CN104807235B - 5th class absorption heat pump - Google Patents

5th class absorption heat pump Download PDF

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Publication number
CN104807235B
CN104807235B CN201510140717.0A CN201510140717A CN104807235B CN 104807235 B CN104807235 B CN 104807235B CN 201510140717 A CN201510140717 A CN 201510140717A CN 104807235 B CN104807235 B CN 104807235B
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generator
solution
heat exchanger
pipeline
pump
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CN201510140717.0A
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CN104807235A (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
    • 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
    • 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
    • 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

Abstract

The present invention provides the 5th class absorption heat pump, belongs to absorption heat pump and technical field of waste heat utilization.Absorber connects generator through solution pump with solution heat exchanger,Generator connects the second generator through solution heat exchanger and the second solution heat exchanger,Second generator connects the 3rd generator,3rd generator is through the second solution pump and the second solution heat exchanger connection absorber,Generator has refrigerant steam channel to connect condenser,Condenser has cryogen liquid pipeline to connect evaporator with choke valve through the 3rd generator,Second generator and the 3rd generator have refrigerant steam channel to connect the second condenser,Second condenser connects evaporator through cryogen liquid pump,Evaporator has refrigerant steam channel to connect absorber,Generator has driving heat medium pipeline,Absorber and condenser have heated medium pipeline,Evaporator and the second generator are had a surplus heat medium pipeline,Second condenser have cooling medium pipeline respectively with ft connection,Form the 5th class absorption heat pump.

Description

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 three major types absorption heat pump, be respectively with high temperature driven thermal medium with Between heated medium the temperature difference be drive the temperature difference first-class absorption type heat pump, with waste heat medium and cold environment (cooling medium) it Between the temperature difference be drive the temperature difference second-kind absorption-type heat pump, and simultaneously with foregoing two kinds of temperature difference be drive the temperature difference the 3rd class inhale Receipts formula heat pump.According to existing understanding or viewpoint, in the absorption heat pump of these three types, high temperature driven heat is discharged into cold environment It is irrational in (cooling medium), not yet has technical staff to propose related absorption heat pump flow so far.
In the 3rd class absorption heat pump for providing warm load high, it is difficult that those skilled in the art encounter such technology Topic：In absorption heat pump flow with TFE-TDE solution as representative, refrigerant vapour latent heat is small, and high-temperature generator release cryogen steams The cryogen liquid temperature degree that vapour and within the condenser heat release are formed after heated medium is high, and sensible heat is relatively large；This causes to absorb The performance index of formula heat pump is very low, and the utilization to high-grade heat energy is unreasonable, influences the effective utilization to waste heat so that the 3rd class Application of the absorption heat pump in high-temperature heat supply field is very limited.
Inventor recognizes above mentioned problem, and have developed the technology new departure for solving the above problems, and develops comprising remaining To drive the temperature difference, it is driving to add with two kinds of different temperature drops of warm load high to the temperature difference between thermal medium and cold environment (cooling medium) 5th class absorption heat pump of the temperature difference；The present invention is provided and realizes that cryogen liquid temperature difference is utilized using the 3rd generator and the second condenser Based on serial 5th class absorption heat pump.
The content of the invention：
Present invention is primarily intended to provide the 5th class absorption heat pump, specific content of the invention subitem is described below：
1. the 5th class absorption heat pump, mainly by generator, the second generator, the 3rd generator, absorber, condenser, Second condenser, evaporator, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger and the second solution heat Exchanger is constituted；Absorber has weak solution pipeline to be connected with generator through solution pump and solution heat exchanger, and generator also has Concentrated solution pipeline is connected through solution heat exchanger and the second solution heat exchanger with the second generator, and the second generator also has dense molten Liquid pipeline is connected with the 3rd generator, and the 3rd generator also has concentrated solution pipeline through the second solution pump and the second solution heat exchanger Connected with absorber, generator also has refrigerant steam channel to be connected with condenser, condenser also has cryogen liquid pipeline and the 3rd hair The 3rd generator has cryogen liquid pipeline to be connected with evaporator through choke valve again after raw device connection, and the second generator and the 3rd occurs Device also has refrigerant steam channel to be connected with the second condenser respectively, and the second condenser also has cryogen liquid pipeline through cryogen liquid pump and steaming Hair device connection, evaporator also has refrigerant steam channel to be connected with absorber, and generator also has driving heat medium pipeline to connect with outside Logical, absorber and condenser also have heated medium pipeline and ft connection respectively, and evaporator and the second generator also have respectively Waste heat medium pipeline and ft connection, the second condenser also have cooling medium pipeline and ft connection, form the 5th kind absorption type Heat pump.
2. the 5th class absorption heat pump, is in the 5th class absorption heat pump described in the 1st, to cancel choke valve, by the Three generators have cryogen liquid pipeline to be connected with evaporator through choke valve to be adjusted to the 3rd generator and have cryogen liquid pipeline and evaporator Connection, forms the 5th class absorption heat pump.
3. the 5th class absorption heat pump, be in the 5th class absorption heat pump described in the 1st, increase the 4th generator, Second throttle, the 3rd solution pump, the 3rd solution heat exchanger and heat exchanger, it is molten through the 3rd that absorber sets up weak solution pipeline Liquid pump and the 3rd solution heat exchanger are connected with the 4th generator, and the 4th generator also has concentrated solution pipeline to be handed over through the 3rd solution heat Parallel operation and the second solution heat exchanger are connected with the second generator, have refrigerant steam channel that adjustment is connected with condenser in generator After thering is refrigerant steam channel to be connected with the 4th generator for generator the 4th generator have again cryogen liquid pipeline through heat exchanger, 3rd generator and second throttle are connected with evaporator, and the 4th generator also has refrigerant steam channel to be connected with condenser, heat Exchanger also has heated medium pipeline and ft connection, forms the 5th class absorption heat pump.
4. the 5th class absorption heat pump, be in the 5th class absorption heat pump described in the 1st, increase the 4th generator, Second throttle, the 3rd solution heat exchanger and heat exchanger, have weak solution pipeline to be handed over through solution pump and solution heat absorber Parallel operation connects with generator and is adjusted to absorber and has weak solution pipeline through solution pump, solution heat exchanger and the 3rd solution heat exchange Device is connected with generator, has concentrated solution pipeline to occur through solution heat exchanger and the second solution heat exchanger and second in generator Device connection is adjusted to generator has concentrated solution pipeline to be connected with the 4th generator through the 3rd solution heat exchanger, and the 4th generator is again There is concentrated solution pipeline to be connected with the second generator through solution heat exchanger and the second solution heat exchanger, there is cryogen to steam in generator Vapour passage is connected with condenser and is adjusted to after generator has refrigerant steam channel to be connected with the 4th generator the 4th generator again There is cryogen liquid pipeline to be connected with evaporator through heat exchanger, the 3rd generator and second throttle, the 4th generator also has cryogen Steam channel is connected with condenser, and heat exchanger also has heated medium pipeline and ft connection, forms the 5th kind absorption type heat Pump.
5. the 5th class absorption heat pump, be in the 5th class absorption heat pump described in the 1st, increase the 4th generator, Second throttle, the 3rd solution pump, the 3rd solution heat exchanger and heat exchanger, have weak solution pipeline through solution pump by absorber Connected with generator with solution heat exchanger and be adjusted to absorber and have weak solution pipeline through solution pump and solution heat exchanger and Four generators are connected, and the 4th generator has concentrated solution pipeline to connect with generator through the 3rd solution pump and the 3rd solution heat exchanger again It is logical, there is concentrated solution pipeline to be connected with the second generator through solution heat exchanger and the second solution heat exchanger in generator and be adjusted to Generator has concentrated solution pipeline to occur through the 3rd solution heat exchanger, solution heat exchanger and the second solution heat exchanger and second Device is connected, and is had refrigerant steam channel to be connected with condenser in generator and is adjusted to generator and has refrigerant steam channel and the 4th generation The 4th generator has cryogen liquid pipeline to connect through heat exchanger, the 3rd generator and second throttle and evaporator again after device connection Logical, the 4th generator also has refrigerant steam channel to be connected with condenser, and heat exchanger also has heated medium pipeline to connect with outside It is logical, form the 5th class absorption heat pump.
6. the 5th class absorption heat pump, is in any 5th class absorption heat pump described in 3-5, to cancel choke valve And second throttle, there is cryogen liquid pipeline to be connected with evaporator through choke valve in the 3rd generator and be adjusted to the 3rd generator and have cold Agent liquid pipeline is connected with evaporator, is had cryogen liquid pipeline to be connected with evaporator through second throttle in the 3rd generator and is adjusted to Three generators have cryogen liquid pipeline to be connected with evaporator, form the 5th class absorption heat pump.
7. the 5th class absorption heat pump, be in the 5th class absorption heat pump described in the 3rd, increase the 5th generator, 3rd choke valve, the 4th solution pump, the 4th solution heat exchanger and second heat exchanger, absorber set up weak solution pipeline through Four solution pumps and the 4th solution heat exchanger are connected with the 5th generator, and the 5th generator also has concentrated solution pipeline through the 4th solution Heat exchanger and the second solution heat exchanger are connected with the second generator, and the 4th generator is had into refrigerant steam channel and condenser Connection is adjusted to the 5th generator after the 4th generator has refrigerant steam channel to be connected with the 5th generator cryogen liquid pipe again Road connects through second heat exchanger, the 3rd generator and the 3rd choke valve with evaporator, and the 5th generator also has refrigerant vapour to lead to Road is connected with condenser, and the 4th generator is had into cryogen liquid pipeline through heat exchanger, the 3rd generator and second throttle and steaming Hair device connection is adjusted to the 4th generator has cryogen liquid pipeline through the 5th generator, heat exchanger, the 3rd generator and second section Stream valve is connected with evaporator, and second heat exchanger also has heated medium pipeline and ft connection, forms the 5th kind absorption type heat Pump.
8. the 5th class absorption heat pump, be in the 5th class absorption heat pump described in the 4th, increase the 5th generator, 3rd choke valve, the 4th solution heat exchanger and second heat exchanger, have weak solution pipeline through solution pump, solution heat by absorber Exchanger and the 3rd solution heat exchanger connected with generator be adjusted to absorber have weak solution pipeline through solution pump, solution heat hand over Parallel operation, the 4th solution heat exchanger and the 3rd solution heat exchanger are connected with generator, and the 4th generator is had into concentrated solution pipeline Connected with the second generator through solution heat exchanger and the second solution heat exchanger and be adjusted to the 4th generator and have concentrated solution pipeline Connected with the 5th generator through the 4th solution heat exchanger, the 5th generator has concentrated solution pipeline through solution heat exchanger and again Two solution heat exchangers are connected with the second generator, are had refrigerant steam channel to be connected with condenser in the 4th generator and are adjusted to The 5th generator has cryogen liquid pipeline to be handed over through the second heat again after four generators have refrigerant steam channel to be connected with the 5th generator Parallel operation, the 3rd generator and the 3rd choke valve are connected with evaporator, and the 5th generator also has refrigerant steam channel to connect with condenser It is logical, there is cryogen liquid pipeline that adjustment is connected with evaporator through heat exchanger, the 3rd generator and second throttle in the 4th generator For the 4th generator has cryogen liquid pipeline through the 5th generator, heat exchanger, the 3rd generator and second throttle and evaporator Connection, second heat exchanger also has heated medium pipeline and ft connection, forms the 5th class absorption heat pump.
9. the 5th class absorption heat pump, be in the 5th class absorption heat pump described in the 5th, increase the 5th generator, 3rd choke valve, the 4th solution pump, the 4th solution heat exchanger and second heat exchanger, have weak solution pipeline through molten by absorber Liquid pump and solution heat exchanger connected with the 4th generator be adjusted to absorber have weak solution pipeline through solution pump and solution heat hand over Parallel operation is connected with the 5th generator, the 5th generator have again concentrated solution pipeline through the 4th solution pump and the 4th solution heat exchanger with 4th generator is connected, and has concentrated solution pipeline molten through the 3rd solution heat exchanger, solution heat exchanger and second in generator Liquid heat exchanger connects with the second generator and is adjusted to generator and has concentrated solution pipeline through the 3rd solution heat exchanger, the 4th molten Liquid heat exchanger, solution heat exchanger and the second solution heat exchanger are connected with the second generator, and the 4th generator is had into cryogen Steam channel is connected with condenser and is adjusted to the 5th hair after the 4th generator has refrigerant steam channel to be connected with the 5th generator Raw device has cryogen liquid pipeline to be connected with evaporator through second heat exchanger, the 3rd generator and the 3rd choke valve again, and the 5th occurs Device also has refrigerant steam channel to be connected with condenser, and the 4th generator is had into cryogen liquid pipeline through heat exchanger, the 3rd generator Connected with evaporator with second throttle and be adjusted to the 4th generator and have cryogen liquid pipeline through the 5th generator, heat exchanger, Three generators and second throttle are connected with evaporator, and second heat exchanger also has heated medium pipeline and ft connection, shape Into the 5th class absorption heat pump.
