionally is referred to as Absorption Refrigerator by refrigerant, the 4th class absorption heat pump at this time；In the present invention Referred to as the 4th class absorption heat pump.
Embodiment：
First it is noted that in the statement of structure and flow, do not repeat in the case of inessential；To apparent Flow do not state.The present invention is described in detail with example below in conjunction with the accompanying drawings.
What the 4th class absorption heat pump shown in Fig. 1 was realized in：
(1) in structure, it mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, Throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger are formed；Absorber 3 has weak solution Pipeline is connected through solution heat exchanger 10 with the second absorber 4, and the second absorber 4 also has weak solution pipeline through solution pump 8 and the Two solution heat exchangers 11 are connected with generator 1, and generator 1 also has concentrated solution pipeline through the second solution heat exchanger 11 and second Generator 2 connects, and the second generator 2 also has concentrated solution pipeline to connect through the second solution pump 9 and solution heat exchanger 10 with absorber 3 Logical, generator 1 also has refrigerant steam channel to be connected with condenser 5, and the second generator 2 also has refrigerant steam channel to be absorbed with second Device 4 connects, and second generator 2 has cryogen liquid pipeline warp again after the also cryogen liquid pipeline of condenser 5 is connected with the second generator 2 Throttle valve 7 is connected with evaporator 6, and evaporator 6 also has refrigerant steam channel to be connected with absorber 3, and generator 1, which also has, drives heat to be situated between Matter pipeline is connected with outside, and absorber 3 and condenser 5 also have heated medium pipeline to be connected with outside respectively, and evaporator 6 also has Waste heat medium pipeline is connected with outside, and the second absorber 4 also has cooling medium pipeline to be connected with outside.
(2) in flow, the weak solution of absorber 3 enters the second absorber 4 through solution heat exchanger 10, absorbs refrigerant vapour And heat release enters generator 1 in cooling medium, the weak solution of the second absorber 4 through 8 and second solution heat exchanger 11 of solution pump, The solution that driving thermal medium flows through generator 1, heating enters in it discharges refrigerant vapour and is provided to condenser 5, generator 1 Concentrated solution enters the second generator 2, heat absorption release refrigerant vapour through the second solution heat exchanger 11 and is carried to the second absorber 4 For the concentrated solution of the second generator 2 enters absorber 3 through the second solution pump 9 and solution heat exchanger 10, absorbs refrigerant vapour simultaneously Heat release is in heated medium；The refrigerant vapour heat release of condenser 5 occurs in heated medium into cryogen liquid, cryogen liquid stream through second There is provided, formed through the throttling of throttle valve 7 into evaporator 6, heat absorption into refrigerant vapour and to absorber 3 again after 2 heat release of device cooling 4th class absorption heat pump.
What the 4th class absorption heat pump shown in Fig. 2 was realized in：
(1) in structure, in the 4th class absorption heat pump shown in Fig. 1, the 3rd generator of increase, second throttle, the 3rd Solution pump, the 3rd solution heat exchanger and heat exchanger, the second absorber 4 add weak solution pipeline through the 3rd solution pump 14 and Three solution heat exchangers 15 are connected with the 3rd generator 12, and the 3rd generator 12 also has concentrated solution pipeline through the 3rd solution heat exchange Device 15 is connected with the second generator 2, is had refrigerant steam channel to connect with condenser 5 in generator 1 and is adjusted to generator 1 and has cryogen The 3rd generator 12 has cryogen liquid pipeline to occur through heat exchanger 16, second again after steam channel is connected with the 3rd generator 12 Device 2 and second throttle 13 are connected with evaporator 6, and the 3rd generator 12 also has refrigerant steam channel to be connected with condenser 5, and heat is handed over Parallel operation 16 also has heated medium pipeline to be connected with outside.
(2) in flow, the refrigerant vapour that generator 1 produces is supplied to the 3rd generator 12 to make driving thermal medium, and second inhales The part weak solution for receiving device 4 enters the 3rd generator 12, refrigerant vapour through the 3rd solution pump 14 and the 3rd solution heat exchanger 15 The 3rd generator 12, heating are flowed through into the solution release refrigerant vapour in it and is provided to condenser 5, the 3rd generator 12 Concentrated solution enters the second generator 2 through the 3rd solution heat exchanger 15；Flow through the refrigerant vapour heat release Cheng Leng of the 3rd generator 12 Followed by 16 and second generator 2 of heat exchanger and progressively heat release cools down after agent liquid, and the cryogen liquid after cooling is saved through second The stream throttling of valve 13 enters evaporator 6, forms the 4th class absorption heat pump.
What the 4th class absorption heat pump shown in Fig. 3 was realized in：
(1) in structure, in the 4th class absorption heat pump shown in Fig. 1, the 3rd generator of increase, second throttle, the 3rd Solution heat exchanger and heat exchanger, have weak solution pipeline through 8 and second solution heat exchanger 11 of solution pump by the second absorber 4 Connected with generator 1 and be adjusted to the second absorber 4 and have weak solution pipeline through solution pump 8, the second solution heat exchanger 11 and the 3rd Solution heat exchanger 15 is connected with generator 1, and generator 1 is had concentrated solution pipeline through the second solution heat exchanger 11 and the second hair The raw connection of device 2, which is adjusted to generator 1, has concentrated solution pipeline to be connected through the 3rd solution heat exchanger 15 with the 3rd generator 12, and the 3rd Generator 12 has concentrated solution pipeline to be connected through the second solution heat exchanger 11 with the second generator 2 again, and generator 1 is had cryogen steaming Vapour passage connected with condenser 5 be adjusted to generator 1 have refrigerant steam channel connected with the 3rd generator 12 after the 3rd occur Device 12 has cryogen liquid pipeline to be connected through heat exchanger 16, the second generator 2 and second throttle 13 with evaporator 6 again, the 3rd hair Raw device 12 also has refrigerant steam channel to be connected with condenser 5, and heat exchanger 16 also has heated medium pipeline to be connected with outside.
(2) in flow, the refrigerant vapour that generator 1 produces is supplied to the 3rd generator 12 to make driving thermal medium, and second inhales The weak solution for receiving device 4 enters generator 1 through solution pump 8, the second solution heat exchanger 11 and the 3rd solution heat exchanger 15, occurs The concentrated solution of device 1 enters the 3rd generator 12 through the 3rd solution heat exchanger 15, and refrigerant vapour flows through the 3rd generator 12, heating Solution in into it discharges refrigerant vapour and is provided to condenser 5, and the concentrated solution of the 3rd generator 12 is handed over through the second solution heat Parallel operation 11 enters the second generator 2；The refrigerant vapour heat release for flowing through the 3rd generator 12 is handed over followed by heat afterwards into cryogen liquid 16 and second generator 2 of parallel operation and progressively heat release cool down, and the cryogen liquid after cooling enters evaporator through the throttling of second throttle 13 6, form the 4th class absorption heat pump.
What the 4th class absorption heat pump shown in Fig. 4 was realized in：
(1) in structure, in the 4th class absorption heat pump shown in Fig. 1, the 3rd generator of increase, second throttle, the 3rd Solution pump, the 3rd solution heat exchanger and heat exchanger, have the weak solution pipeline molten through solution pump 8 and second second absorber 4 Liquid heat exchanger 11 connected with generator 1 be adjusted to the second absorber 4 have weak solution pipeline through 8 and second solution of solution pump heat hand over Parallel operation 11 is connected with the 3rd generator 12, and the 3rd generator 12 has concentrated solution pipeline through the 3rd solution pump 14 and the 3rd solution heat again Exchanger 15 is connected with generator 1, and generator 1 is had concentrated solution pipeline through the second solution heat exchanger 11 and the second generator 2 Connection, which is adjusted to generator 1, has concentrated solution pipeline through the 3rd solution heat exchanger 15 and the second solution heat exchanger 11 and the second hair Raw device 2 connects, and has refrigerant steam channel to connect with condenser 5 in generator 1 and is adjusted to generator 1 and has refrigerant steam channel and the The 3rd generator 12 has cryogen liquid pipeline through heat exchanger 16, the second generator 2 and the second section again after the connection of three generators 12 Stream valve 13 is connected with evaporator 6, and the 3rd generator 12 also has refrigerant steam channel to be connected with condenser 5, and heat exchanger 16 also has Heated medium pipeline is connected with outside.
(2) in flow, the refrigerant vapour that generator 1 produces is supplied to the 3rd generator 12 to make driving thermal medium, and second inhales The weak solution for receiving device 4 enters the 3rd generator 12 through 8 and second solution heat exchanger 11 of solution pump, and refrigerant vapour flows through the 3rd hair Solution release refrigerant vapour that raw device 12, heating enter in it is simultaneously provided to condenser 5, and the concentrated solution of the 3rd generator 12 is through the Three solution pumps 14 and the 3rd solution heat exchanger 15 enter generator 1, and the concentrated solution of generator 1 is through the 3rd solution heat exchanger 15 Enter the second generator 2 with the second solution heat exchanger 11；Flow through the refrigerant vapour heat release of the 3rd generator 12 into cryogen liquid it Followed by 16 and second generator 2 of heat exchanger and progressively heat release cools down afterwards, and the cryogen liquid after cooling is through second throttle 13 Throttling enters evaporator 6, forms the 4th class absorption heat pump.
What the 4th class absorption heat pump shown in Fig. 5 was realized in：
(1) in structure, in the 4th class absorption heat pump shown in Fig. 2, the 4th generator of increase, the 3rd throttle valve, the 4th Solution pump, the 4th solution heat exchanger and second heat exchanger, the second absorber 4 add weak solution pipeline through the 4th solution pump 19 Connected with the 4th solution heat exchanger 20 with the 4th generator 17, the 4th generator 17 also has concentrated solution pipeline through the 4th solution heat Exchanger 20 is connected with the second generator 2, and the 4th generator 17 also has refrigerant steam channel and condenser 5, by the 3rd generator 12, which have refrigerant steam channel to be connected with condenser 5, is adjusted to the 3rd generator 12 and has refrigerant steam channel to connect with the 4th generator 17 After logical 4th generator 17 have again cryogen liquid pipeline through second heat exchanger 21, the second generator 2 and the 3rd throttle valve 18 with Evaporator 6 connects, and the 3rd generator 12 is had cryogen liquid pipeline through heat exchanger 16, the second generator 2 and second throttle 13 Connected with evaporator 6 be adjusted to the 3rd generator 12 have cryogen liquid pipeline through the 4th generator 17, heat exchanger 16, second occur Device 2 and second throttle 13 are connected with evaporator 6, and second heat exchanger 21 also has heated medium pipeline to be connected with outside.
(2) in flow, refrigerant vapour and cryogen liquid that the 3rd generator 12 produces are supplied to the 4th generator 17 to drive Thermal medium, the part weak solution of the second absorber 4 enter the 4th through the 4th solution pump 19 and the 4th solution heat exchanger 20 and occur Device 17, refrigerant vapour and cryogen liquid stream enter solution release refrigerant vapour in it and to condensation through the 4th generator 17, heating Device 5 provides, and the concentrated solution of the 4th generator 17 enters the second generator 2 through the 4th solution heat exchanger 20；Flow through the 4th generation The refrigerant vapour heat release of device 17 is into followed by 21 and second generator 2 of second heat exchanger and progressively heat release drop after cryogen liquid Temperature, the cryogen liquid after cooling down enter evaporator 6 through the throttling of the 3rd throttle valve 18；The cryogen liquid of 3rd generator 12 followed by 4th generator 17,16 and second generator of heat exchanger, 2 heat release cooling, the cryogen liquid after cooling down are saved through second throttle 13 Stream enters evaporator 6, forms the 4th class absorption heat pump.
What the 4th class absorption heat pump shown in Fig. 6 was realized in：
(1) in structure, in the 4th class absorption heat pump shown in Fig. 3, the 4th generator of increase, the 3rd throttle valve, the 4th Solution heat exchanger and second heat exchanger, have weak solution pipeline through solution pump 8, the second solution heat exchange by the second absorber 4 11 and the 3rd solution heat exchanger 15 of device connected with generator 1 be adjusted to the second absorber 4 have weak solution pipeline through solution pump 8, 4th solution heat exchanger 20, the second solution heat exchanger 11 and the 3rd solution heat exchanger 15 are connected with generator 1, by the 3rd Generator 12 has concentrated solution pipeline to connect with the second generator 2 through the second solution heat exchanger 11 to be adjusted to the 3rd generator 12 and have Concentrated solution pipeline is connected through the second solution heat exchanger 11 with the 4th generator 17, and the 4th generator 17 has concentrated solution pipeline warp again 4th solution heat exchanger 20 is connected with the second generator 2, and the 4th generator 17 also has refrigerant steam channel and condenser 5, will 3rd generator 12 has refrigerant steam channel to connect with condenser 5 to be adjusted to the 3rd generator 12 and have refrigerant steam channel and the 4th The 4th generator 17 has cryogen liquid pipeline through second heat exchanger 21, the second generator 2 and the 3rd again after generator 17 connects Throttle valve 18 is connected with evaporator 6, and the 3rd generator 12 is had cryogen liquid pipeline through heat exchanger 16, the second generator 2 and Two throttle valves 13 are connected with evaporator 6 to be adjusted to the 3rd generator 12 and has cryogen liquid pipeline through the 4th generator 17, heat exchanger 16th, the second generator 2 and second throttle 13 are connected with evaporator 6, second heat exchanger 21 also have heated medium pipeline with Outside connection.
(2) in flow, refrigerant vapour and cryogen liquid that the 3rd generator 12 produces are supplied to the 4th generator 17 to drive Thermal medium, the weak solution of the second absorber 4 is through solution pump 8, the 4th solution heat exchanger 20, the second solution heat exchanger 11 and Three solution heat exchangers 15 enter generator 1, and the concentrated solution of generator 1 enters the 3rd generator through the 3rd solution heat exchanger 15 12, the concentrated solution of the 3rd generator 12 enters the 4th generator 17, refrigerant vapour and cryogen liquid through the second solution heat exchanger 11 The 4th generator 17, heating are flowed through into the solution release refrigerant vapour in it and is provided to condenser 5, the 4th generator 17 Concentrated solution enters the second generator 2 through the 4th solution heat exchanger 20；Flow through the refrigerant vapour heat release Cheng Leng of the 4th generator 17 Followed by 21 and second generator 2 of second heat exchanger and progressively heat release cools down after agent liquid, and the cryogen liquid after cooling down passes through The throttling of 3rd throttle valve 18 enters evaporator 6；The cryogen liquid of 3rd generator 12 is followed by the 4th generator 17, heat exchanger 16 and 2 heat release of the second generator cooling, cryogen liquid after cooling down enters evaporator 6 through the throttling of second throttle 13, formation the Four class absorption heat pumps.
What the 4th class absorption heat pump shown in Fig. 7 was realized in：
(1) in structure, in the 4th class absorption heat pump shown in Fig. 4, the 4th generator of increase, the 3rd throttle valve, the 4th Solution pump, the 4th solution heat exchanger and second heat exchanger, have weak solution pipeline through solution pump 8 and by the second absorber 4 Two solution heat exchangers 11 are connected with the 3rd generator 12 to be adjusted to the second absorber 4 and has weak solution pipeline through solution pump 8 and Two solution heat exchangers 11 are connected with the 4th generator 17, and the 4th generator 17 has concentrated solution pipeline through 19 He of the 4th solution pump again 4th solution heat exchanger 20 is connected with the 3rd generator 12, and generator 1 is had concentrated solution pipeline through the 3rd solution heat exchanger 15 and second solution heat exchanger 11 connected with the second generator 2 be adjusted to generator 1 have concentrated solution pipeline through the 3rd solution heat Exchanger 15, the 4th solution heat exchanger 20 and the second solution heat exchanger 11 are connected with the second generator 2, the 4th generator 17 Also refrigerant steam channel and condenser 5, have refrigerant steam channel to be connected with condenser 5 in the 3rd generator 12 and are adjusted to the 3rd Generator 12 have refrigerant steam channel connected with the 4th generator 17 after the 4th generator 17 have cryogen liquid pipeline again through second Heat exchanger 21, the second generator 2 and the 3rd throttle valve 18 are connected with evaporator 6, and the 3rd generator 12 is had cryogen liquid pipeline Connected through heat exchanger 16, the second generator 2 and second throttle 13 with evaporator 6 and be adjusted to the 3rd generator 12 and have cryogen liquid Pipeline is connected through the 4th generator 17, heat exchanger 16, the second generator 2 and second throttle 13 with evaporator 6, and the second heat is handed over Parallel operation 21 also has heated medium pipeline to be connected with outside.
(2) in flow, refrigerant vapour and cryogen liquid that the 3rd generator 12 produces are supplied to the 4th generator 17 to drive Thermal medium, the weak solution of the second absorber 4 enter the 4th generator 17, cryogen through 8 and second solution heat exchanger 11 of solution pump The solution that steam and cryogen liquid stream enter in it through the 4th generator 17, heating discharges refrigerant vapour and is provided to condenser 5, the The concentrated solution of four generators 17 enters the 3rd generator 12 through the 4th solution pump 19 and the 4th solution heat exchanger 20, and the 3rd occurs The concentrated solution of device 12 enters generator 1 through the 3rd solution pump 14 and the 3rd solution heat exchanger 15, and the concentrated solution of generator 1 is through the Three solution heat exchangers 15, the 4th solution heat exchanger 20 and the second solution heat exchanger 11 enter the second generator 2；Flow through The refrigerant vapour heat release of four generators 17 into after cryogen liquid followed by 21 and second generator 2 of second heat exchanger and progressively Heat release cools down, and the cryogen liquid after cooling down enters evaporator 6 through the throttling of the 3rd throttle valve 18；The cryogen liquid of 3rd generator 12 according to Secondary to flow through the 4th generator 17,16 and second generator of heat exchanger, 2 heat release cooling, the cryogen liquid after cooling down is through the second throttling The throttling of valve 13 enters evaporator 6, forms the 4th class absorption heat pump.
What the 4th class absorption heat pump shown in Fig. 8 was realized in：
(1) in structure, it mainly by generator, the second generator, absorber, the second absorber, condenser, evaporator, Throttle valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, the 3rd generator, the 3rd solution pump, 3rd solution heat exchanger and the 3rd absorber are formed；Absorber 3 has weak solution pipeline through solution heat exchanger 10 and second Absorber 4 connects, and the second absorber 4 also has weak solution pipeline to be absorbed through 8 and second solution heat exchanger 11 and the 3rd of solution pump Device 22 connects, and the 3rd absorber 22 also has weak solution pipeline through the 3rd solution pump 14 and the 3rd solution heat exchanger 15 and generator 1 connection, generator 1 also have concentrated solution pipeline to be connected through the 3rd solution heat exchanger 15 with the 3rd generator 12, the 3rd generator 12 also have concentrated solution pipeline to be connected through the second solution heat exchanger 11 with the second generator 2, and the second generator 2 also has concentrated solution pipe The second solution pump of road 9 and solution heat exchanger 10 are connected with absorber 3, and generator 1 also has refrigerant steam channel and condenser 5 Connection, the second generator 2 also have refrigerant steam channel to be connected with the second absorber 4, and the 3rd generator 12 also has refrigerant vapour to lead to Road is connected with the 3rd absorber 22, condenser 5 also have cryogen liquid pipeline connected with the second generator 2 after the second generator 2 again There is cryogen liquid pipeline to be connected through throttle valve 7 with evaporator 6, evaporator 6 also has refrigerant steam channel to be connected with absorber 3, occurs 1 and the 3rd generator 12 of device also has driving heat medium pipeline to be connected with outside respectively, absorber 3,5 and the 3rd absorber of condenser 22 also have heated medium pipeline connect with outside respectively, and the medium pipeline that also has surplus heat of evaporator 6 is connected with exterior, the second absorption Device 4 also has cooling medium pipeline to be connected with outside.
(2) in flow, the weak solution of absorber 3 enters the second absorber 4 through solution heat exchanger 10, absorbs refrigerant vapour And heat release enters the 3rd through 8 and second solution heat exchanger 11 of solution pump and absorbs in cooling medium, the weak solution of the second absorber 4 Device 22, absorbing refrigerant vapour, simultaneously heat release is in heated medium, and the weak solution of the 3rd absorber 22 is through the 3rd solution pump 14 and the 3rd Solution heat exchanger 15 enters generator 1, and the solution release cryogen that driving thermal medium flows through generator 1, heating enters in it steams Vapour is simultaneously provided to condenser 5, and the concentrated solution of generator 1 enters the 3rd generator 12, driving heat through the 3rd solution heat exchanger 15 The solution that medium flows through the 3rd generator 12, heating enters in it discharges refrigerant vapour and is provided to the 3rd absorber 22, the 3rd The concentrated solution of generator 12 enters the second generator 2, heat absorption release refrigerant vapour and to second through the second solution heat exchanger 11 Absorber 4 provides, and the concentrated solution of the second generator 2 enters absorber 3 through the second solution pump 9 and solution heat exchanger 10, absorbs Refrigerant vapour and heat release are in heated medium；The refrigerant vapour heat release of condenser 5 is in heated medium into cryogen liquid, cryogen liquid stream Again through the throttling of throttle valve 7 into evaporator 6, heat absorption into refrigerant vapour and to absorber 3 after 2 heat release of the second generator cooling There is provided, form the 4th class absorption heat pump.
What the 4th class absorption heat pump shown in Fig. 9 was realized in：
(1) in structure, in the 4th class absorption heat pump shown in Fig. 8, the 4th generator of increase, second throttle, the 4th Solution pump, the 4th solution heat exchanger and heat exchanger, the 3rd absorber 22 add weak solution pipeline through 19 He of the 4th solution pump 4th solution heat exchanger 20 is connected with the 4th generator 17, and the 4th generator 17 also has concentrated solution pipeline through the 4th generator 20 Connected with the 3rd generator 12, there is refrigerant steam channel to connect with condenser 5 in generator 1 and be adjusted to generator 1 and have cryogen steaming The 4th generator 17 has cryogen liquid pipeline through heat exchanger 16, the second generator again after vapour passage is connected with the 4th generator 17 2 and second throttle 13 connected with evaporator 6, the 4th generator 17 also have refrigerant steam channel connected with condenser 5, heat exchange Device 16 also has heated medium pipeline to be connected with outside.
(2) in flow, the refrigerant vapour that generator 1 produces is supplied to the 4th generator 17 to make driving thermal medium, and the 3rd inhales The part weak solution for receiving device 22 enters the 4th generator 17, refrigerant vapour through the 4th solution pump 19 and the 4th solution heat exchanger 20 The 4th generator 17, heating are flowed through into the solution release refrigerant vapour in it and is provided to condenser 5, the 4th generator 17 Concentrated solution enters the 3rd generator 12 through the 4th solution heat exchanger 20；Flow through the refrigerant vapour heat release Cheng Leng of the 4th generator 17 Followed by 16 and second generator 2 of heat exchanger and progressively heat release cools down after agent liquid, and the cryogen liquid after cooling is saved through second The stream throttling of valve 13 enters evaporator 6, forms the 4th class absorption heat pump.