10. the 5th class absorption heat pump, is in any 5th class absorption heat pump described in 7-9, to cancel throttling Valve, second throttle and the 3rd choke valve, have cryogen liquid pipeline to be connected with evaporator through choke valve in the 3rd generator and are adjusted to 3rd generator has cryogen liquid pipeline to be connected with evaporator, and the 3rd generator is had into cryogen liquid pipeline through second throttle and evaporation Device connection is adjusted to the 3rd generator has cryogen liquid pipeline to be connected with evaporator, and the 3rd generator is had into cryogen liquid pipeline through the 3rd Choke valve connects with evaporator and is adjusted to the 3rd generator and has cryogen liquid pipeline to be connected with evaporator, forms the 5th kind absorption type heat Pump.
11. the 5th class absorption heat pumps, mainly by generator, the second generator, the 3rd generator, absorber, condenser, Second condenser, evaporator, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat are handed over Parallel operation, the 4th generator, the 3rd solution heat exchanger and the second absorber are constituted；Absorber has weak solution pipeline molten through the 3rd Liquid heat exchanger is connected with the second absorber, and the second absorber also has weak solution pipeline through solution pump and solution heat exchanger and hair Raw device connection, generator also has concentrated solution pipeline to connect through solution heat exchanger and the second solution heat exchanger and the second generator Logical, the second generator also has concentrated solution pipeline to be connected with the 3rd generator, and the 3rd generator has concentrated solution pipeline through the second solution Heat exchanger is connected with the 4th generator, and the 4th generator also has concentrated solution pipeline through the second solution pump and the 3rd solution heat exchange Device is connected with absorber, and generator also has refrigerant steam channel to be connected with condenser, and condenser has cryogen liquid pipeline and the 3rd hair The 3rd generator has cryogen liquid pipeline to be connected with evaporator through the 4th generator and choke valve again after raw device connection, and second occurs Device and the 3rd generator also have refrigerant steam channel to be connected with the second condenser respectively, and the second condenser also has cryogen liquid pipeline to pass through Cryogen liquid pump is connected with evaporator, and the 4th generator also has refrigerant steam channel to be connected with the second absorber, and evaporator is also cold Agent steam channel is connected with absorber, and generator also has driving heat medium pipeline and ft connection, and absorber and condenser also divide There are not heated medium pipeline and ft connection, evaporator and the second generator heat medium pipeline of also having a surplus respectively connect with outside Logical, the second condenser and the second absorber also have cooling medium pipeline and ft connection respectively, form the 5th class absorption heat pump.
12. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in the 11st, to cancel choke valve, will 4th generator have cryogen liquid pipeline connected with evaporator through choke valve be adjusted to the 4th generator have cryogen liquid pipeline with evaporation Device is connected, and forms the 5th class absorption heat pump.
13. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in the 11st, to increase the 5th and occur Device, second throttle, the 3rd solution pump, the 4th solution heat exchanger and heat exchanger, the second absorber set up weak solution pipeline Connected with the 5th generator through the 3rd solution pump and the 4th solution heat exchanger, the 5th generator also has concentrated solution pipeline through the 4th Solution heat exchanger and the second solution heat exchanger are connected with the second generator, and generator is had into refrigerant steam channel and condenser Connection is adjusted to the 5th generator after generator has refrigerant steam channel to be connected with the 5th generator has cryogen liquid pipeline to pass through again Heat exchanger, the 3rd generator, the 4th generator and second throttle are connected with evaporator, and the 5th generator also has refrigerant vapour Passage is connected with condenser, and heat exchanger also has heated medium pipeline and ft connection, forms the 5th class absorption heat pump.
14. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in the 11st, to increase the 5th and occur Device, second throttle, the 4th solution heat exchanger and heat exchanger, have weak solution pipeline through solution pump and molten by the second absorber Liquid heat exchanger connects with generator and is adjusted to the second absorber and has weak solution pipeline through solution pump, solution heat exchanger and the 4th Solution heat exchanger is connected with generator, and generator is had into concentrated solution pipeline through solution heat exchanger and the second solution heat exchanger Connected with the second generator and be adjusted to generator and there is concentrated solution pipeline to be connected with the 5th generator through the 4th solution heat exchanger, Five generators have concentrated solution pipeline to be connected with the second generator through solution heat exchanger and the second solution heat exchanger again, will occur Device has refrigerant steam channel to be connected with condenser to be adjusted to after generator has refrigerant steam channel to be connected with the 5th generator Five generators have cryogen liquid pipeline to connect through heat exchanger, the 3rd generator, the 4th generator and second throttle and evaporator again Logical, the 5th generator also has refrigerant steam channel to be connected with condenser, and heat exchanger also has heated medium pipeline to connect with outside It is logical, form the 5th class absorption heat pump.
15. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in the 11st, to increase the 5th and occur Device, second throttle, the 3rd solution pump, the 4th solution heat exchanger and heat exchanger, have weak solution pipeline by the second absorber Connected with generator through solution pump and solution heat exchanger and be adjusted to the second absorber and have weak solution pipeline through solution pump and solution Heat exchanger is connected with the 5th generator, and the 5th generator has concentrated solution pipeline through the 3rd solution pump and the 4th solution heat exchange again Device is connected with generator, has concentrated solution pipeline to occur through solution heat exchanger and the second solution heat exchanger and second in generator Device connection is adjusted to generator has concentrated solution pipeline through the 4th solution heat exchanger, solution heat exchanger and the second solution heat exchange Device is connected with the second generator, is had refrigerant steam channel to be connected with condenser in generator and is adjusted to generator and has refrigerant vapour to lead to The 5th generator has cryogen liquid pipeline through heat exchanger, the 3rd generator, the 4th generation again after road is connected with the 5th generator Device and second throttle are connected with evaporator, and the 5th generator also has refrigerant steam channel to be connected with condenser, and heat exchanger is also There are heated medium pipeline and ft connection, form the 5th class absorption heat pump.
16. the 5th class absorption heat pumps, are in any 5th class absorption heat pump described in 13-15, to cancel section Stream valve and second throttle, have cryogen liquid pipeline to be connected with evaporator through choke valve in the 4th generator and are adjusted to the 4th generator There is cryogen liquid pipeline to be connected with evaporator, have cryogen liquid pipeline that adjustment is connected with evaporator through second throttle in the 4th generator For the 4th generator has cryogen liquid pipeline to be connected with evaporator, the 5th class absorption heat pump is formed.
17. the 5th class absorption heat pumps, be in the 5th class absorption heat pump described in the 1st, increase the 4th generator, 3rd solution pump, the 3rd solution heat exchanger and the second absorber, have weak solution pipeline through solution pump and solution heat by absorber Exchanger connects with generator and is adjusted to absorber and has weak solution pipeline to be inhaled through solution pump and the 3rd solution heat exchanger and second Device connection is received, the second absorber has weak solution pipeline to be connected with generator through the 3rd solution pump and solution heat exchanger, will send out again Raw device has concentrated solution pipeline to be connected with the second generator through solution heat exchanger and the second solution heat exchanger to be adjusted to generator There is concentrated solution pipeline to be connected with the 4th generator through solution heat exchanger, the 4th generator has concentrated solution pipeline through the 3rd solution again Heat exchanger and the second solution heat exchanger are connected with the second generator, and the 4th generator also has refrigerant steam channel to be inhaled with second Device connection is received, the 4th generator also has driving heat medium pipeline and ft connection, and the second absorber also has heated medium pipeline With ft connection, the 5th class absorption heat pump is formed.
18. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in the 17th, to cancel choke valve, will 3rd generator have cryogen liquid pipeline connected with evaporator through choke valve be adjusted to the 3rd generator have cryogen liquid pipeline with evaporation Device is connected, and forms the 5th class absorption heat pump.
19. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in the 17th, to increase the 5th and occur Device, second throttle, the 4th solution pump, the 4th solution heat exchanger and heat exchanger, the second absorber set up weak solution pipeline Connected with the 5th generator through the 4th solution pump and the 4th solution heat exchanger, the 5th generator also has concentrated solution pipeline through the 4th Solution heat exchanger is connected with the 4th generator, is had refrigerant steam channel to be connected with condenser in generator and is adjusted to generator and has The 5th generator has cryogen liquid pipeline through heat exchanger, the 3rd generator again after refrigerant steam channel is connected with the 5th generator Connected with second throttle with evaporator, the 5th generator also has refrigerant steam channel to be connected with condenser, and heat exchanger also has Heated medium pipeline and ft connection, form the 5th class absorption heat pump.
20. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in the 17th, to increase the 5th and occur Device, second throttle, the 4th solution heat exchanger and heat exchanger, have weak solution pipeline through the 3rd solution pump by the second absorber Connected with generator with solution heat exchanger and be adjusted to the second absorber and have weak solution pipeline through the 3rd solution pump, solution heat exchange Device and the 4th solution heat exchanger are connected with generator, and generator is had into concentrated solution pipeline through solution heat exchanger and the 4th generation Device connection is adjusted to generator has concentrated solution pipeline to be connected with the 5th generator through the 4th solution heat exchanger, and the 5th generator is again There is concentrated solution pipeline to be connected with the 4th generator through solution heat exchanger, there is refrigerant steam channel to be connected with condenser in generator The 5th generator has cryogen liquid pipeline to be handed over through heat again after being adjusted to generator and having refrigerant steam channel to be connected with the 5th generator Parallel operation, the 3rd generator and second throttle are connected with evaporator, and the 5th generator also has refrigerant steam channel to connect with condenser Logical, heat exchanger also has heated medium pipeline and ft connection, forms the 5th class absorption heat pump.
21. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in the 17th, to increase the 5th and occur Device, second throttle, the 4th solution pump, the 4th solution heat exchanger and heat exchanger, have weak solution pipeline by the second absorber Connected with generator through the 3rd solution pump and solution heat exchanger and be adjusted to the second absorber and have weak solution pipeline through the 3rd solution Pump and solution heat exchanger are connected with the 5th generator, and the 5th generator has concentrated solution pipeline molten through the 4th solution pump and the 4th again Liquid heat exchanger is connected with generator, has concentrated solution pipeline to connect adjustment with the 4th generator through solution heat exchanger in generator For generator has concentrated solution pipeline to be connected with the 4th generator through the 4th solution heat exchanger and solution heat exchanger, by generator There is refrigerant steam channel to be connected with condenser to be adjusted to the 5th after generator has refrigerant steam channel to be connected with the 5th generator Generator has cryogen liquid pipeline to be connected with evaporator through heat exchanger, the 3rd generator and second throttle again, the 5th generator Also refrigerant steam channel is connected with condenser, and heat exchanger also has heated medium pipeline and ft connection, forms the 5th class Absorption heat pump.
22. the 5th class absorption heat pumps, are the 5th hairs in any 5th class absorption heat pump described in 19-21 Raw device sets up driving heat medium pipeline and ft connection, forms the 5th class absorption heat pump.
23. the 5th class absorption heat pumps, are in any 5th class absorption heat pump described in 19-22, to cancel section Stream valve and second throttle, have cryogen liquid pipeline to be connected with evaporator through choke valve in the 3rd generator and are adjusted to the 3rd generator There is cryogen liquid pipeline to be connected with evaporator, have cryogen liquid pipeline that adjustment is connected with evaporator through second throttle in the 3rd generator For the 3rd generator has cryogen liquid pipeline to be connected with evaporator, the 5th class absorption heat pump is formed.
24. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in the 17th, to increase the 5th and occur Device, the 4th solution heat exchanger and the 3rd absorber, have weak solution pipeline through solution pump and the 3rd solution heat exchange by absorber Device connects with the second absorber and is adjusted to absorber and has weak solution pipeline to be connected with the 3rd absorber through the 4th solution heat exchanger, 3rd absorber has weak solution pipeline to be connected with the second absorber through solution pump and the 3rd solution heat exchanger again, and the 3rd is occurred Device has concentrated solution pipeline to be connected with absorber through the second solution pump and the second solution heat exchanger to be adjusted to the 3rd generator and have dense Solution line is connected through the second solution heat exchanger with the 5th generator, and the 5th generator has concentrated solution pipeline through the second solution again Pump and the 4th solution heat exchanger are connected with absorber, and the 5th generator also has refrigerant steam channel to be connected with the 3rd absorber, The 3rd generator has cryogen liquid pipeline through choke valve and steaming again after having cryogen liquid pipeline to be connected with the 3rd generator condenser Hair device connection is adjusted to the 3rd generator after condenser has cryogen liquid pipeline to be connected with the 3rd generator cryogen liquid pipeline again Connected with evaporator through the 5th generator and choke valve, the 3rd absorber also has cooling medium pipeline and ft connection, form the Five class absorption heat pumps.
25. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in the 24th, to cancel choke valve, will 5th generator have cryogen liquid pipeline connected with evaporator through choke valve be adjusted to the 5th generator have cryogen liquid pipeline with evaporation Device is connected, and forms the 5th class absorption heat pump.