What the 4th class absorption heat pump shown in Figure 10 was realized in：
(1) in structure, in the 4th class absorption heat pump shown in Fig. 8, the 4th generator of increase, second throttle, the 4th Solution heat exchanger and heat exchanger, have weak solution pipeline to be handed over through the 3rd solution pump 14 and the 3rd solution heat the 3rd absorber 22 Parallel operation 15 connected with generator 1 be adjusted to the 3rd absorber 22 have weak solution pipeline through the 3rd solution pump 14, the 3rd solution heat hand over 15 and the 4th solution heat exchanger 20 of parallel operation is connected with generator 1, and generator 1 is had concentrated solution pipeline through the 3rd solution heat exchange Device 15 is connected with the 3rd generator 12 to be adjusted to generator 1 and has concentrated solution pipeline to occur through the 4th solution heat exchanger 20 and the 4th Device 17 connects, and the 4th generator 17 has concentrated solution pipeline to be connected through the 3rd solution heat exchanger 15 with the 3rd generator 12 again, will Generator 1 has refrigerant steam channel to connect with condenser 5 to be adjusted to generator 1 and have refrigerant steam channel with the 4th generator 17 to connect 4th generator 17 has cryogen liquid pipeline through heat exchanger 16, the second generator 2 and second throttle 13 and evaporation again after logical Device 6 connects, and the 4th generator 17 also has refrigerant steam channel to be connected with condenser 5, and the 4th generator 17, which also has, drives thermal medium Pipeline is connected with outside, and heat exchanger 16 also has heated medium pipeline to be connected with outside.
(2) in flow, drive the refrigerant vapour that thermal medium and generator 1 produce to be provided to the 4th generator 17 and drive heat negative Lotus, the weak solution of the 3rd absorber 22 is through the 3rd solution pump 14, the 3rd solution heat exchanger 15 and the 4th solution heat exchanger 20 Into generator 1, the concentrated solution of generator 1 enters the 4th generator 17, refrigerant vapour and drive through the 4th solution heat exchanger 20 The solution that dynamic thermal medium flows through the 4th generator 17, heating enters in it discharges refrigerant vapour and is provided to condenser 5, the 4th hair The concentrated solution of raw device 17 enters the 3rd generator 12 through the 3rd solution heat exchanger 15；Flow through the refrigerant vapour of the 4th generator 17 Heat release into after cryogen liquid followed by 16 and second generator 2 of heat exchanger and progressively heat release cooling, the cryogen liquid after cooling Enter evaporator 6 through the throttling of second throttle 13, form the 4th class absorption heat pump.
What the 4th class absorption heat pump shown in Figure 11 was realized in：
(1) in structure, in the 4th class absorption heat pump shown in Fig. 8, the 4th generator of increase, second throttle, the 4th Solution pump, the 4th solution heat exchanger and heat exchanger, have weak solution pipeline through 14 He of the 3rd solution pump by the 3rd absorber 22 3rd solution heat exchanger 15 connected with generator 1 be adjusted to the 3rd absorber 22 have weak solution pipeline through the 3rd solution pump 14 and 3rd solution heat exchanger 15 is connected with the 4th generator 17, and the 4th generator 17 also has concentrated solution pipeline through the 4th solution pump 19 Connected with the 4th solution heat exchanger 20 with generator 1, by generator 1 have concentrated solution pipeline through the 3rd solution heat exchanger 15 with The connection of 3rd generator 12, which is adjusted to generator 1, has concentrated solution pipeline through the 4th solution heat exchanger 20 and the 3rd solution heat exchange Device 15 is connected with the 3rd generator 12, by generator 1 have refrigerant steam channel connect with condenser 5 be adjusted to generator 1 have it is cold The 4th generator 17 has cryogen liquid pipeline to be sent out through heat exchanger 16, second again after agent steam channel is connected with the 4th generator 17 Raw device 2 and second throttle 13 are connected with evaporator 6, and the 4th generator 17 also has refrigerant steam channel to be connected with condenser 5, heat Exchanger 16 also has heated medium pipeline to be connected with outside.
(2) in flow, the refrigerant vapour that generator 1 produces is supplied to the 4th generator 17 to make driving thermal medium, and the 3rd inhales The weak solution for receiving device 22 enters the 4th generator 17 through the 3rd solution pump 14 and the 3rd solution heat exchanger 15, and refrigerant vapour flows through The solution release that 4th generator 17, heating enter in it and provides refrigerant vapour to condenser 5, the 4th generator 17 it is dense molten Liquid enters generator 1 through the 4th solution pump 19 and the 4th solution heat exchanger 20, and the concentrated solution of generator 1 is handed over through the 4th solution heat 20 and the 3rd solution heat exchanger 15 of parallel operation enters the 3rd generator 12；Flow through the refrigerant vapour heat release Cheng Leng of the 4th generator 17 Followed by 16 and second generator 2 of heat exchanger and progressively heat release cools down after agent liquid, and the cryogen liquid after cooling is saved through second The stream throttling of valve 13 enters evaporator 6, forms the 4th class absorption heat pump.
What the 4th class absorption heat pump shown in Figure 12 was realized in：
(1) in structure, in the 4th class absorption heat pump shown in Fig. 1, increase newly-increased generator, newly-increased absorber, increase newly Solution pump and newly-increased solution heat exchanger, have weak solution pipeline to connect through solution heat exchanger 10 and the second absorber 4 absorber 3 The logical absorber 3 that is adjusted to has weak solution pipeline to be connected through newly-increased solution heat exchanger D with newly-increased absorber B, increases absorber B newly again There is weak solution pipeline to be connected through newly-increased solution pump C and solution heat exchanger 10 with the second absorber 4, the second generator 2 is had dense Solution line is connected through the second solution pump 9 and solution heat exchanger 10 with absorber 3 to be adjusted to the second generator 2 and has concentrated solution pipe Road is connected through solution heat exchanger 10 with newly-increased generator A, and newly-increased generator A has concentrated solution pipeline through 9 He of the second solution pump again Newly-increased solution heat exchanger D is connected with absorber 3, and newly-increased generator A also has refrigerant steam channel to be connected with newly-increased absorber B, There is cryogen liquid pipeline to connect with evaporator 6 through throttle valve 7 in second generator 2 to be adjusted to the second generator 2 and have cryogen liquid pipeline Newly-increased generator A has cryogen liquid pipeline to be connected through throttle valve 7 with evaporator 6 again after being connected with newly-increased generator A, increases newly and absorbs Device B also has cooling medium pipeline to be connected with outside.
(2) in flow, the weak solution of absorber 3 enters newly-increased absorber B through newly-increased solution heat exchanger D, absorbs cryogen Simultaneously heat release in cooling medium, increases the weak solution of absorber B newly through increasing solution pump C and solution heat exchanger 10 newly into second to steam Absorber 4；The concentrated solution of second generator 2 enters newly-increased generator A, heat absorption release refrigerant vapour simultaneously through solution heat exchanger 10 There is provided to newly-increased absorber B, the concentrated solution for increasing generator A newly enters absorption through the second solution pump 9 and newly-increased solution heat exchanger D Device 3；Followed by the second generator 2 and newly-increased generator A and progressively heat release cools down the cryogen liquid of condenser 5, after cooling down Cryogen liquid enters evaporator 6 through the throttling of throttle valve 7, forms the 4th class absorption heat pump.
What the 4th class absorption heat pump shown in Figure 13 was realized in：
(1) in structure, in the 4th class absorption heat pump shown in Fig. 2, increase newly-increased generator, newly-increased absorber, increase newly Solution pump and newly-increased solution heat exchanger, have weak solution pipeline to connect through solution heat exchanger 10 and the second absorber 4 absorber 3 The logical absorber 3 that is adjusted to has weak solution pipeline to be connected through newly-increased solution heat exchanger D with newly-increased absorber B, increases absorber B newly again There is weak solution pipeline to be connected through newly-increased solution pump C and solution heat exchanger 10 with the second absorber 4, the second generator 2 is had dense Solution line is connected through the second solution pump 9 and solution heat exchanger 10 with absorber 3 to be adjusted to the second generator 2 and has concentrated solution pipe Road is connected through solution heat exchanger 10 with newly-increased generator A, and newly-increased generator A has concentrated solution pipeline through 9 He of the second solution pump again Newly-increased solution heat exchanger D is connected with absorber 3, and newly-increased generator A also has refrigerant steam channel to be connected with newly-increased absorber B, There is cryogen liquid pipeline to connect with evaporator 6 through throttle valve 7 in second generator 2 to be adjusted to the second generator 2 and have cryogen liquid pipeline Newly-increased generator A has cryogen liquid pipeline to be connected through throttle valve 7 with evaporator 6 again after being connected with newly-increased generator A, by the second hair Raw device 2 has cryogen liquid pipeline connect with evaporator 6 through second throttle 13 to be adjusted to the second generator 2 and have cryogen liquid pipeline and newly Newly-increased generator A has cryogen liquid pipeline to be connected through second throttle 13 with evaporator 6 again after increasing generator A connections, increases newly and inhales Receiving device B also has cooling medium pipeline to be connected with outside.
(2) in flow, the weak solution of absorber 3 enters newly-increased absorber B through newly-increased solution heat exchanger D, absorbs cryogen Simultaneously heat release in cooling medium, increases the weak solution of absorber B newly through increasing solution pump C and solution heat exchanger 10 newly into second to steam Absorber 4；The concentrated solution of second generator 2 enters newly-increased generator A, heat absorption release refrigerant vapour simultaneously through solution heat exchanger 10 There is provided to newly-increased absorber B, the concentrated solution for increasing generator A newly enters absorption through the second solution pump 9 and newly-increased solution heat exchanger D Device 3；Followed by the second generator 2 and newly-increased generator A and progressively heat release cools down the cryogen liquid of condenser 5, after cooling down Cryogen liquid enters evaporator 6 through the throttling of throttle valve 7；The cryogen liquid that 3rd generator 12 produces is followed by heat exchanger 16, the Two generators 2 and newly-increased generator A and progressively heat release cool down, and the cryogen liquid after cooling down throttles to enter through second throttle 13 to be steamed Device 6 is sent out, forms the 4th class absorption heat pump.
What the 4th class absorption heat pump shown in Figure 14 was realized in：
(1) in structure, in the 4th class absorption heat pump shown in Fig. 5, increase newly-increased generator, newly-increased absorber, increase newly Solution pump and newly-increased solution heat exchanger, have weak solution pipeline to connect through solution heat exchanger 10 and the second absorber 4 absorber 3 The logical absorber 3 that is adjusted to has weak solution pipeline to be connected through newly-increased solution heat exchanger D with newly-increased absorber B, increases absorber B newly again There is weak solution pipeline to be connected through newly-increased solution pump C and solution heat exchanger 10 with the second absorber 4, the second generator 2 is had dense Solution line is connected through the second solution pump 9 and solution heat exchanger 10 with absorber 3 to be adjusted to the second generator 2 and has concentrated solution pipe Road is connected through solution heat exchanger 10 with newly-increased generator A, and newly-increased generator A has concentrated solution pipeline through 9 He of the second solution pump again Newly-increased solution heat exchanger D is connected with absorber 3, and newly-increased generator A also has refrigerant steam channel to be connected with newly-increased absorber B, There is cryogen liquid pipeline to connect with evaporator 6 through throttle valve 7 in second generator 2 to be adjusted to the second generator 2 and have cryogen liquid pipeline Newly-increased generator A has cryogen liquid pipeline to be connected through throttle valve 7 with evaporator 6 again after being connected with newly-increased generator A, by the second hair Raw device 2 has cryogen liquid pipeline connect with evaporator 6 through second throttle 13 to be adjusted to the second generator 2 and have cryogen liquid pipeline and newly Newly-increased generator A has cryogen liquid pipeline to be connected through second throttle 13 with evaporator 6 again after increasing generator A connections, by second Generator 2 have cryogen liquid pipeline connected through the 3rd throttle valve 18 with evaporator 6 be adjusted to the second generator 2 have cryogen liquid pipeline with Newly-increased generator A has cryogen liquid pipeline to be connected through the 3rd throttle valve 18 with evaporator 6 again after newly-increased generator A connections, increases newly Absorber B also has cooling medium pipeline to be connected with outside.
(2) in flow, the weak solution of absorber 3 enters newly-increased absorber B through newly-increased solution heat exchanger D, absorbs cryogen Simultaneously heat release in cooling medium, increases the weak solution of absorber B newly through increasing solution pump C and solution heat exchanger 10 newly into second to steam Absorber 4；The concentrated solution of second generator 2 enters newly-increased generator A, heat absorption release refrigerant vapour simultaneously through solution heat exchanger 10 There is provided to newly-increased absorber B, the concentrated solution for increasing generator A newly enters absorption through the second solution pump 9 and newly-increased solution heat exchanger D Device 3；Followed by the second generator 2 and newly-increased generator A and progressively heat release cools down the cryogen liquid of condenser 5, after cooling down Cryogen liquid enters evaporator 6 through the throttling of throttle valve 7；3rd generator 12 produce cryogen liquid followed by the 4th generator 17, Heat exchanger 16, the second generator 2 and newly-increased generator A and progressively heat release cool down, and the cryogen liquid after cooling down is through the second throttling The throttling of valve 13 enters evaporator 6；The cryogen liquid that 4th generator 17 produces is followed by second heat exchanger 21, the second generator 2 and newly-increased generator A and progressively heat release cool down, and the cryogen liquid after cooling down enters evaporator 6, shape through the throttling of the 3rd throttle valve 18 Into the 4th class absorption heat pump.
What the 4th class absorption heat pump shown in Figure 15 was realized in：
(1) in structure, in the 4th class absorption heat pump shown in Fig. 1, increase newly-increased generator, newly-increased absorber, increase newly Solution pump and newly-increased solution heat exchanger, have refrigerant steam channel to connect with absorber 3 evaporator 6 and are adjusted to evaporator 6 and have Refrigerant steam channel is connected with newly-increased absorber B, and newly-increased absorber B also has weak solution pipeline through newly-increased solution pump C and new solubilising Liquid heat exchanger D is connected with newly-increased generator A, newly-increased generator A also have concentrated solution pipeline through newly-increased solution heat exchanger D with it is new Increase absorber B connections, newly-increased generator A also has refrigerant steam channel to be connected with absorber 3, increases generator A newly and also drives heat Medium pipeline is connected with outside, and newly-increased absorber B also has heated medium pipeline to be connected with outside.
(2) in flow, the refrigerant vapour that evaporator 6 produces enters newly-increased absorber B, increases the weak solution warp of absorber B newly Newly-increased solution pump C and newly-increased solution heat exchanger D enters newly-increased generator A, and driving thermal medium flows through newly-increased generator A, heating Solution in into it discharges refrigerant vapour and is provided to absorber 3, increases the concentrated solution of generator A newly through new solubilization liquid heat exchange Device D enters newly-increased absorber B, absorbs refrigerant vapour and heat release is in heated medium, forms the 4th class absorption heat pump.
What the 4th class absorption heat pump shown in Figure 16 was realized in：
(1) in structure, in the 4th class absorption heat pump shown in Fig. 1, increase newly-increased generator, newly-increased absorber, increase newly Solution pump and newly-increased solution heat exchanger, have refrigerant steam channel to connect with condenser 5 in generator 1 and are adjusted to generator 1 and have Refrigerant steam channel is connected with newly-increased absorber B, and newly-increased absorber B also has weak solution pipeline through newly-increased solution pump C and new solubilising Liquid heat exchanger D is connected with newly-increased generator A, newly-increased generator A also have concentrated solution pipeline through newly-increased solution heat exchanger D with it is new Increase absorber B connections, newly-increased generator A also has refrigerant steam channel to be connected with condenser 5, increases generator A newly and also drives heat Medium pipeline is connected with outside, and newly-increased absorber B also has heated medium pipeline to be connected with outside.
(2) in flow, the refrigerant vapour that generator 1 produces enters newly-increased absorber B, increases the weak solution warp of absorber B newly Newly-increased solution pump C and newly-increased solution heat exchanger D enters newly-increased generator A, and driving thermal medium flows through newly-increased generator A, heating Solution in into it discharges refrigerant vapour and is provided to condenser 5, increases the concentrated solution of generator A newly through new solubilization liquid heat exchange Device D enters newly-increased absorber B, absorbs refrigerant vapour and heat release is in heated medium, forms the 4th class absorption heat pump.
What the 4th class absorption heat pump shown in Figure 17 was realized in：
(1) in structure, in the 4th class absorption heat pump shown in Fig. 1, the cooling that the second absorber 4 is connected with outside is cancelled Medium pipeline, by the second generator 2 have cryogen liquid pipeline connected with evaporator 6 through throttle valve 7 be adjusted to the second generator 2 have it is cold Agent liquid pipeline is connected through 7 and second absorber 4 of throttle valve with evaporator 6.
(2) in flow, the cryogen liquid stream of condenser 5 throttles through throttle valve 7 again after 2 heat release of the second generator cooling to drop Pressure, cryogen liquid stream enter evaporator 6 after being vaporized through the heat absorption of the second absorber 4 and part, form the 4th class absorption heat pump.
The 4th class absorption heat pump shown in Figure 18 is used to freeze what is be realized in：
(1) in structure, in the 4th class absorption heat pump shown in Fig. 1, increase circulating pump, cancel the second absorber 4 with it is outer The cooling medium pipeline of portion's connection, circulating pump E have circulatory mediator pipeline to be steamed after being sequentially communicated the second absorber 4 and evaporator 6 Hair device 6 connects shape with circulating pump E by circulatory mediator pipeline again and forms circulation loop.
(2) in flow, circulating thermal medium flows through the second absorber 4 and absorbs heat, and passes through 6 heat release of evaporator and enters circulation afterwards E is pumped, forms the 4th class absorption heat pump.
What the 5th class absorption heat pump shown in Figure 19 was realized in：
(1) in structure, in the 4th class absorption heat pump shown in Fig. 1, newly-increased generator, newly-increased absorber, new solubilising are added Liquid pump and newly-increased solution heat exchanger, have weak solution pipeline to be connected through solution heat exchanger 10 with the second absorber 4 absorber 3 Being adjusted to absorber 3 has weak solution pipeline to be connected through newly-increased solution heat exchanger D with newly-increased absorber B, and newly-increased absorber B has again Weak solution pipeline is connected through newly-increased solution pump C and solution heat exchanger 10 with the second absorber 4, the second generator 2 is had dense molten Liquid pipeline is connected through the second solution pump 9 and solution heat exchanger 10 with absorber 3 to be adjusted to the second generator 2 and has concentrated solution pipeline Connected through solution heat exchanger 10 with newly-increased generator A, newly-increased generator A has concentrated solution pipeline through the second solution pump 9 and new again Solubilized liquid heat exchanger D is connected with absorber 3, and newly-increased generator A also has refrigerant steam channel to be connected with newly-increased absorber B, newly Increase the generator A medium pipelines that also have surplus heat connect with exterior, newly-increased absorber B also has cooling medium pipeline to connect with exterior.
(1) in structure, the weak solution of absorber 3 enters newly-increased absorber B through newly-increased solution heat exchanger D, absorbs cryogen Simultaneously heat release in cooling medium, increases the weak solution of absorber B newly through increasing solution pump C and solution heat exchanger 10 newly into second to steam Absorber 4；The concentrated solution of second generator 2 enters newly-increased generator A through solution heat exchanger 10, and waste heat medium flows through newly-increased hair The solution that raw device A, heating enter in it discharges refrigerant vapour and is provided to newly-increased absorber B, increases the concentrated solution warp of generator A newly Second solution pump 9 and newly-increased solution heat exchanger D enter absorber 3, form the 5th class absorption heat pump.
What the 5th class absorption heat pump shown in Figure 20 was realized in：
In the 4th class absorption heat pump shown in Fig. 1, the second generator 2 is added waste heat medium pipeline and is connected with outside；It is cold Agent liquid and waste heat medium provide driving thermic load to the second generator 2 jointly, form the 5th class absorption heat pump.
What the 5th class absorption heat pump shown in Figure 21 was realized in：
(1) in structure, in the 4th class absorption heat pump shown in Fig. 1, increase newly-increased generator, newly-increased absorber, increase newly Solution pump and newly-increased solution heat exchanger, have refrigerant steam channel to be connected with the second absorber 4 in second generator 2 and are adjusted to Two generators 2 have refrigerant steam channel to be connected with newly-increased absorber B, and newly-increased absorber B also has weak solution pipeline through new solubilization liquid Pump C and newly-increased solution heat exchanger D is connected with newly-increased generator A, and newly-increased generator A also has concentrated solution pipeline through new solubilization liquid heat Exchanger D is connected with newly-increased absorber B, and newly-increased generator A also has refrigerant steam channel to be connected with the second absorber 4, new additional issue The raw device A medium pipelines that also have surplus heat connects with exterior, and newly-increased absorber B also has cooling medium pipeline to be connected with exterior.
(2) in flow, the refrigerant vapour that the second generator 2 produces enters newly-increased absorber B, increases the dilute molten of absorber B newly Liquid enters newly-increased generator A through newly-increased solution pump C and newly-increased solution heat exchanger D, and waste heat medium flows through newly-increased generator A, adds The solution that heat enters in it discharges refrigerant vapour and is provided to the second absorber 4, increases the concentrated solution of generator A newly through new solubilization liquid Heat exchanger D enters newly-increased absorber B, absorbs refrigerant vapour and heat release is in cooling medium, forms the 5th class absorption heat pump.
The effect that the technology of the present invention can be realized --- the 4th class absorption heat pump proposed by the invention and the 5th class are inhaled Receipts formula heat pump, has the effect that and advantage：
(1) new approaches, new concept and new technology that the temperature difference utilizes are proposed, the further of absorption heat pump technology will be promoted Development and application.
(2) negative effect of the high temperature cryogen liquid to UTILIZATION OF VESIDUAL HEAT IN degree can be solved well, especially to TFE-TDE Solution is the absorption heat pump flow of Typical Representative, can significantly improve the performance index and utilization rate of waste heat of absorption heat pump.
(3) temperature difference producing level is expanded under low temperature cold environment or heated medium temperature, further increases temperature Difference utilizes level, and to playing the role of suppressing and making up because performance index caused by cryogen liquid to Environment release thermal energy reduces.
(4) it can reduce to driving heat medium temperature requirement, or improve the degree of UTILIZATION OF VESIDUAL HEAT IN, or more low temperature can be utilized The residual heat resources of degree.
(5) a variety of concrete technical schemes are provided, numerous different actual states is coped with, there is the wider scope of application.
(6) type of absorption heat pump is enriched, extends the application range of absorption heat pump, is conducive to preferably use Absorption heat pump realizes making full use of for the temperature difference.