26. the 5th class absorption heat pumps, mainly by generator, the second generator, the 3rd generator, absorber, condenser, Second condenser, evaporator, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat are handed over Parallel operation, the 4th generator, the 3rd solution heat exchanger and the second absorber are constituted；Absorber has weak solution pipeline molten through the 3rd Liquid heat exchanger is connected with the second absorber, and the second absorber also has weak solution pipeline through solution pump and solution heat exchanger and hair Raw device connection, generator also has concentrated solution pipeline to connect through solution heat exchanger and the second solution heat exchanger and the second generator Logical, the second generator also has concentrated solution pipeline to be connected with the 3rd generator, and the 3rd generator has concentrated solution pipeline through the second solution Heat exchanger is connected with the 4th generator, and the 4th generator also has concentrated solution pipeline through the second solution pump and the 3rd solution heat exchange Device is connected with absorber, and generator also has refrigerant steam channel to be connected with condenser, and condenser has cryogen liquid pipeline and the 3rd hair The 3rd generator has cryogen liquid pipeline to be connected with evaporator through choke valve again after raw device connection, and the second generator and the 3rd occurs Device also has refrigerant steam channel to be connected with the second condenser respectively, and the second condenser also has cryogen liquid pipeline through cryogen liquid pump and steaming Hair device connection, the 4th generator also has refrigerant steam channel to be connected with the second absorber, evaporator also have refrigerant steam channel and Absorber is connected, and generator also has driving heat medium pipeline and ft connection, and absorber and condenser also have heated Jie respectively Matter pipeline and ft connection, evaporator, the second generator and the 4th generator are also had a surplus heat medium pipeline and ft connection respectively, Second condenser and the second absorber also have cooling medium pipeline and ft connection respectively, form the 5th class absorption heat pump.
27. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in the 26th, to cancel choke valve, will 3rd generator have cryogen liquid pipeline connected with evaporator through choke valve be adjusted to the 3rd generator have cryogen liquid pipeline with evaporation Device is connected, and forms the 5th class absorption heat pump.
28. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in the 11st, to increase the 5th and occur Device, second throttle, the 3rd solution pump, the 4th solution heat exchanger and heat exchanger, the second absorber set up weak solution pipeline Connected with the 5th generator through the 3rd solution pump and the 4th solution heat exchanger, the 5th generator also has concentrated solution pipeline through the 4th Solution heat exchanger and the second solution heat exchanger are connected with the second generator, and generator is had into refrigerant steam channel and condenser Connection is adjusted to the 5th generator after generator has refrigerant steam channel to be connected with the 5th generator has cryogen liquid pipeline to pass through again Heat exchanger, the 3rd generator and second throttle are connected with evaporator, and the 5th generator also has refrigerant steam channel with condensation Device is connected, and heat exchanger also has heated medium pipeline and ft connection, forms the 5th class absorption heat pump.
29. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in the 11st, to increase the 5th and occur Device, second throttle, the 4th solution heat exchanger and heat exchanger, have weak solution pipeline through solution pump and molten by the second absorber Liquid heat exchanger connects with generator and is adjusted to the second absorber and has weak solution pipeline through solution pump, solution heat exchanger and the 4th Solution heat exchanger is connected with generator, and generator is had into concentrated solution pipeline through solution heat exchanger and the second solution heat exchanger Connected with the second generator and be adjusted to generator and there is concentrated solution pipeline to be connected with the 5th generator through the 4th solution heat exchanger, Five generators have concentrated solution pipeline to be connected with the second generator through solution heat exchanger and the second solution heat exchanger again, will occur Device has refrigerant steam channel to be connected with condenser to be adjusted to after generator has refrigerant steam channel to be connected with the 5th generator Five generators have cryogen liquid pipeline to be connected with evaporator through heat exchanger, the 3rd generator and second throttle again, and the 5th occurs Device also has refrigerant steam channel to be connected with condenser, and heat exchanger also has heated medium pipeline and ft connection, forms the 5th Class absorption heat pump.
30. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in the 11st, to increase the 5th and occur Device, second throttle, the 3rd solution pump, the 4th solution heat exchanger and heat exchanger, have weak solution pipeline by the second absorber Connected with generator through solution pump and solution heat exchanger and be adjusted to the second absorber and have weak solution pipeline through solution pump and solution Heat exchanger is connected with the 5th generator, and the 5th generator has concentrated solution pipeline through the 3rd solution pump and the 4th solution heat exchange again Device is connected with generator, has concentrated solution pipeline to occur through solution heat exchanger and the second solution heat exchanger and second in generator Device connection is adjusted to generator has concentrated solution pipeline through the 4th solution heat exchanger, solution heat exchanger and the second solution heat exchange Device is connected with the second generator, is had refrigerant steam channel to be connected with condenser in generator and is adjusted to generator and has refrigerant vapour to lead to The 5th generator has cryogen liquid pipeline through heat exchanger, the 3rd generator and the second throttling again after road is connected with the 5th generator Valve is connected with evaporator, and the 5th generator also has refrigerant steam channel to be connected with condenser, and heat exchanger also has heated medium Pipeline and ft connection, form the 5th class absorption heat pump.
31. the 5th class absorption heat pumps, are in any 5th class absorption heat pump described in 28-30, to cancel section Stream valve and second throttle, have cryogen liquid pipeline to be connected with evaporator through choke valve in the 3rd generator and are adjusted to the 3rd generator There is cryogen liquid pipeline to be connected with evaporator, have cryogen liquid pipeline that adjustment is connected with evaporator through second throttle in the 3rd generator For the 3rd generator has cryogen liquid pipeline to be connected with evaporator, the 5th class absorption heat pump is formed.
32. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in the 17th, to increase the 5th and occur Device, the 4th solution heat exchanger and the 3rd absorber, have weak solution pipeline through solution pump and the 3rd solution heat exchange by absorber Device connects with the second absorber and is adjusted to absorber and has weak solution pipeline to be connected with the 3rd absorber through the 4th solution heat exchanger, 3rd absorber has weak solution pipeline to be connected with the second absorber through solution pump and the 3rd solution heat exchanger again, and the 3rd is occurred Device has concentrated solution pipeline to be connected with absorber through the second solution pump and the second solution heat exchanger to be adjusted to the 3rd generator and have dense Solution line is connected through the second solution heat exchanger with the 5th generator, and the 5th generator has concentrated solution pipeline through the second solution again Pump and the 4th solution heat exchanger are connected with absorber, and the 5th generator also has refrigerant steam channel to be connected with the 3rd absorber, 5th generator also has surplus heat medium pipeline and ft connection, and the 3rd absorber also has cooling medium pipeline and ft connection, shape Into the 5th class absorption heat pump.
33. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in the 32nd, to cancel choke valve, will 3rd generator have cryogen liquid pipeline connected with evaporator through choke valve be adjusted to the 3rd generator have cryogen liquid pipeline with evaporation Device is connected, and forms the 5th class absorption heat pump.
34. the 5th class absorption heat pumps, are in any 5th class absorption heat pump described in 1-33, to increase newly-increased Generator, newly-increased absorber, new solubilization liquid pump and newly-increased solution heat exchanger, have refrigerant steam channel and absorber by evaporator Connection 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 Drive heat medium pipeline and ft connection, newly-increased absorber to also have heated medium pipeline and ft connection, form the 5th class and inhale Receipts formula heat pump.
35. the 5th class absorption heat pumps, are in any 5th described in 1-2,11-12,17-18,24-27,32-33 In class absorption heat pump, increase newly-increased generator, newly-increased absorber, new solubilization liquid pump and newly-increased solution heat exchanger, will occur Device has refrigerant steam channel to be connected with condenser to be adjusted to generator and have refrigerant steam channel to be connected with newly-increased absorber, increase newly and inhale Receiving device also has weak solution pipeline to be connected with newly-increased generator through new solubilization liquid pump and newly-increased solution heat exchanger, and newly-increased generator is also There is concentrated solution pipeline to be connected with newly-increased absorber through newly-increased solution heat exchanger, newly-increased generator also have refrigerant steam channel with it is cold Condenser is connected, and newly-increased generator also has driving heat medium pipeline and ft connection, and newly-increased absorber also has heated medium pipeline With ft connection, the 5th class absorption heat pump is formed.
36. the 5th class absorption heat pumps, are in any 5th kind absorption type heat described in 1-10,17-23,26-33 In pump, the 3rd generator sets up waste heat medium pipeline and ft connection, forms the 5th class absorption heat pump.
37. the 5th class absorption heat pumps, are the 3rd hairs in any 5th class absorption heat pump described in 11-16 Raw device and the 4th generator set up waste heat medium pipeline and ft connection respectively, form the 5th class absorption heat pump.
38. the 5th class absorption heat pumps, are the 3rd hairs in any 5th class absorption heat pump described in 11-16 Raw device or the 4th generator set up waste heat medium pipeline and ft connection, form the 5th class absorption heat pump.
39. the 5th class absorption heat pumps, are the 3rd hairs in any 5th class absorption heat pump described in 24-25 Raw device and the 5th generator set up waste heat medium pipeline and ft connection respectively, form the 5th class absorption heat pump.
40. the 5th class absorption heat pumps, are the 3rd hairs in any 5th class absorption heat pump described in 24-25 Raw device or the 5th generator set up waste heat medium pipeline and ft connection, form the 5th class absorption heat pump.
41. the 5th class absorption heat pumps, are in any 5th class absorption heat pump described in 36-40, to increase new Increase generator, newly-increased absorber, new solubilization liquid pump and newly-increased solution heat exchanger, evaporator is had refrigerant steam channel and absorbed Device connection 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 new Solubilized liquid 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 is also There are driving heat medium pipeline and ft connection, newly-increased absorber also has heated medium pipeline and ft connection, forms the 5th class Absorption heat pump.
42. the 5th class absorption heat pumps, are in any 5th class absorption heat pump described in 1-33, to increase newly-increased Generator, newly-increased absorber, new solubilization liquid pump and newly-increased solution heat exchanger, have refrigerant steam channel and the by the 3rd generator The connection of two condensers is adjusted to the 3rd 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 new solubilization liquid pump and newly-increased solution heat exchanger with newly-increased generator, and newly-increased generator also has concentrated solution pipeline Connected with newly-increased absorber through newly-increased solution heat exchanger, newly-increased generator also has refrigerant steam channel to connect with the second condenser Logical, newly-increased generator also has surplus heat medium pipeline and ft connection, and newly-increased absorber also has cooling medium pipeline and ft connection, Form the 5th class absorption heat pump.
43. the 5th class absorption heat pumps, are in any 5th class absorption heat pump described in 1-10,17-23, to increase Plus newly-increased generator, newly-increased absorber, new solubilization liquid pump and newly-increased solution heat exchanger, there is refrigerant vapour to lead in the second generator Road connects with the second condenser and is adjusted to the second generator and has refrigerant steam channel to be connected with newly-increased absorber, and newly-increased absorber is also There is weak solution pipeline to be connected with newly-increased generator through new solubilization liquid pump and newly-increased solution heat exchanger, newly-increased generator also has dense molten Liquid pipeline is connected through newly-increased solution heat exchanger with newly-increased absorber, and newly-increased generator also has refrigerant steam channel with the second condensation Device is connected, and newly-increased generator also has surplus heat medium pipeline and ft connection, newly-increased absorber also have cooling medium pipeline with it is outside Connection, forms the 5th class absorption heat pump.
44. the 5th class absorption heat pumps, are in any 5th class absorption heat pump described in the 43rd, the 3rd is occurred Device has refrigerant steam channel to be connected with the second condenser to be adjusted to the 3rd generator and have refrigerant steam channel to connect with newly-increased absorber It is logical, form the 5th class absorption heat pump.
45. the 5th class absorption heat pumps, are the 3rd hairs in any 5th class absorption heat pump described in 42-44 Raw device sets up waste heat medium pipeline and ft connection, forms the 5th class absorption heat pump.
46. the 5th class absorption heat pumps, are in any 5th class absorption heat pump described in 11-16, to increase new Increase generator, newly-increased absorber, new solubilization liquid pump and newly-increased solution heat exchanger, by the 4th generator have refrigerant steam channel with The connection of second absorber is adjusted to the 4th generator has refrigerant steam channel to be connected with newly-increased absorber, and newly-increased absorber is also dilute Solution line is connected through new solubilization liquid pump and newly-increased solution heat exchanger with newly-increased generator, and newly-increased generator also has concentrated solution pipe Road connects through newly-increased solution heat exchanger with newly-increased absorber, and newly-increased generator also has refrigerant steam channel to connect with the second absorber Logical, newly-increased generator also has surplus heat medium pipeline and ft connection, and newly-increased absorber also has cooling medium pipeline and ft connection, Form the 5th class absorption heat pump.
47. the 5th class absorption heat pumps, are the 3rd generators in any 5th class absorption heat pump described in the 46th Waste heat medium pipeline and ft connection are set up respectively with the 4th generator, form the 5th class absorption heat pump.
48. the 5th class absorption heat pumps, are the 3rd generators in any 5th class absorption heat pump described in the 46th Or the 4th generator set up waste heat medium pipeline and ft connection, form the 5th class absorption heat pump.
49. the 5th class absorption heat pumps, are in any 5th class absorption heat pump described in 24-25, to increase new Increase generator, newly-increased absorber, new solubilization liquid pump and newly-increased solution heat exchanger, by the 5th generator have refrigerant steam channel with The connection of 3rd absorber is adjusted to the 5th generator has refrigerant steam channel to be connected with newly-increased absorber, and newly-increased absorber is also dilute Solution line is connected through new solubilization liquid pump and newly-increased solution heat exchanger with newly-increased generator, and newly-increased generator also has concentrated solution pipe Road connects through newly-increased solution heat exchanger with newly-increased absorber, and newly-increased generator also has refrigerant steam channel to connect with the 3rd absorber Logical, newly-increased generator also has surplus heat medium pipeline and ft connection, and newly-increased absorber also has cooling medium pipeline and ft connection, Form the 5th class absorption heat pump.
50. the 5th class absorption heat pumps, are the 3rd generators in any 5th class absorption heat pump described in the 49th Waste heat medium pipeline and ft connection are set up respectively with the 5th generator, form the 5th class absorption heat pump.
51. the 5th class absorption heat pumps, are the 3rd generators in any 5th class absorption heat pump described in the 49th Or the 5th generator set up waste heat medium pipeline and ft connection, form the 5th class absorption heat pump.
52. the 5th class absorption heat pumps, are in any 5th class absorption heat pump described in 26-31, to increase new Increase generator, newly-increased absorber, new solubilization liquid pump and newly-increased solution heat exchanger, by the 4th generator have refrigerant steam channel with The connection of second absorber is adjusted to the 4th generator has refrigerant steam channel to be connected with newly-increased absorber, and newly-increased absorber is also dilute Solution line is connected through new solubilization liquid pump and newly-increased solution heat exchanger with newly-increased generator, and newly-increased generator also has concentrated solution pipe Road connects through newly-increased solution heat exchanger with newly-increased absorber, and newly-increased generator also has refrigerant steam channel to connect with the second absorber Logical, newly-increased generator also has surplus heat medium pipeline and ft connection, and newly-increased absorber also has cooling medium pipeline and ft connection, Form the 5th class absorption heat pump.
53. the 5th class absorption heat pumps, are in any 5th class absorption heat pump described in 32-33, to increase new Increase generator, newly-increased absorber, new solubilization liquid pump and newly-increased solution heat exchanger, by the 5th generator have refrigerant steam channel with The connection of 3rd absorber is adjusted to the 5th generator has refrigerant steam channel to be connected with newly-increased absorber, and newly-increased absorber is also dilute Solution line is connected through new solubilization liquid pump and newly-increased solution heat exchanger with newly-increased generator, and newly-increased generator also has concentrated solution pipe Road connects through newly-increased solution heat exchanger with newly-increased absorber, and newly-increased generator also has refrigerant steam channel to connect with the 3rd absorber Logical, newly-increased generator also has surplus heat medium pipeline and ft connection, and newly-increased absorber also has cooling medium pipeline and ft connection, Form the 5th class absorption heat pump.
54. the 5th class absorption heat pumps, are the 3rd hairs in any 5th class absorption heat pump described in 52-53 Raw device sets up waste heat medium pipeline and ft connection, forms the 5th class absorption heat pump.
55. the 5th class absorption heat pumps, are absorbed in any 5th class described in 1-2,17-18,26-27,32-33 In formula heat pump, by the second generator have a surplus heat medium pipeline and ft connection be adjusted to the 3rd generator have a surplus heat medium pipeline with Ft connection, the 3rd generator has cryogen liquid pipeline warp knuckle again after having cryogen liquid pipeline to be connected with the 3rd generator condenser Stream valve connects with evaporator and is adjusted to the second generator after condenser has cryogen liquid pipeline to be connected with the second generator and has cold again Agent liquid pipeline is connected through choke valve with evaporator, forms the 5th class absorption heat pump.
56. the 5th class absorption heat pumps, are in any 5th class absorption heat pump described in 1-41, to increase newly-increased Condenser, newly-increased choke valve and new solubilization liquid choke valve, have concentrated solution pipeline to connect tune with the 3rd generator in the second generator Whole is that the second generator has concentrated solution pipeline to be connected with the 3rd generator through new solubilization liquid choke valve, and the second generator is had into cryogen Steam channel connects with the second condenser and is adjusted to the second generator and has refrigerant steam channel to be connected with newly-increased condenser, increases newly cold Condenser also has cryogen liquid pipeline to be connected with the second condenser or evaporator through newly-increased choke valve, and newly-increased condenser also has cooling medium Pipeline and ft connection, form the 5th class absorption heat pump.
57. the 5th class absorption heat pumps, are in any 5th class absorption heat pump described in 1-41, to increase newly-increased Condenser, newly-increased cryogen liquid pump and new solubilization liquid choke valve, have concentrated solution pipeline to be connected with the 3rd generator in the second generator Being adjusted to the second generator has concentrated solution pipeline to be connected with the 3rd generator through new solubilization liquid choke valve, and the second generator is had into cold Agent steam channel connects with the second condenser and is adjusted to the second generator and has refrigerant steam channel to be connected with newly-increased condenser, increases newly Condenser also has cryogen liquid pipeline to be connected with evaporator through newly-increased cryogen liquid pump, newly-increased condenser also have cooling medium pipeline with it is outer Portion connects, and forms the 5th class absorption heat pump.
Essence of the invention is further illustrated with reference to the 5th class absorption heat pump shown in Fig. 1.
(1) in the 5th class absorption heat pump shown in Fig. 1, the cryogen liquid of condenser 5 flow through the 3rd generator 3 and heat release in Solution, will bring following effect：
1. the thermic load being brought into by high temperature cryogen liquid in evaporator 7 is reduced, the negative shadow to UTILIZATION OF VESIDUAL HEAT IN is reduced Ring.
2. the 3rd generator 3 realizes the raising of solution concentration using the thermic load of cryogen liquid, then relatively reduce generator 1 Required warm load high, can more significantly increase the performance index of source pump.
3. when environment (cooling medium) medium temperature is relatively low, can effectively using the temperature between cryogen liquid and cooling medium Difference, improves the utilization rate for driving thermic load and waste heat load.
(2) thermic load in high temperature driven thermal medium is discharged into refrigerant vapour by generator 1, and a part is by condensation Device 5 is transferred in heated medium, and another part in cooling medium, is belonged to by the 3rd generator 3 and the heat release of the second condenser 6 In with warm load substep temperature drop high be drive the temperature difference the temperature difference utilize new technology.
Brief description of the drawings：
Fig. 1 is according to the 5th class absorption heat pump provided by the present invention 1st kind of structure and schematic flow sheet.
Fig. 2 is according to the 5th class absorption heat pump provided by the present invention 2nd kind of structure and schematic flow sheet.
Fig. 3 is according to the 5th class absorption heat pump provided by the present invention 3rd kind of structure and schematic flow sheet.
Fig. 4 is according to the 5th class absorption heat pump provided by the present invention 4th kind of structure and schematic flow sheet.
Fig. 5 is according to the 5th class absorption heat pump provided by the present invention 5th kind of structure and schematic flow sheet.
Fig. 6 is according to the 5th class absorption heat pump provided by the present invention 6th kind of structure and schematic flow sheet.
Fig. 7 is according to the 5th class absorption heat pump provided by the present invention 7th kind of structure and schematic flow sheet.
Fig. 8 is according to the 5th class absorption heat pump provided by the present invention 8th kind of structure and schematic flow sheet.
Fig. 9 is according to the 5th class absorption heat pump provided by the present invention 9th kind of structure and schematic flow sheet.
Figure 10 is according to the 5th class absorption heat pump provided by the present invention 10th kind of structure and schematic flow sheet.
Figure 11 is according to the 5th class absorption heat pump provided by the present invention 11st kind of structure and schematic flow sheet.
Figure 12 is according to the 5th class absorption heat pump provided by the present invention 12nd kind of structure and schematic flow sheet.
Figure 13 is according to the 5th class absorption heat pump provided by the present invention 13rd kind of structure and schematic flow sheet.
Figure 14 is according to the 5th class absorption heat pump provided by the present invention 14th kind of structure and schematic flow sheet.
Figure 15 is according to the 5th class absorption heat pump provided by the present invention 15th kind of structure and schematic flow sheet.
Figure 16 is according to the 5th class absorption heat pump provided by the present invention 16th kind of structure and schematic flow sheet.
Figure 17 is according to the 5th class absorption heat pump provided by the present invention 17th kind of structure and schematic flow sheet.
Figure 18 is according to the 5th class absorption heat pump provided by the present invention 18th kind of structure and schematic flow sheet.
Figure 19 is according to the 5th class absorption heat pump provided by the present invention 19th kind of structure and schematic flow sheet.
Figure 20 is according to the 5th class absorption heat pump provided by the present invention 20th kind of structure and schematic flow sheet.
Figure 21 is according to the 5th class absorption heat pump provided by the present invention 21st kind of structure and schematic flow sheet.
Figure 22 is according to the 5th class absorption heat pump provided by the present invention 22nd kind of structure and schematic flow sheet.
Figure 23 is according to the 5th class absorption heat pump provided by the present invention 23rd kind of structure and schematic flow sheet.
Figure 24 is according to the 5th class absorption heat pump provided by the present invention 24th kind of structure and schematic flow sheet.
Figure 25 is according to the 5th class absorption heat pump provided by the present invention 25th kind of structure and schematic flow sheet.
In figure, 1- generators, the generators of 2- second, the generators of 3- the 3rd, 4- absorbers, 5- condensers, 6- second is condensed Device, 7- evaporators, 8- choke valves, 9- cryogen liquid pumps, 10- solution pumps, 11- the second solution pumps, 12- solution heat exchangers, 13- Two solution heat exchangers, the generators of 14- the 4th, 15- second throttle, the solution pumps of 16- the 3rd, the solution heat exchangers of 17- the 3rd, 18- heat exchangers, the generators of 19- the 5th, the choke valves of 20- the 3rd, the solution pumps of 21- the 4th, the solution heat exchangers of 22- the 4th, 23- Second heat exchanger, the absorbers of 24- second, the absorbers of 25- the 3rd；A- increases generator newly, and B- increases absorber, the new solubilization liquids of C- newly Pump, D- increases solution heat exchanger newly, and E- increases condenser newly, and F- increases choke valve, the new solubilization liquid choke valves of G- newly.
To note here is that：By taking the 5th class absorption heat pump shown in accompanying drawing 1 as an example, the throttling set in cryogen liquid pipeline Valve 8, can be substituted with gravitational pressure drop；When coolant temperature is relatively low, the cryogen liquid temperature degree for flowing through the 3rd generator 3 is cooled to evaporation During evaporating temperature inside device 7, choke valve 8 can be not provided with, and pressure difference is used for the inner heat exchanger pipeline of the 3rd generator 3 In.
Specific embodiment：
First it is noted that in the statement of structure and flow, it is inessential in the case of do not repeat；To apparent Flow do not state.Below in conjunction with the accompanying drawings the present invention is described in detail with example.
What the 5th class absorption heat pump shown in Fig. 1 was realized in：
(1) in structure, it is mainly by generator, the second generator, the 3rd generator, absorber, condenser, the second condensation Device, evaporator, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger institute Composition；Absorber 4 has weak solution pipeline to be connected with generator 1 through solution pump 10 and solution heat exchanger 12, and generator 1 is also dense Solution line is connected through the solution heat exchanger 13 of solution heat exchanger 12 and second with the second generator 2, and the second generator 2 also has Concentrated solution pipeline is connected with the 3rd generator 3, and the 3rd generator 3 also has concentrated solution pipeline through the second solution pump 11 and the second solution Heat exchanger 13 is connected with absorber 4, and generator 1 also has refrigerant steam channel to be connected with condenser 5, and condenser 5 also has cryogen The 3rd generator 3 has cryogen liquid pipeline to be connected with evaporator 7 through choke valve 8 again after liquid pipeline is connected with the 3rd generator 3, the Two generators 2 and the 3rd generator 3 also have refrigerant steam channel to be connected with the second condenser 6 respectively, and the second condenser 6 is also cold Agent liquid pipeline is connected through cryogen liquid pump 9 with evaporator 7, and evaporator 7 also has refrigerant steam channel to be connected with absorber 4, generator 1 Heat medium pipeline and ft connection are also driven, absorber 4 and condenser 5 also have heated medium pipeline to connect with outside respectively Logical, the generator 2 of evaporator 7 and second is also had a surplus heat medium pipeline and ft connection respectively, and the second condenser 6 also has cooling medium Pipeline and ft connection.
(2) in flow, the weak solution of absorber 4 enters generator 1 through solution pump 10 and solution heat exchanger 12, drives heat Medium flows through generator 1, heating and is provided into the solution release refrigerant vapour in it and to condenser 5, the concentrated solution of generator 1 Through 12 and second solution heat exchanger of solution heat exchanger 13 enter the second generator 2, waste heat medium flow through the second generator 2, Heat into the solution release refrigerant vapour in it and provided to the second condenser 6, the concentrated solution of the second generator 2 enters the 3rd Generator 3, heat absorption release refrigerant vapour are simultaneously provided to the second condenser 6, and the concentrated solution of the 3rd generator 3 is through the second solution pump 11 Enter absorber 4 with the second solution heat exchanger 13, absorb refrigerant vapour and heat release is in heated medium；The cryogen of condenser 5 In heated medium into cryogen liquid, the cryogen liquid of condenser 5 flows through after the heat release of the 3rd generator 3 cooling warp knuckle again for steam heat release The stream throttling of valve 8 enters evaporator 7, and the refrigerant vapour heat release of the second condenser 6 is in cooling medium into cryogen liquid, the second condenser 6 Cryogen liquid through cryogen liquid pump 9 pressurization enter evaporator 7；The cryogen liquid of evaporator 7 absorbs waste heat into refrigerant vapour, evaporator 7 The refrigerant vapour of generation is supplied to absorber 4, forms the 5th class absorption heat pump.