Claims (51)

1. the 4th class absorption heat pump, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporation Device, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger are formed；Absorber (3) has Weak solution pipeline is connected through solution heat exchanger (10) with the second absorber (4), and the second absorber (4) also has weak solution pipeline warp Solution pump (8) and the second solution heat exchanger (11) are connected with generator (1), and generator (1) also has concentrated solution pipeline through second Solution heat exchanger (11) is connected with the second generator (2), and the second generator (2) also has concentrated solution pipeline through the second solution pump (9) connected with solution heat exchanger (10) with absorber (3), generator (1) also has refrigerant steam channel to connect with condenser (5) Logical, the second generator (2) also has refrigerant steam channel to be connected with the second absorber (4), condenser (5) also have cryogen liquid pipeline and The second generator (2) has cryogen liquid pipeline to be connected through throttle valve (7) with evaporator (6) again after second generator (2) connection, steams Hair device (6) also has refrigerant steam channel to be connected with absorber (3), and generator (1), which also has, drives heat medium pipeline to be connected with outside, Absorber (3) and condenser (5) also have heated medium pipeline to be connected with outside respectively, and evaporator (6) also has surplus heat medium tube Road is connected with outside, and the second absorber (4) also has cooling medium pipeline to be connected with outside, forms the 4th class absorption heat pump.
2. the 4th class absorption heat pump, it is in the 4th class absorption heat pump described in claim 1, cancels throttle valve, by the Two generators (2) have cryogen liquid pipeline to connect with evaporator (6) through throttle valve (7) to be adjusted to the second generator (2) and have cryogen liquid Pipeline is connected with evaporator (6), forms the 4th class absorption heat pump.
3. the 4th class absorption heat pump, be in the 4th class absorption heat pump described in claim 1, the 3rd generator of increase, Second throttle, the 3rd solution pump, the 3rd solution heat exchanger and heat exchanger, the second absorber (4) add weak solution pipeline Connected through the 3rd solution pump (14) and the 3rd solution heat exchanger (15) with the 3rd generator (12), the 3rd generator (12) also has Concentrated solution pipeline is connected through the 3rd solution heat exchanger (15) with the second generator (2), and generator (1) is had refrigerant steam channel Connected with condenser (5) be adjusted to generator (1) have refrigerant steam channel connected with the 3rd generator (12) after the 3rd occur Device (12) has cryogen liquid pipeline to connect through heat exchanger (16), the second generator (2) and second throttle (13) and evaporator (6) again Logical, the 3rd generator (12) also has refrigerant steam channel to be connected with condenser (5), and heat exchanger (16) also has heated medium pipe Road is connected with outside, forms the 4th class absorption heat pump.
4. the 4th class absorption heat pump, be in the 4th class absorption heat pump described in claim 1, the 3rd generator of increase, Second throttle, the 3rd solution heat exchanger and heat exchanger, have weak solution pipeline through solution pump (8) by the second absorber (4) Connected with the second solution heat exchanger (11) with generator (1) and be adjusted to the second absorber (4) and have weak solution pipeline through solution pump (8), the second solution heat exchanger (11) and the 3rd solution heat exchanger (15) are connected with generator (1), generator (1) are had dense Solution line is connected through the second solution heat exchanger (11) with the second generator (2) to be adjusted to generator (1) and has concentrated solution pipeline Connected through the 3rd solution heat exchanger (15) with the 3rd generator (12), the 3rd generator (12) has concentrated solution pipeline through second again Solution heat exchanger (11) is connected with the second generator (2), has refrigerant steam channel to be connected with condenser (5) in generator (1) Be adjusted to generator (1) have refrigerant steam channel connected with the 3rd generator (12) after the 3rd generator (12) have cryogen liquid again Pipeline is connected through heat exchanger (16), the second generator (2) and second throttle (13) with evaporator (6), the 3rd generator (12) refrigerant steam channel is connected with condenser (5), heat exchanger (16) also has heated medium pipeline to be connected with outside, Form the 4th class absorption heat pump.
5. the 4th class absorption heat pump, be in the 4th class absorption heat pump described in claim 1, the 3rd generator of increase, Second throttle, the 3rd solution pump, the 3rd solution heat exchanger and heat exchanger, have weak solution pipeline by the second absorber (4) Connected through solution pump (8) and the second solution heat exchanger (11) with generator (1) and be adjusted to the second absorber (4) and have weak solution pipe Road is connected through solution pump (8) and the second solution heat exchanger (11) with the 3rd generator (12), and the 3rd generator (12) has dense again Solution line is connected through the 3rd solution pump (14) and the 3rd solution heat exchanger (15) with generator (1), generator (1) is had dense Solution line is connected through the second solution heat exchanger (11) with the second generator (2) to be adjusted to generator (1) and has concentrated solution pipeline Connected through the 3rd solution heat exchanger (15) and the second solution heat exchanger (11) with the second generator (2), generator (1) is had Refrigerant steam channel is connected with condenser (5) to be adjusted to generator (1) and has refrigerant steam channel to be connected with the 3rd generator (12) The 3rd generator (12) has cryogen liquid pipeline through heat exchanger (16), the second generator (2) and second throttle (13) again afterwards Connected with evaporator (6), the 3rd generator (12) also has refrigerant steam channel to be connected with condenser (5), and heat exchanger (16) is also There is heated medium pipeline to be connected with outside, form the 4th class absorption heat pump.
6. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in claim 3-5, cancels throttle valve And second throttle, there is cryogen liquid pipeline to be connected through throttle valve (7) with evaporator (6) in the second generator (2) and be adjusted to second Generator (2) has cryogen liquid pipeline to be connected with evaporator (6), and the second generator (2) is had cryogen liquid pipeline through second throttle (13) connected with evaporator (6) and be adjusted to the second generator (2) and there is cryogen liquid pipeline to be connected with evaporator (6), form the 4th class Absorption heat pump.
7. the 4th class absorption heat pump, be in the 4th class absorption heat pump described in claim 3, the 4th generator of increase, 3rd throttle valve, the 4th solution pump, the 4th solution heat exchanger and second heat exchanger, the second absorber (4) add weak solution Pipeline is connected through the 4th solution pump (19) and the 4th solution heat exchanger (20) with the 4th generator (17), the 4th generator (17) Also concentrated solution pipeline is connected through the 4th solution heat exchanger (20) with the second generator (2), and the 4th generator (17) is also cold Agent steam channel is connected with condenser (5), is had refrigerant steam channel to be connected with condenser (5) in the 3rd generator (12) and is adjusted to 3rd generator (12) have refrigerant steam channel connected with the 4th generator (17) after the 4th generator (17) have cryogen liquid again Pipeline is connected through second heat exchanger (21), the second generator (2) and the 3rd throttle valve (18) with evaporator (6), by the 3rd hair Raw device (12) has cryogen liquid pipeline to connect through heat exchanger (16), the second generator (2) and second throttle (13) and evaporator (6) It is logical to be adjusted to the 3rd generator (12) and have cryogen liquid pipeline through the 4th generator (17), heat exchanger (16), the second generator (2) Being connected with second throttle (13) with evaporator (6), second heat exchanger (21) also has heated medium pipeline to be connected with outside, Form the 4th class absorption heat pump.
8. the 4th class absorption heat pump, be in the 4th class absorption heat pump described in claim 4, the 4th generator of increase, 3rd throttle valve, the 4th solution heat exchanger and second heat exchanger, have weak solution pipeline through solution pump by the second absorber (4) (8), the second solution heat exchanger (11) and the 3rd solution heat exchanger (15) connect with generator (1) and are adjusted to the second absorber (4) there is the weak solution pipeline molten through solution pump (8), the 4th solution heat exchanger (20), the second solution heat exchanger (11) and the 3rd Liquid heat exchanger (15) is connected with generator (1), and the 3rd generator (12) is had concentrated solution pipeline through the second solution heat exchanger (11) connected with the second generator (2) and be adjusted to the 3rd generator (12) and have concentrated solution pipeline through the second solution heat exchanger (11) Connected with the 4th generator (17), the 4th generator (17) has concentrated solution pipeline through the 4th solution heat exchanger (20) and second again Generator (2) connects, and the 4th generator (17) also has refrigerant steam channel to be connected with condenser (5), by the 3rd generator (12) There is refrigerant steam channel to connect with condenser (5) to be adjusted to the 3rd generator (12) and have refrigerant steam channel and the 4th generator (17) the 4th generator (17) has cryogen liquid pipeline through second heat exchanger (21), the second generator (2) and the again after connecting Three throttle valves (18) are connected with evaporator (6), and the 3rd generator (12) is had cryogen liquid pipeline through heat exchanger (16), the second hair Raw device (2) and second throttle (13) are connected with evaporator (6) to be adjusted to the 3rd generator (12) and has cryogen liquid pipeline through the 4th Generator (17), heat exchanger (16), the second generator (2) and second throttle (13) are connected with evaporator (6), and the second heat is handed over Parallel operation (21) also has heated medium pipeline to be connected with outside, forms the 4th class absorption heat pump.
9. the 4th class absorption heat pump, be in the 4th class absorption heat pump described in claim 5, the 4th generator of increase, 3rd throttle valve, the 4th solution pump, the 4th solution heat exchanger and second heat exchanger, have weak solution by the second absorber (4) Pipeline connects with the 3rd generator (12) through solution pump (8) and the second solution heat exchanger (11) and is adjusted to the second absorber (4) There is weak solution pipeline to be connected through solution pump (8) and the second solution heat exchanger (11) with the 4th generator (17), the 4th generator (17) concentrated solution pipeline is connected through the 4th solution pump (19) and the 4th solution heat exchanger (20) with the 3rd generator (12) again, There is concentrated solution pipeline to occur through the 3rd solution heat exchanger (15) and the second solution heat exchanger (11) with second in generator (1) Device (2) connection, which is adjusted to generator (1), has concentrated solution pipeline through the 3rd solution heat exchanger (15), the 4th solution heat exchanger (20) connected with the second solution heat exchanger (11) with the second generator (2), the 4th generator (17) also has refrigerant steam channel Connected with condenser (5), there is refrigerant steam channel to be connected with condenser (5) in the 3rd generator (12) and be adjusted to the 3rd generator (12) have refrigerant steam channel connected with the 4th generator (17) after the 4th generator (17) have cryogen liquid pipeline again through second Heat exchanger (21), the second generator (2) and the 3rd throttle valve (18) are connected with evaporator (6), and the 3rd generator (12) is had Cryogen liquid pipeline is connected through heat exchanger (16), the second generator (2) and second throttle (13) with evaporator (6) is adjusted to Three generators (12) have cryogen liquid pipeline through the 4th generator (17), heat exchanger (16), the second generator (2) and the second throttling Valve (13) is connected with evaporator (6), and second heat exchanger (21) also has heated medium pipeline to be connected with outside, forms the 4th class Absorption heat pump.
10. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in claim 7-9, cancels throttling Valve, second throttle and the 3rd throttle valve, have cryogen liquid pipeline to connect through throttle valve (7) and evaporator (6) in the second generator (2) It is logical to be adjusted to the second generator (2) and there is cryogen liquid pipeline to be connected with evaporator (6), the second generator (2) there is into cryogen liquid pipeline Connected through second throttle (13) with evaporator (6) be adjusted to the second generator (2) have cryogen liquid pipeline with evaporator (6) even It is logical, there is cryogen liquid pipeline to be connected through the 3rd throttle valve (18) with evaporator (6) in the second generator (2) and be adjusted to the second generator (2) there is cryogen liquid pipeline to be connected with evaporator (6), form the 4th class absorption heat pump.