What the 5th class absorption heat pump shown in Fig. 2 was realized in：
(1) in structure, in the 5th class absorption heat pump shown in Fig. 1, the 4th generator, second throttle, the 3rd are increased Solution pump, the 3rd solution heat exchanger and heat exchanger, it is molten through the 3rd solution pump 16 and the 3rd that absorber 4 sets up weak solution pipeline Liquid heat exchanger 17 is connected with the 4th generator 14, and the 4th generator 14 also has concentrated solution pipeline through the 3rd solution heat exchanger 17 Connected with the second solution heat exchanger 13 with the second generator 2, there is refrigerant steam channel to connect tune with condenser 5 in generator 1 It is whole there is refrigerant steam channel to be connected with the 4th generator 14 for generator 1 after the 4th generator 14 have cryogen liquid pipeline again through heat Exchanger 18, the 3rd generator 3 and second throttle 15 are connected with evaporator 7, and the 4th generator 14 also has refrigerant steam channel Connected with condenser 5, heat exchanger 18 also has heated medium pipeline and ft connection.
(2) in flow, the refrigerant vapour that generator 1 is produced is supplied to the 4th generator 14 to make driving thermal medium, absorber 4 Part weak solution enter the 4th generator 14 through the 3rd solution pump 16 and the 3rd solution heat exchanger 17, refrigerant vapour flows through the Four generators 14, heating are provided into the solution release refrigerant vapour in it and to condenser 5, the concentrated solution of the 4th generator 14 Enter the second generator 2 through the 3rd solution heat exchanger 17 and the second solution heat exchanger 13；Flow through the cold of the 4th generator 14 The heat release of agent steam into passing through the generator 3 of heat exchanger 18 and the 3rd and progressively heat release cooling after cryogen liquid, after cooling Cryogen liquid enters evaporator 7 through the throttling of second throttle 15, forms the 5th class absorption heat pump.
What the 5th class absorption heat pump shown in Fig. 3 was realized in：
(1) in structure, in the 5th class absorption heat pump shown in Fig. 1, the 4th generator, second throttle, the 3rd are increased Solution heat exchanger and heat exchanger, have weak solution pipeline through solution pump 10 and solution heat exchanger 12 and generation by absorber 4 The connection of device 1 is adjusted to absorber 4 has weak solution pipeline through solution pump 10, the solution heat exchanger 17 of solution heat exchanger 12 and the 3rd Connected with generator 1, generator 1 is had into concentrated solution pipeline through the solution heat exchanger 13 and second of solution heat exchanger 12 and second The connection of generator 2 is adjusted to generator 1 has concentrated solution pipeline to be connected with the 4th generator 14 through the 3rd solution heat exchanger 17, the Four generators 14 have concentrated solution pipeline to connect with the second generator 2 through the solution heat exchanger 13 of solution heat exchanger 12 and second again It is logical, there is refrigerant steam channel to be connected with condenser 5 in generator 1 and be adjusted to generator 1 and have refrigerant steam channel and the 4th generation The 4th generator 14 has cryogen liquid pipeline through heat exchanger 18, the 3rd generator 3 and second throttle 15 again after device 14 is connected Connected with evaporator 7, the 4th generator 14 also has refrigerant steam channel to be connected with condenser 5, and heat exchanger 18 also has heated Medium pipeline and ft connection.
(2) in flow, the refrigerant vapour that generator 1 is produced is supplied to the 4th generator 14 to make driving thermal medium, absorber 4 Weak solution through solution pump 10, solution heat exchanger 12 and the 3rd solution heat exchanger 17 enter generator 1, generator 1 it is dense Solution enters the 4th generator 14 through the 3rd solution heat exchanger 17, and refrigerant vapour flows through the 4th generator 14, heating and enters it Interior solution release refrigerant vapour is simultaneously provided to condenser 5, and the concentrated solution of the 4th generator 14 is through solution heat exchanger 12 and the Two solution heat exchanger 13 enters the second generator 2；Flow through the refrigerant vapour heat release of the 4th generator 14 into after cryogen liquid again The generator 3 of heat exchanger 18 and the 3rd and progressively heat release cooling are flowed through, the cryogen liquid after cooling throttles through second throttle 15 Into evaporator 7, the 5th class absorption heat pump is formed.
What the 5th class absorption heat pump shown in Fig. 4 was realized in：
(1) in structure, in the 5th class absorption heat pump shown in Fig. 1, the 4th generator, second throttle, the 3rd are increased Solution pump, the 3rd solution heat exchanger and heat exchanger, have weak solution pipeline through solution pump 10 and solution heat exchange by absorber 4 Device 12 connects with generator 1 and is adjusted to absorber 4 and has weak solution pipeline through solution pump 10 and the hair of solution heat exchanger 12 and the 4th Raw device 14 is connected, and the 4th generator 14 has concentrated solution pipeline through the 3rd solution pump 16 and the 3rd solution heat exchanger 17 and generation again Device 1 is connected, and generator 1 is had into concentrated solution pipeline through the solution heat exchanger 13 of solution heat exchanger 12 and second and the second generator 2 connections are adjusted to generator 1 has concentrated solution pipeline through the 3rd solution heat exchanger 17, the solution of solution heat exchanger 12 and second heat Exchanger 13 is connected with the second generator 2, is had refrigerant steam channel to be connected with condenser 5 in generator 1 and is adjusted to generator 1 and has The 4th generator 14 has cryogen liquid pipeline through heat exchanger the 18, the 3rd again after refrigerant steam channel is connected with the 4th generator 14 Generator 3 and second throttle 15 are connected with evaporator 7, and the 4th generator 14 also has refrigerant steam channel to be connected with condenser 5, Heat exchanger 18 also has heated medium pipeline and ft connection.
(2) in flow, the refrigerant vapour that generator 1 is produced is supplied to the 4th generator 14 to make driving thermal medium, absorber 4 Weak solution enter the 4th generator 14 through solution pump 10 and solution heat exchanger 12, refrigerant vapour flow through the 4th generator 14, Heat into the solution release refrigerant vapour in it and provided to condenser 5, the concentrated solution of the 4th generator 14 is through the 3rd solution Pump 16 and the 3rd solution heat exchanger 17 enter generator 1, and the concentrated solution of generator 1 is through the 3rd solution heat exchanger 17, solution 12 and second solution heat exchanger of heat exchanger 13 enters the second generator 2；Flow through the refrigerant vapour heat release of the 4th generator 14 Pass through the generator 3 of heat exchanger 18 and the 3rd and progressively heat release cooling after into cryogen liquid, cryogen liquid after cooling is through the The throttling of two choke valve 15 enters evaporator 7, forms the 5th class absorption heat pump.
What the 5th class absorption heat pump shown in Fig. 5 was realized in：
(1) in structure, in the 5th class absorption heat pump shown in Fig. 2, the 5th generator, the 3rd choke valve, the 4th are increased Solution pump, the 4th solution heat exchanger and second heat exchanger, absorber 4 set up weak solution pipeline through the 4th solution pump 21 and Four solution heat exchangers 22 are connected with the 5th generator 19, and the 5th generator 19 also has concentrated solution pipeline through the 4th solution heat exchange The solution heat exchanger 13 of device 22 and second is connected with the second generator 2, and the 4th generator 14 is had into refrigerant steam channel with condensation The connection of device 5 is adjusted to the 5th generator 19 after the 4th generator 14 has refrigerant steam channel to be connected with the 5th generator 19 to be had again Cryogen liquid pipeline is connected through second heat exchanger 23, the 3rd generator 3 and the 3rd choke valve 20 with evaporator 7, the 5th generator 19 also have refrigerant steam channel to be connected with condenser 5, and the 4th generator 14 is had into cryogen liquid pipeline through heat exchanger 18, the 3rd hair Raw device 3 and second throttle 15 connected with evaporator 7 be adjusted to the 4th generator 14 have cryogen liquid pipeline through the 5th generator 19, Heat exchanger 18, the 3rd generator 3 and second throttle 15 are connected with evaporator 7, and second heat exchanger 23 also has heated Jie Matter pipeline and ft connection.
(2) in flow, the refrigerant vapour and cryogen liquid that the 4th generator 14 is produced are supplied to the 5th generator 19 to drive Thermal medium, the part weak solution of absorber 4 enters the 5th generator 19 through the 4th solution pump 21 and the 4th solution heat exchanger 22, Refrigerant vapour and cryogen liquid flow through the 5th generator 19, heating and are carried into the solution release refrigerant vapour in it and to condenser 5 For the concentrated solution of the 5th generator 19 enters the second generator through the 4th solution heat exchanger 22 and the second solution heat exchanger 13 2；Flow through the refrigerant vapour heat release of the 5th generator 19 into after cryogen liquid again through the generator 3 of second heat exchanger 23 and the 3rd simultaneously Progressively heat release cooling, the cryogen liquid after cooling enters evaporator 7 through the throttling of the 3rd choke valve 20；Flow through the 5th generator 19 Again through entering evaporator 7, shape after heat exchanger 18, the 3rd generator 3 and second throttle 15 after cryogen liquid heat release cooling Into the 5th class absorption heat pump.
What the 5th class absorption heat pump shown in Fig. 6 was realized in：
(1) in structure, in the 5th class absorption heat pump shown in Fig. 3, the 5th generator, the 3rd choke valve, the 4th are increased Solution heat exchanger and second heat exchanger, have weak solution pipeline through solution pump 10, solution heat exchanger 12 and by absorber 4 Three solution heat exchangers 17 connect with generator 1 and are adjusted to absorber 4 and have weak solution pipeline through solution pump 10, solution heat exchanger 12nd, the 4th solution heat exchanger 22 and the 3rd solution heat exchanger 17 are connected with generator 1, and the 4th generator 14 is had into concentrated solution Pipeline connects with the second generator 2 through the solution heat exchanger 13 of solution heat exchanger 12 and second and is adjusted to the 4th generator 14 and has Concentrated solution pipeline is connected through the 4th solution heat exchanger 22 with the 5th generator 19, and the 5th generator 19 has concentrated solution pipeline to pass through again The solution heat exchanger 13 of solution heat exchanger 12 and second is connected with the second generator 2, and the 4th generator 14 is had into refrigerant vapour Passage is connected with condenser 5 and is adjusted to the 5th hair after the 4th generator 14 has refrigerant steam channel to be connected with the 5th generator 19 Raw device 19 has cryogen liquid pipeline to be connected with evaporator 7 through second heat exchanger 23, the 3rd generator 3 and the 3rd choke valve 20 again, 5th generator 19 also has refrigerant steam channel to be connected with condenser 5, and the 4th generator 14 is had into cryogen liquid pipeline through heat exchange Device 18, the 3rd generator 3 and second throttle 15 connect with evaporator 7 and are adjusted to the 4th generator 14 and have cryogen liquid pipeline through Five generators 19, heat exchanger 18, the 3rd generator 3 and second throttle 15 are connected with evaporator 7, and second heat exchanger 23 is also There are heated medium pipeline and ft connection.
(2) in flow, the refrigerant vapour and cryogen liquid that the 4th generator 14 is produced are supplied to the 5th generator 19 to drive Thermal medium, the weak solution of absorber 4 is through solution pump 10, solution heat exchanger 12, the 4th solution heat exchanger 22 and the 3rd solution Heat exchanger 17 enters generator 1, and the concentrated solution of generator 1 enters the 4th generator 14 through the 3rd solution heat exchanger 17, the The concentrated solution of four generators 14 enters the 5th generator 19 through the 4th solution heat exchanger 22, and refrigerant vapour and cryogen liquid flow through the Five generators 19, heating are provided into the solution release refrigerant vapour in it and to condenser 5, the concentrated solution of the 5th generator 19 Enter the second generator 2 through 12 and second solution heat exchanger of solution heat exchanger 13；The cryogen for flowing through the 5th generator 19 steams Vapour heat release is lowered the temperature through the generator 3 of second heat exchanger 23 and the 3rd and progressively heat release again into after cryogen liquid, cold after cooling Agent liquid enters evaporator 7 through the throttling of the 3rd choke valve 20；Flow through the 5th generator 19 the heat release of cryogen liquid cooling after again through heat Enter evaporator 7 after exchanger 18, the 3rd generator 3 and second throttle 15, form the 5th class absorption heat pump.
What the 5th class absorption heat pump shown in Fig. 7 was realized in：
(1) in structure, in the 5th class absorption heat pump shown in Fig. 4, the 5th generator, the 3rd choke valve, the 4th are increased Solution pump, the 4th solution heat exchanger and second heat exchanger, have weak solution pipeline through solution pump 10 and solution heat by absorber 4 Exchanger 12 connects with the 4th generator 14 and is adjusted to absorber 4 and has weak solution pipeline through solution pump 10 and solution heat exchanger 12 Connected with the 5th generator 19, the 5th generator 19 has concentrated solution pipeline through the 4th solution pump 21 and the 4th solution heat exchanger again 22 are connected with the 4th generator 14, and generator 1 is had into concentrated solution pipeline through the 3rd solution heat exchanger 17, solution heat exchanger 12 and second solution heat exchanger 13 connected with the second generator 2 and be adjusted to generator 1 and have concentrated solution pipeline through the 3rd solution Heat exchanger 17, the 4th solution heat exchanger 22, the solution heat exchanger 13 of solution heat exchanger 12 and second and the second generator 2 Connection, has refrigerant steam channel to be connected with condenser 5 in the 4th generator 14 and is adjusted to the 4th generator 14 and has refrigerant vapour to lead to The 5th generator 19 has cryogen liquid pipeline through second heat exchanger 23, the 3rd generator again after road is connected with the 5th generator 19 3 and the 3rd choke valve 20 connected with evaporator 7, the 5th generator 19 also has refrigerant steam channel to be connected with condenser 5, by the 4th Generator 14 has cryogen liquid pipeline to be connected with evaporator 7 and be adjusted to through heat exchanger 18, the 3rd generator 3 and second throttle 15 4th generator 14 have cryogen liquid pipeline through the 5th generator 19, heat exchanger 18, the 3rd generator 3 and second throttle 15 with Evaporator 7 is connected, and second heat exchanger 23 also has heated medium pipeline and ft connection.
(2) in flow, the refrigerant vapour and cryogen liquid that the 4th generator 14 is produced are supplied to the 5th generator 19 to drive Thermal medium, the weak solution of absorber 4 enters the 5th generator 19 through solution pump 10 and solution heat exchanger 12, refrigerant vapour and cold Agent liquid flows through the 5th generator 19, heating and is provided into the solution release refrigerant vapour in it and to condenser 5, the 5th generator 19 concentrated solution enters the 4th generator 14 through the 4th solution pump 21 and the 4th solution heat exchanger 22, the 4th generator 14 it is dense Solution enters generator 1 through the 3rd solution pump 16 and the 3rd solution heat exchanger 17, and the concentrated solution of generator 1 is through the 3rd solution heat Exchanger 17, the 4th solution heat exchanger 22,12 and second solution heat exchanger of solution heat exchanger 13 enter the second generator 2；Flow through the refrigerant vapour heat release of the 5th generator 19 into after cryogen liquid again through the generator 3 of second heat exchanger 23 and the 3rd simultaneously Progressively heat release cooling, the cryogen liquid after cooling enters evaporator 7 through the throttling of the 3rd choke valve 20；Flow through the 5th generator 19 Again through entering evaporator 7, shape after heat exchanger 18, the 3rd generator 3 and second throttle 15 after cryogen liquid heat release cooling Into the 5th class absorption heat pump.
What the 5th class absorption heat pump shown in Fig. 8 was realized in：
(1) in structure, it is mainly by generator, the second generator, the 3rd generator, absorber, condenser, the second condensation Device, evaporator, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, Four generators, the 3rd solution heat exchanger and the second absorber are constituted；Absorber 4 has weak solution pipeline to be handed over through the 3rd solution heat Parallel operation 17 is connected with the second absorber 24, and the second absorber 24 also has weak solution pipeline through solution pump 10 and solution heat exchanger 12 Connected with generator 1, generator 1 also has concentrated solution pipeline through the solution heat exchanger 13 and second of solution heat exchanger 12 and second Generator 2 is connected, and the second generator 2 also has concentrated solution pipeline to be connected with the 3rd generator 3, and the 3rd generator 3 has concentrated solution pipe The second solution heat exchanger of road 13 is connected with the 4th generator 14, and the 4th generator 14 also has concentrated solution pipeline through the second solution The solution heat exchanger 17 of pump 11 and the 3rd is connected with absorber 4, and generator 1 also has refrigerant steam channel to be connected with condenser 5, cold The 3rd generator 3 has cryogen liquid pipeline through the 4th generator 14 again after condenser 5 has cryogen liquid pipeline to be connected with the 3rd generator 3 Connected with choke valve 8 with evaporator 7, the second generator 2 and the 3rd generator 3 also have refrigerant steam channel with the second condensation respectively Device 6 is connected, and the second condenser 6 also has cryogen liquid pipeline to be connected with evaporator 7 through cryogen liquid pump 9, and the 4th generator 14 is also cold Agent steam channel is connected with the second absorber 24, and evaporator 7 also has refrigerant steam channel to be connected with absorber 4, and generator 1 also has Drive heat medium pipeline and ft connection, absorber 4 and condenser 5 also has heated medium pipeline and ft connection respectively, steams The hair generator 2 of device 7 and second is also had a surplus heat medium pipeline and ft connection respectively, and the second condenser 6 and the second absorber 24 are also There are cooling medium pipeline and ft connection respectively, the 4th generator 14 also has surplus heat medium pipeline and ft connection.
(2) in flow, the weak solution of absorber 4 enters the second absorber 24, absorbs cold through the 3rd solution heat exchanger 17 , in cooling medium, the weak solution of the second absorber 24 enters through solution pump 10 and solution heat exchanger 12 and occurs for agent steam and heat release Device 1, drives thermal medium to flow through generator 1, heating and is provided into the solution release refrigerant vapour in it and to condenser 5, occurs The concentrated solution of device 1 enters the second generator 2 through 12 and second solution heat exchanger of solution heat exchanger 13, and waste heat medium flows through the Two generators 2, heating are provided into the solution release refrigerant vapour in it and to the second condenser 6, the second generator 2 it is dense molten Liquid enters the 3rd generator 3, heat absorption release and refrigerant vapour and is provided to the second condenser 6, and the concentrated solution of the 3rd generator 3 is through the Two solution heat exchanger 13 enters the 4th generator 14, and cryogen liquid and waste heat medium flow through the 4th generator 14, heating and enter it Interior solution discharges refrigerant vapour and is provided to the second absorber 24, and the concentrated solution of the 4th generator 14 is through the He of the second solution pump 11 3rd solution heat exchanger 17 enters absorber 4, absorbs refrigerant vapour and heat release is in heated medium；The cryogen of condenser 5 steams Vapour heat release flows through the 3rd generator 3 and the 4th generator 14 simultaneously successively in heated medium into cryogen liquid, the cryogen liquid of condenser 5 Progressively enter evaporator 7 through the throttling of choke valve 8 again after heat release cooling, the refrigerant vapour heat release of the second condenser 6 is situated between in cooling Matter enters evaporator 7 into cryogen liquid, the cryogen liquid of the second condenser 6 through the pressurization of cryogen liquid pump 9；The cryogen liquid of evaporator 7 absorbs Waste heat is supplied to absorber 4 into refrigerant vapour, the refrigerant vapour that evaporator 7 is produced, and forms the 5th class absorption heat pump.
What the 5th class absorption heat pump shown in Fig. 9 was realized in：
(1) in structure, in the 5th class absorption heat pump shown in Fig. 8, the 5th generator, second throttle, the 3rd are increased Solution pump, the 4th solution heat exchanger and heat exchanger, the second absorber 24 set up weak solution pipeline through the He of the 3rd solution pump 16 4th solution heat exchanger 22 is connected with the 5th generator 19, and the 5th generator 19 also has concentrated solution pipeline to be handed over through the 4th solution heat The solution heat exchanger 13 of parallel operation 22 and second is connected with the second generator 2, and generator 1 is had into refrigerant steam channel and condenser 5 Connection is adjusted to the 5th generator 19 after generator 1 has refrigerant steam channel to be connected with the 5th generator 19 cryogen liquid pipe again Road connects through heat exchanger 18, the 3rd generator 3, the 4th generator 14 and second throttle 15 with evaporator 7, the 5th generator 19 also have refrigerant steam channel to be connected with condenser 5, and heat exchanger 18 also has heated medium pipeline and ft connection.
(2) in flow, the refrigerant vapour that generator 1 is produced is supplied to the 5th generator 19 to make driving thermal medium, and second inhales The part weak solution for receiving device 24 enters the 5th generator 19, refrigerant vapour through the 3rd solution pump 16 and the 4th solution heat exchanger 22 The 5th generator 19, heating is flowed through to be provided into the solution release refrigerant vapour in it and to condenser 5, the 5th generator 19 Concentrated solution enters the second generator 2 through the 4th solution heat exchanger 22 and the second solution heat exchanger 13, flows through the 5th generator Into cryogen liquid, cryogen liquid flows through heat exchanger 18, the 3rd generator 3 and the 4th generator 14 and puts successively for 19 refrigerant vapour heat release Enter evaporator 7 through the throttling of second throttle 15 again after heat drop temperature, form the 5th class absorption heat pump.
What the 5th class absorption heat pump shown in Figure 10 was realized in：
(1) in structure, in the 5th class absorption heat pump shown in Fig. 8, the 5th generator, second throttle, the 4th are increased Solution heat exchanger and heat exchanger, by the second absorber 24 have weak solution pipeline through solution pump 10 and solution heat exchanger 12 with The connection of generator 1 is adjusted to the second absorber 24 has weak solution pipeline through solution pump 10, the solution of solution heat exchanger 12 and the 4th Heat exchanger 22 is connected with generator 1, and generator 1 is had into concentrated solution pipeline through the solution heat exchange of solution heat exchanger 12 and second Device 13 connects with the second generator 2 and is adjusted to generator 1 and has concentrated solution pipeline through the 4th solution heat exchanger 22 and the 5th generation Device 19 is connected, and the 5th generator 19 has concentrated solution pipeline through the solution heat exchanger 13 and second of solution heat exchanger 12 and second again Generator 2 is connected, by generator 1 have refrigerant steam channel connected with condenser 5 be adjusted to generator 1 have refrigerant steam channel with The 5th generator 19 has cryogen liquid pipeline through heat exchanger 18, the 3rd generator 3, the 4th hair again after 5th generator 19 is connected Raw device 14 and second throttle 15 are connected with evaporator 7, and the 5th generator 19 also has refrigerant steam channel to be connected with condenser 5, Heat exchanger 18 also has heated medium pipeline and ft connection.
(2) in flow, the refrigerant vapour that generator 1 is produced is supplied to the 5th generator 19 to make driving thermal medium, and second inhales The weak solution for receiving device 24 enters generator 1, generator through solution pump 10, solution heat exchanger 12 and the 4th solution heat exchanger 22 1 concentrated solution through the 4th solution heat exchanger 22 enter the 5th generator 19, refrigerant vapour flow through the 5th generator 19, heat into Enter release refrigerant vapour of the solution in it and provided to condenser 5, the concentrated solution of the 5th generator 19 is through solution heat exchanger 12 Enter the second generator 2 with the second solution heat exchanger 13, flow through the refrigerant vapour heat release of the 5th generator 19 into cryogen liquid it After pass through heat exchanger 18, the 3rd generator 3 and the 4th generator 14 and progressively heat release cooling, after cooling cryogen liquid warp The throttling of second throttle 15 enters evaporator 7, forms the 5th class absorption heat pump.
What the 5th class absorption heat pump shown in Figure 11 was realized in：
(1) in structure, in the 5th class absorption heat pump shown in Fig. 8, the 5th generator, second throttle, the 3rd are increased Solution pump, the 4th solution heat exchanger and heat exchanger, have weak solution pipeline through solution pump 10 and solution by the second absorber 24 Heat exchanger 12 connects with generator 1 and is adjusted to the second absorber 24 and has weak solution pipeline through solution pump 10 and solution heat exchanger 12 connect with the 5th generator 19, and the 5th generator 19 has concentrated solution pipeline through the 3rd solution pump 16 and the 4th solution heat exchange again Device 22 is connected with generator 1, by generator 1 have concentrated solution pipeline through the solution heat exchanger 13 of solution heat exchanger 12 and second with The connection of second generator 2 is adjusted to generator 1 has concentrated solution pipeline through the 4th solution heat exchanger 22, the and of solution heat exchanger 12 Second solution heat exchanger 13 is connected with the second generator 2, has refrigerant steam channel to connect adjustment with condenser 5 in generator 1 The 5th generator 19 has cryogen liquid pipeline to be handed over through heat again after having refrigerant steam channel to be connected with the 5th generator 19 for generator 1 Parallel operation 18, the 3rd generator 3, the 4th generator 14 and second throttle 15 are connected with evaporator 7, and the 5th generator 19 is also cold Agent steam channel is connected with condenser 5, and heat exchanger 18 also has heated medium pipeline and ft connection.
(2) in flow, the refrigerant vapour that generator 1 is produced is supplied to the 5th generator 19 to make driving thermal medium, and second inhales The weak solution for receiving device 24 enters the 5th generator 19 through solution pump 10 and solution heat exchanger 12, and refrigerant vapour flows through the 5th generation Device 19, heating are provided into the solution release refrigerant vapour in it and to condenser 5, and the concentrated solution of the 5th generator 19 is through the 3rd Solution pump 16 and the 4th solution heat exchanger 22 enter generator 1, the concentrated solution of generator 1 through the 4th solution heat exchanger 22, 12 and second solution heat exchanger of solution heat exchanger 13 enters the second generator 2；Flow through the refrigerant vapour of the 5th generator 19 Heat release is into passing through heat exchanger 18, the 3rd generator 3 and the 4th generator 14 and progressively heat release cooling, cooling after cryogen liquid Cryogen liquid afterwards enters evaporator 7 through the throttling of second throttle 15, forms the 5th class absorption heat pump.