11. the 4th class absorption heat pump, mainly by generator, the second generator, absorber, the second absorber, condenser, evaporation Device, throttle valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, the 3rd generator, the 3rd solution Pump, the 3rd solution heat exchanger and the 3rd absorber are formed；Absorber (3) has weak solution pipeline through solution heat exchanger (10) Connected with the second absorber (4), the second absorber (4) also has weak solution pipeline through solution pump (8) and the second solution heat exchanger (11) connected with the 3rd absorber (22), the 3rd absorber (22) also has the weak solution pipeline molten through the 3rd solution pump (14) and the 3rd Liquid heat exchanger (15) is connected with generator (1), generator (1) also have concentrated solution pipeline through the 3rd solution heat exchanger (15) with 3rd generator (12) connects, and the 3rd generator (12) also has concentrated solution pipeline through the second solution heat exchanger (11) and the second hair Raw device (2) connection, the second generator (2) also have concentrated solution pipeline through the second solution pump (9) and solution heat exchanger (10) with inhaling Device (3) connection is received, generator (1) also has refrigerant steam channel to be connected with condenser (5), and the second generator (2) also has cryogen steaming Vapour passage is connected with the second absorber (4), and the 3rd generator (12) also has refrigerant steam channel to be connected with the 3rd absorber (22), Condenser (5) also have cryogen liquid pipeline connected with the second generator (2) after the second generator (2) have cryogen liquid pipeline warp knuckle again Stream valve (7) is connected with evaporator (6), and evaporator (6) also has refrigerant steam channel to be connected with absorber (3), generator (1) and the Three generators (12) also have driving heat medium pipeline to be connected with outside respectively, absorber (3), condenser (5) and the 3rd absorber (22) heated medium pipeline also connect with outside respectively, evaporator (6) medium pipeline that also has surplus heat is connected with exterior, and second Absorber (4) also has cooling medium pipeline to be connected with outside, forms the 4th class absorption heat pump.
, will 12. the 4th class absorption heat pump, is in the 4th class absorption heat pump described in claim 11, cancels throttle valve Second generator (2) has cryogen liquid pipeline to connect with evaporator (6) through throttle valve (7) to be adjusted to the second generator (2) and have cryogen Liquid pipeline is connected with evaporator (6), forms the 4th class absorption heat pump.
13. the 4th class absorption heat pump, is in the 4th class absorption heat pump described in claim 11, increase the 4th occurs Device, second throttle, the 4th solution pump, the 4th solution heat exchanger and heat exchanger, the 3rd absorber (22) add weak solution Pipeline is connected through the 4th solution pump (19) and the 4th solution heat exchanger (20) with the 4th generator (17), the 4th generator (17) Also concentrated solution pipeline is connected through the 4th generator (20) with the 3rd generator (12), and generator (1) is had refrigerant steam channel Connected with condenser (5) be adjusted to generator (1) have refrigerant steam channel connected with the 4th generator (17) after the 4th occur Device (17) has cryogen liquid pipeline to connect through heat exchanger (16), the second generator (2) and second throttle (13) and evaporator (6) again Logical, the 4th generator (17) also has refrigerant steam channel to be connected with condenser (5), and heat exchanger (16) also has heated medium pipe Road is connected with outside, forms the 4th class absorption heat pump.
14. the 4th class absorption heat pump, is in the 4th class absorption heat pump described in claim 11, increase the 4th occurs Device, second throttle, the 4th solution heat exchanger and heat exchanger, have the weak solution pipeline molten through the 3rd the 3rd absorber (22) Liquid pump (14) and the 3rd solution heat exchanger (15) are connected with generator (1) to be adjusted to the 3rd absorber (22) and has weak solution pipeline Connected through the 3rd solution pump (14), the 3rd solution heat exchanger (15) and the 4th solution heat exchanger (20) with generator (1), will Generator (1) has concentrated solution pipeline to connect with the 3rd generator (12) through the 3rd solution heat exchanger (15) to be adjusted to generator (1) concentrated solution pipeline is connected through the 4th solution heat exchanger (20) with the 4th generator (17), the 4th generator (17) has again Concentrated solution pipeline is connected through the 3rd solution heat exchanger (15) with the 3rd generator (12), has refrigerant vapour to lead in generator (1) Road connected with condenser (5) be adjusted to generator (1) have refrigerant steam channel connected with the 4th generator (17) after the 4th hair Raw device (17) has cryogen liquid pipeline through heat exchanger (16), the second generator (2) and second throttle (13) and evaporator (6) again Connection, the 4th generator (17) also have refrigerant steam channel to be connected with condenser (5), and heat exchanger (16) also has heated medium Pipeline is connected with outside, forms the 4th class absorption heat pump.
15. the 4th class absorption heat pump, is in the 4th class absorption heat pump described in claim 11, increase the 4th occurs Device, second throttle, the 4th solution pump, the 4th solution heat exchanger and heat exchanger, have weak solution by the 3rd absorber (22) Pipeline connects with generator (1) through the 3rd solution pump (14) and the 3rd solution heat exchanger (15) and is adjusted to the 3rd absorber (22) There is weak solution pipeline to be connected through the 3rd solution pump (14) and the 3rd solution heat exchanger (15) with the 4th generator (17), the 4th hair Raw device (17) also has concentrated solution pipeline to be connected through the 4th solution pump (19) and the 4th solution heat exchanger (20) with generator (1), There is concentrated solution pipeline to be connected through the 3rd solution heat exchanger (15) with the 3rd generator (12) in generator (1) and be adjusted to generator (1) concentrated solution pipeline connects through the 4th solution heat exchanger (20) and the 3rd solution heat exchanger (15) with the 3rd generator (12) It is logical, there is refrigerant steam channel to connect with condenser (5) in generator (1) and be adjusted to generator (1) and have refrigerant steam channel and the The 4th generator (17) has cryogen liquid pipeline through heat exchanger (16), the second generator (2) again after four generators (17) connection Connected with second throttle (13) with evaporator (6), the 4th generator (17) also has refrigerant steam channel to connect with condenser (5) Logical, heat exchanger (16) also has heated medium pipeline to be connected with outside, forms the 4th class absorption heat pump.
16. the 4th class absorption heat pump, is the 4th hair in any 4th class absorption heat pump described in claim 13-15 Raw device (17) is added driving heat medium pipeline and is connected with outside, forms the 4th class absorption heat pump.
17. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in claim 13-16, cancels section Valve and second throttle are flowed, has cryogen liquid pipeline to be connected through throttle valve (7) with evaporator (6) in the second generator (2) and is adjusted to Second generator (2) has cryogen liquid pipeline to be connected with evaporator (6), and the second generator (2) is had cryogen liquid pipeline through the second section Stream valve (13) is connected with evaporator (6) to be adjusted to the second generator (2) and has cryogen liquid pipeline to be connected with evaporator (6), formation the Four class absorption heat pumps.
18. the 4th class absorption heat pump, is in the 4th class absorption heat pump described in claim 1 or claim 11, increases Add newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, absorber (3) is had into weak solution pipeline Connected through solution heat exchanger (10) with the second absorber (4) and be adjusted to absorber (3) and have weak solution pipeline through new solubilization liquid heat Exchanger (D) is connected with newly-increased absorber (B), and newly-increased absorber (B) has weak solution pipeline through newly-increased solution pump (C) and solution again Heat exchanger (10) is connected with the second absorber (4), have concentrated solution pipeline through the second solution pump (9) in the second generator (2) and Solution heat exchanger (10) is connected with absorber (3) to be adjusted to the second generator (2) and has concentrated solution pipeline through solution heat exchanger (10) connected with newly-increased generator (A), newly-increased generator (A) has concentrated solution pipeline through the second solution pump (9) and new solubilization liquid again Heat exchanger (D) is connected with absorber (3), and newly-increased generator (A) also has refrigerant steam channel to be connected with newly-increased absorber (B), By the second generator (2) have cryogen liquid pipeline connected with evaporator (6) through throttle valve (7) be adjusted to the second generator (2) have it is cold Agent liquid pipeline increases generator (A) newly after being connected with newly-increased generator (A) has cryogen liquid pipeline through throttle valve (7) and evaporator again (6) connect, newly-increased absorber (B) also has cooling medium pipeline to be connected with outside, forms the 4th class absorption heat pump.
19. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in claim 18, cancels throttling Valve, has cryogen liquid pipeline to be connected with evaporator (6) through throttle valve (7) in newly-increased generator (A) and is adjusted to newly-increased generator (A) and has Cryogen liquid pipeline is connected with evaporator (6), forms the 4th class absorption heat pump.
20. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in claim 3-5,13-16, increases Add newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, absorber (3) is had into weak solution pipeline Connected through solution heat exchanger (10) with the second absorber (4) and be adjusted to absorber (3) and have weak solution pipeline through new solubilization liquid heat Exchanger (D) is connected with newly-increased absorber (B), and newly-increased absorber (B) has weak solution pipeline through newly-increased solution pump (C) and solution again Heat exchanger (10) is connected with the second absorber (4), have concentrated solution pipeline through the second solution pump (9) in the second generator (2) and Solution heat exchanger (10) is connected with absorber (3) to be adjusted to the second generator (2) and has concentrated solution pipeline through solution heat exchanger (10) connected with newly-increased generator (A), newly-increased generator (A) has concentrated solution pipeline through the second solution pump (9) and new solubilization liquid again Heat exchanger (D) is connected with absorber (3), and newly-increased generator (A) also has refrigerant steam channel to be connected with newly-increased absorber (B), By the second generator (2) have cryogen liquid pipeline connected with evaporator (6) through throttle valve (7) be adjusted to the second generator (2) have it is cold Agent liquid pipeline increases generator (A) newly after being connected with newly-increased generator (A) has cryogen liquid pipeline through throttle valve (7) and evaporator again (6) connect, there is cryogen liquid pipeline to be connected through second throttle (13) with evaporator (6) in the second generator (2) and be adjusted to second Generator (2) has cryogen liquid pipeline to increase generator (A) after being connected with newly-increased generator (A) newly has cryogen liquid pipeline through second again Throttle valve (13) is connected with evaporator (6), and newly-increased absorber (B) also has cooling medium pipeline to be connected with outside, forms the 4th class Absorption heat pump.
21. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in claim 20, cancels throttle valve And second throttle, there is cryogen liquid pipeline to be connected through throttle valve (7) with evaporator (6) in newly-increased generator (A) and be adjusted to newly-increased Generator (A) has cryogen liquid pipeline to be connected with evaporator (6), and newly-increased generator (A) is had cryogen liquid pipeline through second throttle (13) connected with evaporator (6) and be adjusted to newly-increased generator (A) and there is cryogen liquid pipeline to be connected with evaporator (6), the 4th class of formation Absorption heat pump.
22. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in claim 7-9, increase is newly-increased Generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, have weak solution pipeline through solution by absorber (3) Heat exchanger (10) is connected with the second absorber (4) to be adjusted to absorber (3) and has weak solution pipeline through newly-increased solution heat exchanger (D) connected with newly-increased absorber (B), newly-increased absorber (B) has weak solution pipeline through newly-increased solution pump (C) and solution heat exchange again Device (10) is connected with the second absorber (4), and the second generator (2) is had concentrated solution pipeline through the second solution pump (9) and solution heat Exchanger (10) connected with absorber (3) be adjusted to the second generator (2) have concentrated solution pipeline through solution heat exchanger (10) with Newly-increased generator (A) connection, newly-increased generator (A) have concentrated solution pipeline through the second solution pump (9) and new solubilization liquid heat exchange again Device (D) is connected with absorber (3), and newly-increased generator (A) also has refrigerant steam channel to be connected with newly-increased absorber (B), by second Generator (2) has cryogen liquid pipeline to connect with evaporator (6) through throttle valve (7) to be adjusted to the second generator (2) and have cryogen liquid pipe Road increases generator (A) newly after being connected with newly-increased generator (A) has cryogen liquid pipeline to connect through throttle valve (7) and evaporator (6) again It is logical, there is cryogen liquid pipeline to be connected through second throttle (13) with evaporator (6) in the second generator (2) and be adjusted to the second generator (2) have cryogen liquid pipeline to increase generator (A) after being connected with newly-increased generator (A) newly has cryogen liquid pipeline through second throttle again (13) connected with evaporator (6), there is cryogen liquid pipeline to connect through the 3rd throttle valve (18) and evaporator (6) in the second generator (2) It is logical to be adjusted to the second generator (2) and there is cryogen liquid pipeline connect with newly-increased generator (A) to increase generator (A) newly afterwards and have cryogen again Liquid pipeline is connected through the 3rd throttle valve (18) with evaporator (6), and newly-increased absorber (B) also has cooling medium pipeline to connect with outside It is logical, form the 4th class absorption heat pump.
23. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in claim 22, cancels throttling Valve, second throttle and the 3rd throttle valve, have cryogen liquid pipeline to connect through throttle valve (7) and evaporator (6) in newly-increased generator (A) It is logical to be adjusted to newly-increased generator (A) and there is cryogen liquid pipeline to be connected with evaporator (6), newly-increased generator (A) there is into cryogen liquid pipeline Connected through second throttle (13) with evaporator (6) be adjusted to newly-increased generator (A) have cryogen liquid pipeline with evaporator (6) even It is logical, there is cryogen liquid pipeline to be connected through the 3rd throttle valve (18) with evaporator (6) in newly-increased generator (A) and be adjusted to newly-increased generator (A) there is cryogen liquid pipeline to be connected with evaporator (6), form the 4th class absorption heat pump.
24. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in claim 1-17, increase is newly-increased Generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, have refrigerant steam channel with inhaling by evaporator (6) Receipts device (3) connection, which is adjusted to evaporator (6), has refrigerant steam channel to be connected with newly-increased absorber (B), increases absorber (B) newly and also has Weak solution pipeline is connected through newly-increased solution pump (C) and newly-increased solution heat exchanger (D) with newly-increased generator (A), increases generator newly (A) there is concentrated solution pipeline to be connected through newly-increased solution heat exchanger (D) with newly-increased absorber (B), it is also cold to increase generator (A) newly Agent steam channel is connected with absorber (3), and newly-increased generator (A), which also has, drives heat medium pipeline to be connected with outside, increases newly and absorbs Device (B) also has heated medium pipeline to be connected with outside, forms the 4th class absorption heat pump.
25. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in claim 18-23, increase is new Increase the second generator, newly-increased second absorber, newly-increased second solution pump and newly-increased second solution heat exchanger, by evaporator (6) There is refrigerant steam channel to connect with absorber (3) to be adjusted to evaporator (6) and there is refrigerant steam channel with newly-increased second absorber to connect Logical, newly-increased second absorber also has weak solution pipeline through newly-increased second solution pump and newly-increased second solution heat exchanger with increasing the newly Two generators connect, and newly-increased second generator also has concentrated solution pipeline to be absorbed through newly-increased second solution heat exchanger with newly-increased second Device connects, and newly-increased second generator also has refrigerant steam channel to be connected with absorber (3), increases the second generator newly and also has driving heat Medium pipeline is connected with outside, and newly-increased second absorber also has heated medium pipeline to be connected with outside, is formed the 4th class and is absorbed Formula heat pump.
26. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in claim 1-2,11-12, increases Add newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, there is refrigerant vapour to lead in generator (1) Road is connected with condenser (5) to be adjusted to generator (1) and has refrigerant steam channel to be connected with newly-increased absorber (B), increases absorber newly (B) there is weak solution pipeline to be connected through newly-increased solution pump (C) and newly-increased solution heat exchanger (D) with newly-increased generator (A), increase newly Generator (A) also has concentrated solution pipeline to be connected through newly-increased solution heat exchanger (D) with newly-increased absorber (B), increases generator (A) newly Also refrigerant steam channel is connected with condenser (5), and newly-increased generator (A), which also has, drives heat medium pipeline to be connected with outside, newly Increasing absorber (B) also has heated medium pipeline to be connected with outside, forms the 4th class absorption heat pump.
27. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in claim 18-19, increase is new Increase the second generator, newly-increased second absorber, newly-increased second solution pump and newly-increased second solution heat exchanger, by generator (1) There is refrigerant steam channel to connect with condenser (5) to be adjusted to generator (1) and there is refrigerant steam channel with newly-increased second absorber to connect Logical, newly-increased second absorber also has weak solution pipeline through newly-increased second solution pump and newly-increased second solution heat exchanger with increasing the newly Two generators connect, and newly-increased second generator also has concentrated solution pipeline to be absorbed through newly-increased second solution heat exchanger with newly-increased second Device connects, and newly-increased second generator also has refrigerant steam channel to be connected with condenser, increases the second generator newly and also has driving heat to be situated between Matter pipeline is connected with outside, and newly-increased second absorber also has heated medium pipeline to be connected with outside, forms the 4th kind absorption type Heat pump.
28. the 4th class absorption heat pump, is in the 4th class absorption heat pump described in claim 1 or claim 11, takes Disappear the cooling medium pipeline that the second absorber (4) is connected with outside, and the second generator (2) is had cryogen liquid pipeline through throttle valve (7) connected with evaporator (6) be adjusted to the second generator (2) have cryogen liquid pipeline through throttle valve (7) and the second absorber (4) with Evaporator (6) connects, and forms the 4th class absorption heat pump.
29. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in claim 3-5,13-16, takes Disappear the cooling medium pipeline that the second absorber (4) is connected with outside, and the second generator (2) is had cryogen liquid pipeline through throttle valve (7) connected with evaporator (6) be adjusted to the second generator (2) have cryogen liquid pipeline through throttle valve (7) and the second absorber (4) with Evaporator (6) connects, and has cryogen liquid pipeline to connect adjustment with evaporator (6) through second throttle (13) in the second generator (2) There is cryogen liquid pipeline to be connected through second throttle (13) and the second absorber (4) with evaporator (6) for the second generator (2), shape Into the 4th class absorption heat pump.
30. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in claim 3-5,13-16, takes Disappear the cooling medium pipeline that the second absorber (4) is connected with outside, and the second generator (2) is had cryogen liquid pipeline through throttle valve (7) connected with evaporator (6) be adjusted to the second generator (2) have cryogen liquid pipeline through throttle valve (7) and the second absorber (4) with Evaporator (6) connects, or has cryogen liquid pipeline to connect tune with evaporator (6) through second throttle (13) in the second generator (2) Whole is that the second generator (2) has cryogen liquid pipeline to be connected through second throttle (13) and the second absorber (4) with evaporator (6), Form the 4th class absorption heat pump.
31. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in claim 7-9, cancels second Absorber (4) and exterior cooling medium pipeline connect, and carry out the one-out-three in following Adjusted Option, three select two or three to select Three, obtain the 4th class absorption heat pump：Adjusted Option one, be by the second generator (2) have cryogen liquid pipeline through throttle valve (7) with Evaporator (6) connection, which is adjusted to the second generator (2), has cryogen liquid pipeline through throttle valve (7) and the second absorber (4) and evaporation Device (6) connects；Adjusted Option two, is that the second generator (2) is had cryogen liquid pipeline through second throttle (13) and evaporator (6) Connection, which is adjusted to the second generator (2), has cryogen liquid pipeline through second throttle (13) and the second absorber (4) and evaporator (6) Connection；Adjusted Option three, is to have cryogen liquid pipeline to be connected through the 3rd throttle valve (18) with evaporator (6) in the second generator (2) Being adjusted to the second generator (2) has cryogen liquid pipeline to connect through the 3rd throttle valve (18) and the second absorber (4) with evaporator (6) It is logical.
32. the 4th class absorption heat pump, is in any 4th class absorption heat pump described in claim 18, cancels second and inhale The cooling medium pipeline that device (4) is connected with outside is received, cancels the cooling medium pipeline that newly-increased absorber (B) is connected with outside, will Newly-increased generator (A) has cryogen liquid pipeline to connect to be adjusted to increase generator (A) newly with evaporator (6) through throttle valve (7) and have cryogen Liquid pipeline is connected through throttle valve (7), the second absorber (4) and newly-increased absorber (A) with evaporator (6), is formed the 4th class and is absorbed Formula heat pump.
33. the 4th class absorption heat pump, is in any 4th kind absorption type described in claim 1,3-5,7-9,11,13-16 In heat pump, cancel the cooling medium pipeline that the second absorber (4) is connected with outside, have technical measures 1. --- increase circulating pump, Circulating pump (E) has circulatory mediator pipeline to be sequentially communicated the second absorber (4) and the finisher (6) of evaporator (6) circulation again Medium pipeline connects shape and composition circulation loop with circulating pump (E), forms the 4th class absorption heat pump；Separately there are technical measures 2. --- increase intermediate heat exchanger, intermediate heat exchanger connect the second absorber 4 and evaporator 6, form the 4th kind absorption type Heat pump.
34. the 4th class absorption heat pump, is the increase in any 4th class absorption heat pump described in claim 18,20,22 Circulating pump, cancels the cooling medium pipeline that the second absorber (4) is connected with outside, cancels newly-increased absorber (B) and is connected with outside Cooling medium pipeline, circulating pump (E) have circulatory mediator pipeline be sequentially communicated newly-increased absorber (B), the second absorber (4) and steam The finisher (6) of hair device (6) connects shape with circulating pump (E) by circulatory mediator pipeline again and forms circulation loop, forms the 4th Class absorption heat pump.
35. the 5th class absorption heat pump, is in the 4th class absorption heat pump described in claim 1 or claim 11, increases Add newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, absorber (3) is had into weak solution pipeline Connected through solution heat exchanger (10) with the second absorber (4) and be adjusted to absorber (3) and have weak solution pipeline through new solubilization liquid heat Exchanger (D) is connected with newly-increased absorber (B), and newly-increased absorber (B) has weak solution pipeline through newly-increased solution pump (C) and solution again Heat exchanger (10) is connected with the second absorber (4), have concentrated solution pipeline through the second solution pump (9) in the second generator (2) and Solution heat exchanger (10) is connected with absorber (3) to be adjusted to the second generator (2) and has concentrated solution pipeline through solution heat exchanger (10) connected with newly-increased generator (A), newly-increased generator (A) has concentrated solution pipeline through the second solution pump (9) and new solubilization liquid again Heat exchanger (D) is connected with absorber (3), and newly-increased generator (A) also has refrigerant steam channel to be connected with newly-increased absorber (B), Newly-increased generator (A) medium pipeline that also has surplus heat connect with exterior, and newly-increased absorber (B) also cooling medium pipeline connects with outside It is logical, form the 5th class absorption heat pump.
36. the 5th class absorption heat pump, is in any 4th class absorption heat pump described in claim 35, cancels throttling Valve, has cryogen liquid pipeline to be connected with evaporator (6) through throttle valve (7) in the second generator (2) and is adjusted to the second generator (2) and has Cryogen liquid pipeline is connected with evaporator (6), forms the 5th class absorption heat pump.
37. the 5th class absorption heat pump, is in any 4th class absorption heat pump described in claim 3-5,13-16, increases Add newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, absorber (3) is had into weak solution pipeline Connected through solution heat exchanger (10) with the second absorber (4) and be adjusted to absorber (3) and have weak solution pipeline through new solubilization liquid heat Exchanger (D) is connected with newly-increased absorber (B), and newly-increased absorber (B) has weak solution pipeline through newly-increased solution pump (C) and solution again Heat exchanger (10) is connected with the second absorber (4), have concentrated solution pipeline through the second solution pump (9) in the second generator (2) and Solution heat exchanger (10) is connected with absorber (3) to be adjusted to the second generator (2) and has concentrated solution pipeline through solution heat exchanger (10) connected with newly-increased generator (A), newly-increased generator (A) has concentrated solution pipeline through the second solution pump (9) and new solubilization liquid again Heat exchanger (D) is connected with absorber (3), and newly-increased generator (A) also has refrigerant steam channel to be connected with newly-increased absorber (B), Newly-increased generator (A) medium pipeline that also has surplus heat connect with exterior, and newly-increased absorber (B) also cooling medium pipeline connects with outside It is logical, form the 4th class absorption heat pump.