What the 5th class absorption heat pump shown in Figure 12 was realized in：
(1) in structure, in the 5th class absorption heat pump shown in Fig. 1, the 4th generator, the 3rd solution pump, the 3rd are increased Solution heat exchanger and the second absorber, have weak solution pipeline through solution pump 10 and solution heat exchanger 12 and hair by absorber 4 The raw connection of device 1 is adjusted to absorber 4 has weak solution pipeline through the solution heat exchanger 17 of solution pump 10 and the 3rd and the second absorber 24 connections, the second absorber 24 has weak solution pipeline to be connected with generator 1 through the 3rd solution pump 16 and solution heat exchanger 12 again, There is concentrated solution pipeline to connect tune with the second generator 2 through the solution heat exchanger 13 of solution heat exchanger 12 and second in generator 1 It is whole for generator 1 has concentrated solution pipeline to be connected with the 4th generator 14 through solution heat exchanger 12, the 4th generator 14 has dense again Solution line is connected through the 3rd solution heat exchanger 17 and the second solution heat exchanger 13 with the second generator 2, the 4th generator 14 also have refrigerant steam channel to be connected with the second absorber 24, and the 4th generator 14 also has driving heat medium pipeline to connect with outside Logical, the second absorber 24 also has heated medium pipeline and ft connection.
(2) in flow, the weak solution of absorber 4 enters the second absorber through solution pump 10 and the 3rd solution heat exchanger 17 24th, absorb refrigerant vapour and heat release is in heated medium, the weak solution of the second absorber 24 is through the 3rd solution pump 16 and solution heat Exchanger 12 enters generator 1, and the concentrated solution of generator 1 enters the 4th generator 14 through solution heat exchanger 12, drives heat to be situated between Mass flow is through the 4th generator 14, heating is into the solution release refrigerant vapour in it and is supplied to the second absorber 24, the 4th hair The concentrated solution of raw device 14 enters the second generator 2 through the 3rd solution heat exchanger 17 and the second solution heat exchanger 13, forms the Five class absorption heat pumps.
What the 5th class absorption heat pump shown in Figure 13 was realized in：
(1) in structure, in the 5th class absorption heat pump shown in Figure 12, the 5th generator, second throttle, the 4th are increased Solution pump, the 4th solution heat exchanger and heat exchanger, the second absorber 24 set up weak solution pipeline through the He of the 4th solution pump 21 4th solution heat exchanger 22 is connected with the 5th generator 19, and the 5th generator 19 also has concentrated solution pipeline to be handed over through the 4th solution heat Parallel operation 22 is connected with the 4th generator 14, is had refrigerant steam channel to be connected with condenser 5 in generator 1 and is adjusted to generator 1 and has The 5th generator 19 has cryogen liquid pipeline through heat exchanger the 18, the 3rd again after refrigerant steam channel is connected with the 5th generator 19 Generator 3 and second throttle 15 are connected with evaporator 7, and the 5th generator 19 also has refrigerant steam channel to be connected with condenser 5, Heat exchanger 18 also has heated medium pipeline and ft connection.
(2) in flow, the refrigerant vapour that generator 1 is produced is supplied to the 5th generator 19 to make driving thermal medium, and second inhales The part weak solution for receiving device 24 enters the 5th generator 19, refrigerant vapour through the 4th solution pump 21 and the 4th solution heat exchanger 22 The 5th generator 19, heating is flowed through to be provided into the solution release refrigerant vapour in it and to condenser 5, the 5th generator 19 Concentrated solution enters the 4th generator 14 through the 4th solution heat exchanger 22；Flow through the refrigerant vapour heat release Cheng Leng of the 5th generator 19 Agent liquid, cryogen liquid flow through successively heat exchanger 18 and the heat release of the 3rd generator 3 cooling after again through second throttle 15 throttle into Enter evaporator 7, form the 5th class absorption heat pump.
What the 5th class absorption heat pump shown in Figure 14 was realized in：
(1) in structure, in the 5th class absorption heat pump shown in Figure 12, the 5th generator, second throttle, the 4th are increased Solution heat exchanger and heat exchanger, have weak solution pipeline through the 3rd solution pump 16 and solution heat exchanger by the second absorber 24 12 connected with generator 1 be adjusted to the second absorber 24 have weak solution pipeline through the 3rd solution pump 16, solution heat exchanger 12 and 4th solution heat exchanger 22 is connected with generator 1, and generator 1 is had into concentrated solution pipeline through the hair of solution heat exchanger 12 and the 4th The raw connection of device 14 is adjusted to generator 1 has concentrated solution pipeline to be connected with the 5th generator 19 through the 4th solution heat exchanger 22, the Five generators 19 have concentrated solution pipeline to be connected with the 4th generator 14 through solution heat exchanger 12 again, have cryogen to steam in generator 1 Vapour passage is connected with condenser 5 and is adjusted to the 5th generation after generator 1 has refrigerant steam channel to be connected with the 5th generator 19 Device 19 has cryogen liquid pipeline to be connected with evaporator 7 through heat exchanger 18, the 3rd generator 3 and second throttle 15 again, the 5th hair Raw device 19 also has refrigerant steam channel to be connected with condenser 5, and the 5th generator 19 also has driving heat medium pipeline and ft connection, Heat exchanger 18 also has heated medium pipeline and ft connection.
(2) in flow, the refrigerant vapour that thermal medium and generator 1 are produced is driven to provide hot negative to the 5th generator 19 Lotus, the weak solution of the second absorber 24 enters through the 3rd solution pump 16, the solution heat exchanger 22 of solution heat exchanger 12 and the 4th Generator 1, the concentrated solution of generator 1 enters the 5th generator 19 through the 4th solution heat exchanger 22, drives thermal medium and cryogen Steam flows through the 5th generator 19, heating and is provided into the solution release refrigerant vapour in it and to condenser 5, the 5th generator 19 concentrated solution enters the 4th generator 14 through solution heat exchanger 12；Flow through the refrigerant vapour heat release Cheng Leng of the 5th generator 19 The generator 3 of heat exchanger 18 and the 3rd and progressively heat release cooling are passed through after agent liquid, the cryogen liquid after cooling is through second section The stream throttling of valve 15 enters evaporator 7, forms the 5th class absorption heat pump.
What the 5th class absorption heat pump shown in Figure 15 was realized in：
(1) in structure, in the 5th class absorption heat pump shown in Figure 12, the 5th generator, second throttle, the 4th are increased Solution pump, the 4th solution heat exchanger and heat exchanger, have weak solution pipeline through the He of the 3rd solution pump 16 by the second absorber 24 Solution heat exchanger 12 connects with generator 1 and is adjusted to the second absorber 24 and has weak solution pipeline through the 3rd solution pump 16 and solution Heat exchanger 12 is connected with the 5th generator 19, and the 5th generator 19 has concentrated solution pipeline molten through the 4th solution pump 21 and the 4th again Liquid heat exchanger 22 is connected with generator 1, and generator 1 is had into concentrated solution pipeline through the generator 14 of solution heat exchanger 12 and the 4th Connection is adjusted to generator 1 has concentrated solution pipeline through the 4th solution heat exchanger 22 and the generator of solution heat exchanger 12 and the 4th 14 connections, have refrigerant steam channel to be connected with condenser 5 in generator 1 and are adjusted to generator 1 and have refrigerant steam channel and the 5th The 5th generator 19 has cryogen liquid pipeline through heat exchanger 18, the 3rd generator 3 and the second throttling again after generator 19 is connected Valve 15 is connected with evaporator 7, and the 5th generator 19 also has refrigerant steam channel to be connected with condenser 5, and heat exchanger 18 also has quilt Heating medium pipeline and ft connection.
(2) in flow, the refrigerant vapour that generator 1 is produced is supplied to the 5th generator 19 to make driving thermal medium, and second inhales The weak solution for receiving device 24 enters the 5th generator 19 through the 3rd solution pump 16 and solution heat exchanger 12, and refrigerant vapour flows through the 5th Generator 19, heating are provided into the solution release refrigerant vapour in it and to condenser 5, the concentrated solution warp of the 5th generator 19 4th solution pump 21 and the 4th solution heat exchanger 22 enter generator 1, and the concentrated solution of generator 1 is through the 4th solution heat exchanger 22 and solution heat exchanger 12 enter the 4th generator 14；The refrigerant vapour heat release of the 5th generator 19 is flowed through into after cryogen liquid The generator 3 of heat exchanger 18 and the 3rd and progressively heat release cooling are passed through, the cryogen liquid after cooling is saved through second throttle 15 Stream enters evaporator 7, forms the 5th class absorption heat pump.
What the 5th class absorption heat pump shown in Figure 16 was realized in：
(1) in structure, in the 5th class absorption heat pump shown in Figure 12, the 5th generator, the 4th solution heat exchange are increased Device and the 3rd absorber, have weak solution pipeline to be absorbed through the solution heat exchanger 17 and second of solution pump 10 and the 3rd absorber 4 The connection of device 24 is adjusted to absorber 4 has weak solution pipeline to be connected with the 3rd absorber 25 through the 4th solution heat exchanger 22, and the 3rd Absorber 25 has weak solution pipeline to be connected with the second absorber 24 through the solution heat exchanger 17 of solution pump 10 and the 3rd again, by the 3rd Generator 3 has concentrated solution pipeline to be connected with absorber 4 and be adjusted to the 3rd through the second solution pump 11 and the second solution heat exchanger 13 Generator 3 has concentrated solution pipeline to be connected with the 5th generator 19 through the second solution heat exchanger 13, and the 5th generator 19 has dense again Solution line is connected through the second solution pump 11 and the 4th solution heat exchanger 22 with absorber 4, and the 5th generator 19 also has cryogen Steam channel is connected with the 3rd absorber 25, the 3rd generation after having cryogen liquid pipeline to be connected with the 3rd generator 3 condenser 5 Device 3 has cryogen liquid pipeline to be connected with evaporator 7 through choke valve 8 to be adjusted to condenser 5 and have cryogen liquid pipeline and the 3rd generator 3 again The 3rd generator 3 has cryogen liquid pipeline to be connected with evaporator 7 through the 5th generator 19 and choke valve 8 again after connection, the 5th hair Raw device 19 also has surplus heat medium pipeline and ft connection, and the 3rd absorber 25 also has cooling medium pipeline and ft connection.
(2) in flow, the weak solution of absorber 4 enters the 3rd absorber 25, absorbs cold through the 4th solution heat exchanger 22 , in cooling medium, the weak solution of the 3rd absorber 25 enters through the solution heat exchanger 17 of solution pump 10 and the 3rd for agent steam and heat release Second absorber 24；The concentrated solution of the 3rd generator 3 through the second solution heat exchanger 13 enter the 5th generator 19, cryogen liquid and Waste heat medium flows through the 5th generator 19, heating and is provided into the solution release refrigerant vapour in it and to the 3rd absorber 25, The concentrated solution of the 5th generator 19 enters absorber 4 through the second solution pump 11 and the 4th solution heat exchanger 22；Condenser 5 it is cold Agent liquid flows through the 3rd generator 3 and the 5th generator 19 and progressively heat release cooling successively, and the cryogen liquid after cooling is through choke valve 8 Throttling enters evaporator 7, forms the 5th class absorption heat pump.
What the 5th class absorption heat pump shown in Figure 17 was realized in：
(1) in structure, it is mainly by generator, the second generator, the 3rd generator, absorber, condenser, the second condensation Device, evaporator, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, Four generators, the 3rd solution heat exchanger and the second absorber are constituted；Absorber 4 has weak solution pipeline to be handed over through the 3rd solution heat Parallel operation 17 is connected with the second absorber 24, and the second absorber 24 also has weak solution pipeline through solution pump 10 and solution heat exchanger 12 Connected with generator 1, generator 1 also has concentrated solution pipeline through the solution heat exchanger 13 and second of solution heat exchanger 12 and second Generator 2 is connected, and the second generator 2 also has concentrated solution pipeline to be connected with the 3rd generator 3, and the 3rd generator 3 has concentrated solution pipe The second solution heat exchanger of road 13 is connected with the 4th generator 14, and the 4th generator 14 also has concentrated solution pipeline through the second solution The solution heat exchanger 17 of pump 11 and the 3rd is connected with absorber 4, and generator 1 also has refrigerant steam channel to be connected with condenser 5, cold The 3rd generator 3 has cryogen liquid pipeline through choke valve 8 and steaming again after condenser 5 has cryogen liquid pipeline to be connected with the 3rd generator 3 Hair device 7 is connected, and the second generator 2 and the 3rd generator 3 also have refrigerant steam channel to be connected with the second condenser 6 respectively, and second Condenser 6 also has cryogen liquid pipeline to be connected with evaporator 7 through cryogen liquid pump 9, the 4th generator 14 also have refrigerant steam channel and Second absorber 24 is connected, and evaporator 7 also has refrigerant steam channel to be connected with absorber 4, and generator 1 also has driving thermal medium pipe Road and ft connection, absorber 4 and condenser 5 also have heated medium pipeline and ft connection respectively, and evaporator 7, second is sent out The raw generator 14 of device 2 and the 4th is also had a surplus heat medium pipeline and ft connection respectively, and the second condenser 6 and the second absorber 24 are also There are cooling medium pipeline and ft connection respectively.