38. the 5th class absorption heat pump, is in any 5th class absorption heat pump described in claim 37, cancels throttle valve And second throttle, there is cryogen liquid pipeline to be connected through throttle valve (7) with evaporator (6) in the second generator (2) and be adjusted to second Generator (2) has cryogen liquid pipeline to be connected with evaporator (6), and the second generator (2) is had cryogen liquid pipeline through second throttle (13) connected with evaporator (6) and be adjusted to the second generator (2) and there is cryogen liquid pipeline to be connected with evaporator (6), form the 5th class Absorption heat pump.
39. the 5th class absorption heat pump, is in any 4th class absorption heat pump described in claim 7-9, increase is newly-increased Generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, have weak solution pipeline through solution by absorber (3) Heat exchanger (10) is connected with the second absorber (4) to be adjusted to absorber (3) and has weak solution pipeline through newly-increased solution heat exchanger (D) connected with newly-increased absorber (B), newly-increased absorber (B) has weak solution pipeline through newly-increased solution pump (C) and solution heat exchange again Device (10) is connected with the second absorber (4), and the second generator (2) is had concentrated solution pipeline through the second solution pump (9) and solution heat Exchanger (10) connected with absorber (3) be adjusted to the second generator (2) have concentrated solution pipeline through solution heat exchanger (10) with Newly-increased generator (A) connection, newly-increased generator (A) have concentrated solution pipeline through the second solution pump (9) and new solubilization liquid heat exchange again Device (D) is connected with absorber (3), and newly-increased generator (A) also has refrigerant steam channel to be connected with newly-increased absorber (B), new additional issue Raw device (A) medium pipeline that also has surplus heat connect with exterior, and newly-increased absorber (B) also has cooling medium pipeline to be connected with exterior, shape Into the 5th class absorption heat pump.
40. the 5th class absorption heat pump, is in any 5th class absorption heat pump described in claim 39, cancels throttling Valve, second throttle and the 3rd throttle valve, have cryogen liquid pipeline to connect through throttle valve (7) and evaporator (6) in the second generator (2) It is logical to be adjusted to the second generator (2) and there is cryogen liquid pipeline to be connected with evaporator (6), the second generator (2) there is into cryogen liquid pipeline Connected through second throttle (13) with evaporator (6) be adjusted to the second generator (2) have cryogen liquid pipeline with evaporator (6) even It is logical, there is cryogen liquid pipeline to be connected through the 3rd throttle valve (18) with evaporator (6) in the second generator (2) and be adjusted to the second generator (2) there is cryogen liquid pipeline to be connected with evaporator (6), form the 5th class absorption heat pump.
41. the 5th class absorption heat pump, is in any 4th class absorption heat pump described in claim 1-17,28-34 Two generators (2) are added waste heat medium pipeline and are connected with outside, form the 5th class absorption heat pump.
42. the 5th class absorption heat pump, is the second hair in any 4th class absorption heat pump described in claim 18-23 Raw device (2) and newly-increased generator (A) are added waste heat medium pipeline and are connected with outside respectively, form the 5th class absorption heat pump.
43. the 5th class absorption heat pump, is the second hair in any 4th class absorption heat pump described in claim 18-23 Raw device (2) or newly-increased generator (A) are added waste heat medium pipeline and are connected with outside, form the 5th class absorption heat pump.
44. the 5th class absorption heat pump, is in any 5th class absorption heat pump described in claim 41, increases new additional issue Raw device, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, have refrigerant steam channel with absorbing by evaporator (6) Device (3) connection, which is adjusted to evaporator (6), has refrigerant steam channel to be connected with newly-increased absorber (B), and it is also dilute to increase absorber (B) newly Solution line is connected through newly-increased solution pump (C) and newly-increased solution heat exchanger (D) with newly-increased generator (A), increases generator (A) newly Also concentrated solution pipeline is connected through newly-increased solution heat exchanger (D) with newly-increased absorber (B), and newly-increased generator (A) also has cryogen Steam channel is connected with absorber (3), and newly-increased generator (A), which also has, drives heat medium pipeline to be connected with outside, increases absorber newly (B) there is heated medium pipeline to be connected with outside, form the 5th class absorption heat pump.
45. the 5th class absorption heat pump, be in any 5th class absorption heat pump described in claim 35-38,42-43, Newly-increased second generator of increase, newly-increased second absorber, newly-increased second solution pump and newly-increased second solution heat exchanger, will evaporate Device (6) has refrigerant steam channel to connect with absorber (3) to be adjusted to evaporator (6) and have refrigerant steam channel to absorb with newly-increased second Device connects, newly-increased second absorber also have weak solution pipeline through newly-increased second solution pump and newly-increased second solution heat exchanger with newly Increase the connection of the second generator, newly-increased second generator also has concentrated solution pipeline through newly-increased second solution heat exchanger and newly-increased second Absorber connects, and newly-increased second generator also has refrigerant steam channel to be connected with absorber (3), increases the second generator newly and also has drive Dynamic heat medium pipeline is connected with outside, and newly-increased second absorber also has heated medium pipeline to be connected with outside, forms the 5th class Absorption heat pump.
46. the 5th class absorption heat pump, is in any 4th class absorption heat pump described in claim 1-17, increase is newly-increased Generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, have refrigerant steam channel by the second generator (2) Connected with the second absorber (4) and be adjusted to the second generator (2) and there is refrigerant steam channel to be connected with newly-increased absorber (B), increased newly Absorber (B) also has weak solution pipeline to connect through newly-increased solution pump (C) and newly-increased solution heat exchanger (D) with newly-increased generator (A) Logical, newly-increased generator (A) also has concentrated solution pipeline to be connected through newly-increased solution heat exchanger (D) with newly-increased absorber (B), new additional issue Raw device (A) also has refrigerant steam channel connect with the second absorber (4), and newly-increased generator (A) also has surplus heat medium pipeline and outside Portion connects, and newly-increased absorber (B) also has cooling medium pipeline to be connected with outside, forms the 5th class absorption heat pump.
47. the 5th class absorption heat pump, is in any 5th class absorption heat pump described in claim 35-40, increase is new Increase the second generator, newly-increased second absorber, newly-increased second solution pump and newly-increased second solution heat exchanger, by newly-increased generator (A) there is refrigerant steam channel to connect with newly-increased absorber (B) to be adjusted to newly-increased generator (A) and have refrigerant steam channel and newly-increased the Two absorbers connect, and newly-increased second absorber also has weak solution pipeline through newly-increased second solution pump and newly-increased second solution heat exchange Device connect with newly-increased second generator, newly-increased second generator also have concentrated solution pipeline through newly-increased second solution heat exchanger with newly Increase the connection of the second absorber, newly-increased second generator also has refrigerant steam channel to be connected with newly-increased absorber (B), increases the second hair newly The raw device medium pipeline that also has surplus heat connect with exterior, and newly-increased second absorber, which also has, to be cooled down medium pipeline and connected with exterior, formation 5th class absorption heat pump.
48. the 5th class absorption heat pump, is the second hair in any 5th class absorption heat pump described in claim 45-47 Raw device (2) is added waste heat medium pipeline and is connected with outside, forms the 5th class absorption heat pump.
49. the 5th class absorption heat pump, is in any 4th class absorption heat pump described in claim 18-23, increase is new Increase the second generator, newly-increased second absorber, newly-increased second solution pump and newly-increased second solution heat exchanger, by newly-increased generator (A) there is refrigerant steam channel to connect with newly-increased absorber (B) to be adjusted to newly-increased generator (A) and have refrigerant steam channel and newly-increased the Two absorbers connect, and newly-increased second absorber also has weak solution pipeline through newly-increased second solution pump and newly-increased second solution heat exchange Device connect with newly-increased second generator, newly-increased second generator also have concentrated solution pipeline through newly-increased second solution heat exchanger with newly Increase the connection of the second absorber, newly-increased second generator also has refrigerant steam channel to be connected with newly-increased absorber (B), increases the second hair newly The raw device medium pipeline that also has surplus heat connect with exterior, and newly-increased second absorber, which also has, to be cooled down medium pipeline and connected with exterior, formation 5th class absorption heat pump.
50. the 5th class absorption heat pump, is second generator in any 5th class absorption heat pump described in claim 49 (2) waste heat medium pipeline is added respectively and is connected with outside with newly-increased generator (A), form the 5th class absorption heat pump.
51. the 5th class absorption heat pump, is second generator in any 5th class absorption heat pump described in claim 49 (2) or newly-increased generator (A) is added waste heat medium pipeline and is connected with outside, forms the 5th class absorption heat pump.
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CN106322815B (en) * 2015-09-28 2020-05-29 李华玉 Fifth-class absorption heat pump
CN106440473B (en) * 2015-09-28 2020-06-16 李华玉 Fifth-class absorption heat pump
CN106369865B (en) * 2016-05-30 2020-04-07 李华玉 Double-effect fourth-class and fifth-class absorption heat pump
CN115218536A (en) * 2020-02-21 2022-10-21 李华玉 Third/fourth type heat-driven absorption-compression heat pump
CN112984860A (en) * 2020-02-21 2021-06-18 李华玉 Absorption-compression heat pump of the third/fourth type
CN115355629A (en) * 2020-02-21 2022-11-18 李华玉 Third/fourth absorption heat pump

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4520634A (en) * 1983-04-13 1985-06-04 Hitachi, Ltd. Multi-stage absorption refrigeration system
CN101182962A (en) * 2007-11-25 2008-05-21 李华玉 Composite absorption heat pump
CN102200358A (en) * 2010-06-29 2011-09-28 上海理工大学 Two-stage double-effect lithium bromide (LiBr) refrigeration-heat pump cycle system
CN102305489A (en) * 2011-08-19 2012-01-04 李华玉 Compound first-class absorption heat pump based on single-effect flow
CN102538279A (en) * 2012-02-03 2012-07-04 李华玉 Triple-generation double absorption system and third-class absorption heat pump
CN102679612A (en) * 2012-05-14 2012-09-19 李华玉 Fractional condensation third-class absorption type heat pump

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101776343A (en) * 2009-11-09 2010-07-14 李华玉 Solution series circulated two-stage first-type absorption heat pump using single effect as first stage
CN101968286B (en) * 2010-10-10 2011-11-02 李华玉 Double absorption-double generation system and multi-terminal heat supply third kind absorption heat pumps
CN102419026B (en) * 2011-07-27 2013-11-20 李华玉 Absorption-type heat source temperature changer

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4520634A (en) * 1983-04-13 1985-06-04 Hitachi, Ltd. Multi-stage absorption refrigeration system
CN101182962A (en) * 2007-11-25 2008-05-21 李华玉 Composite absorption heat pump
CN102200358A (en) * 2010-06-29 2011-09-28 上海理工大学 Two-stage double-effect lithium bromide (LiBr) refrigeration-heat pump cycle system
CN102305489A (en) * 2011-08-19 2012-01-04 李华玉 Compound first-class absorption heat pump based on single-effect flow
CN102538279A (en) * 2012-02-03 2012-07-04 李华玉 Triple-generation double absorption system and third-class absorption heat pump
CN102679612A (en) * 2012-05-14 2012-09-19 李华玉 Fractional condensation third-class absorption type heat pump

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