(2) in flow, the weak solution of absorber 4 enters the second absorber 24, absorbs cold through the 3rd solution heat exchanger 17 , in cooling medium, the weak solution of the second absorber 24 enters through solution pump 10 and solution heat exchanger 12 and occurs for agent steam and heat release Device 1, drives thermal medium to flow through generator 1, heating and is provided into the solution release refrigerant vapour in it and to condenser 5, occurs The concentrated solution of device 1 enters the second generator 2 through 12 and second solution heat exchanger of solution heat exchanger 13, and waste heat medium flows through the Two generators 2, heating are provided into the solution release refrigerant vapour in it and to the second condenser 6, the second generator 2 it is dense molten Liquid enters the 3rd generator 3, heat absorption release and refrigerant vapour and is provided to the second condenser 6, and the concentrated solution of the 3rd generator 3 is through the Two solution heat exchanger 13 enters the 4th generator 14, the solution that waste heat medium flows through the 4th generator 14, heating enters in it Release refrigerant vapour is simultaneously provided to the second absorber 24, and the concentrated solution of the 4th generator 14 is through the second solution pump 11 and the 3rd solution Heat exchanger 17 enters absorber 4, absorbs refrigerant vapour and heat release is in heated medium；The refrigerant vapour heat release of condenser 5 in Heated medium throttles through choke valve 8 again into cryogen liquid, the cryogen liquid of condenser 5 after flowing through the heat release of the 3rd generator 3 cooling Into evaporator 7, in cooling medium into cryogen liquid, the cryogen liquid of the second condenser 6 is passed through for the refrigerant vapour heat release of the second condenser 6 The pressurization of cryogen liquid pump 9 enters evaporator 7；The cryogen liquid of evaporator 7 absorbs waste heat into refrigerant vapour, the cryogen that evaporator 7 is produced Steam is supplied to absorber 4, forms the 5th class absorption heat pump.
What the 5th class absorption heat pump shown in Figure 18 was realized in：
(1) in structure, in the 5th class absorption heat pump shown in Figure 12, the 5th generator, the 4th solution heat exchange are increased Device and the 3rd absorber, have weak solution pipeline to be absorbed through the solution heat exchanger 17 and second of solution pump 10 and the 3rd absorber 4 The connection of device 24 is adjusted to absorber 4 has weak solution pipeline to be connected with the 3rd absorber 25 through the 4th solution heat exchanger 22, and the 3rd Absorber 25 has weak solution pipeline to be connected with the second absorber 24 through the solution heat exchanger 17 of solution pump 10 and the 3rd again, by the 3rd Generator 3 has concentrated solution pipeline to be connected with absorber 4 and be adjusted to the 3rd through the second solution pump 11 and the second solution heat exchanger 13 Generator 3 has concentrated solution pipeline to be connected with the 5th generator 19 through the second solution heat exchanger 13, and the 5th generator 19 has dense again Solution line is connected through the second solution pump 11 and the 4th solution heat exchanger 22 with absorber 4, and the 5th generator 19 also has cryogen Steam channel is connected with the 3rd absorber 25, and the 5th generator 19 also has surplus heat medium pipeline and ft connection, the 3rd absorber 25 also have cooling medium pipeline and ft connection.
(2) in flow, the weak solution of absorber 4 enters the 3rd absorber 25, absorbs cold through the 4th solution heat exchanger 22 , in cooling medium, the weak solution of the 3rd absorber 25 enters through the solution heat exchanger 17 of solution pump 10 and the 3rd for agent steam and heat release Second absorber 24；The concentrated solution of the 3rd generator 3 enters the 5th generator 19, waste heat medium through the second solution heat exchanger 13 Flow through the 5th generator 19, heating to be provided into the solution release refrigerant vapour in it and to the 3rd absorber 25, the 5th occurs The concentrated solution of device 19 enters absorber 4 through the second solution pump 11 and the 4th solution heat exchanger 22, forms the 5th kind absorption type heat Pump.
What the 5th class absorption heat pump shown in Figure 19 was realized in：
(1) in structure, in the 5th 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 absorber 4 evaporator 7 and are adjusted to evaporator 7 and have Refrigerant steam channel is connected with newly-increased absorber B, and newly-increased absorber B also has weak solution pipeline through new solubilization liquid 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 4, and newly-increased generator A also has driving heat Medium pipeline and ft connection, newly-increased absorber B also have heated medium pipeline and ft connection.
(2) in flow, the refrigerant vapour that evaporator 7 is produced enters newly-increased absorber B, increases the weak solution warp of absorber B newly New solubilization liquid pump C and newly-increased solution heat exchanger D enters newly-increased generator A, drives thermal medium to flow through newly-increased generator A, heating Solution in into it discharges refrigerant vapour and is provided to absorber 4, 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 5th class absorption heat pump.
What the 5th class absorption heat pump shown in Figure 20 was realized in：
(1) in structure, in the 5th class absorption heat pump shown in Fig. 1, generator 1 there are into refrigerant steam channel and condenser 5 connections are adjusted to generator 1 has refrigerant steam channel to be connected with newly-increased absorber B, and newly-increased absorber B also has weak solution pipeline to pass 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 Solubilized 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 condenser 5, newly Increase generator A and also have driving heat medium pipeline and ft connection, newly-increased absorber B also has heated medium pipeline to connect with outside It is logical.
(2) in flow, the refrigerant vapour that generator 1 is produced enters newly-increased absorber B, increases the weak solution warp of absorber B newly New solubilization liquid pump C and newly-increased solution heat exchanger D enters newly-increased generator A, drives thermal medium to flow 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 5th class absorption heat pump.
What the 5th class absorption heat pump shown in Figure 21 was realized in：
In the 5th class absorption heat pump shown in Fig. 1, the 3rd generator 3 sets up waste heat medium pipeline and ft connection；It is cold Agent liquid and waste heat medium flow through the 3rd generator 3, and heating is carried into the solution release refrigerant vapour in it and to the second condenser 6 For forming the 5th class absorption heat pump.
What the 5th class absorption heat pump shown in Figure 22 was realized in：
(1) in structure, in the 5th 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 condenser 6 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 are 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 condenser 6, new additional issue Raw device A also has surplus heat medium pipeline and ft connection, and newly-increased absorber B also has cooling medium pipeline and ft connection.
(2) in flow, the refrigerant vapour that the second generator 2 is produced enters newly-increased absorber B, increases the dilute molten of absorber B newly Liquid enters newly-increased generator A through new solubilization liquid 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 condenser 6, 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.
What the 5th class absorption heat pump shown in Figure 23 was realized in：
In the 5th class absorption heat pump shown in Figure 19, the 3rd generator 3 there are into refrigerant steam channel and the second condenser 6 Connection is adjusted to the 3rd generator 3 has refrigerant steam channel to be connected with newly-increased absorber B, forms the 5th class absorption heat pump.
What the 5th class absorption heat pump shown in Figure 24 was realized in：
In the 5th class absorption heat pump shown in Fig. 1, have a surplus heat medium pipeline and ft connection of the second generator 2 is adjusted For the 3rd generator 3 is had a surplus heat medium pipeline and ft connection, there is cryogen liquid pipeline to be connected with the 3rd generator 3 condenser 5 The 3rd generator 3 has cryogen liquid pipeline to be connected with evaporator 7 through choke valve 8 and is adjusted to condenser 5 and has cryogen liquid pipeline again afterwards Second generator 2 has cryogen liquid pipeline to be connected with evaporator 7 through choke valve 8 again after being connected with the second generator 2, forms the 5th Class absorption heat pump.
What the 5th class absorption heat pump shown in Figure 25 was realized in：
(1) in structure, in the 5th class absorption heat pump shown in Fig. 1, increase newly-increased condenser, newly-increased choke valve and increase newly Solution choke valve, has concentrated solution pipeline to be connected with the 3rd generator 3 in second generator 2 and is adjusted to the second generator 2 and has dense molten Liquid pipeline is connected through new solubilization liquid choke valve G with the 3rd generator 3, has refrigerant steam channel cold with second in second generator 2 The connection of condenser 6 is adjusted to the second generator 2 has refrigerant steam channel to be connected with newly-increased condenser E, and newly-increased condenser E also has cryogen Liquid pipeline is connected through newly-increased choke valve F with the second condenser 6, and newly-increased condenser E also has cooling medium pipeline and ft connection.
(2) in flow, the concentrated solution of the second generator 2 enters the 3rd generator through new solubilization liquid choke valve G reducing pressure by regulating flow 3, the refrigerant vapour that the second generator 2 is produced enters newly-increased condenser E, heat release in cooling medium into cryogen liquid, increases condenser E newly Cryogen liquid enter the second condenser 6 through newly-increased choke valve F reducing pressure by regulating flow, form the 5th class absorption heat pump.
The effect that the technology of the present invention can be realized --- the 5th class absorption heat pump proposed by the invention, with following effect Fruit and advantage：
(1) new approaches, new ideas and new technology that the temperature difference is utilized are proposed, will promote absorption heat pump technology development and Using.
(2) negative effect of the high temperature cryogen liquid to UTILIZATION OF VESIDUAL HEAT IN degree can be well solved, especially to TFE-TDE Solution is the absorption heat pump flow of Typical Representative, can significantly improve performance index and the heat energy utilization effect of absorption heat pump Rate.
(3) effectively using the temperature difference between cryogen liquid and environment, the high temperature driven heat needed for effectively reducing generator Load, improves the value of high temperature driven thermic load.
(4) input of high temperature driven thermic load can be reduced, or improves the degree of UTILIZATION OF VESIDUAL HEAT IN, or more low temperature can be utilized The residual heat resources of degree.
(5) various concrete technical schemes are given, numerous different actual states are coped with, there is the scope of application wider.
(6) type of absorption heat pump is enriched, the range of application of absorption heat pump is extended, is conducive to preferably using Absorption heat pump realizes making full use of for the temperature difference.

Claims (57)

1. the 5th class absorption heat pump, mainly by generator, the second generator, the 3rd generator, absorber, condenser, second Condenser, evaporator, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchange Device is constituted；Absorber (4) has weak solution pipeline to be connected with generator (1) through solution pump (10) and solution heat exchanger (12), Generator (1) also has concentrated solution pipeline through solution heat exchanger (12) and the second solution heat exchanger (13) and the second generator (2) connect, the second generator (2) also has concentrated solution pipeline to be connected with the 3rd generator (3), and the 3rd generator (3) also has dense molten Liquid pipeline is connected through the second solution pump (11) and the second solution heat exchanger (13) with absorber (4), and generator (1) also has cryogen Steam channel is connected with condenser (5), and the 3rd sends out after condenser (5) also has cryogen liquid pipeline to be connected with the 3rd generator (3) Raw device (3) has cryogen liquid pipeline to be connected with evaporator (7) through choke valve (8) again, the second generator (2) and the 3rd generator (3) Also there is refrigerant steam channel to be connected with the second condenser (6) respectively, the second condenser (6) also has cryogen liquid pipeline through cryogen liquid pump (9) connected with evaporator (7), evaporator (7) also has refrigerant steam channel to be connected with absorber (4), and generator (1) also has driving Heat medium pipeline and ft connection, absorber (4) and condenser (5) also have heated medium pipeline and ft connection respectively, steam Hair device (7) and the second generator (2) are also had a surplus heat medium pipeline and ft connection respectively, and the second condenser (6) also has cooling Jie Matter pipeline and ft connection, form the 5th class absorption heat pump.
2. the 5th class absorption heat pump, is in the 5th class absorption heat pump described in claim 1, to cancel choke valve, by the Three generators (3) have cryogen liquid pipeline to be connected with evaporator (7) through choke valve (8) to be adjusted to the 3rd generator (3) and have cryogen liquid Pipeline is connected with evaporator (7), forms the 5th class absorption heat pump.
3. the 5th class absorption heat pump, be in the 5th class absorption heat pump described in claim 1, increase the 4th generator, Second throttle, the 3rd solution pump, the 3rd solution heat exchanger and heat exchanger, absorber (4) set up weak solution pipeline through Three solution pumps (16) and the 3rd solution heat exchanger (17) are connected with the 4th generator (14), and the 4th generator (14) also has dense molten Liquid pipeline is connected through the 3rd solution heat exchanger (17) and the second solution heat exchanger (13) with the second generator (2), will be occurred Device (1) has refrigerant steam channel to be connected with condenser (5) to be adjusted to generator (1) and have refrigerant steam channel and the 4th generator (14) the 4th generator (14) has cryogen liquid pipeline through heat exchanger (18), the 3rd generator (3) and second section again after connecting Stream valve (15) is connected with evaporator (7), and the 4th generator (14) also has refrigerant steam channel to be connected with condenser (5), heat exchange Device (18) also has heated medium pipeline and ft connection, forms the 5th class absorption heat pump.
4. the 5th class absorption heat pump, be in the 5th class absorption heat pump described in claim 1, increase the 4th generator, Second throttle, the 3rd solution heat exchanger and heat exchanger, have weak solution pipeline through solution pump (10) and molten by absorber (4) Liquid heat exchanger (12) connected with generator (1) be adjusted to absorber (4) have weak solution pipeline through solution pump (10), solution heat hand over Parallel operation (12) and the 3rd solution heat exchanger (17) are connected with generator (1), and generator (1) is had into concentrated solution pipeline through solution heat Exchanger (12) and the second solution heat exchanger (13) connect with the second generator (2) and are adjusted to generator (1) and have concentrated solution pipe The solution heat exchangers of Lu Jing tri- (17) is connected with the 4th generator (14), and the 4th generator (14) has concentrated solution pipeline through molten again Liquid heat exchanger (12) and the second solution heat exchanger (13) are connected with the second generator (2), and generator (1) is had into refrigerant vapour Passage is connected with condenser (5) and is adjusted to the 4th after generator (1) has refrigerant steam channel to be connected with the 4th generator (14) Generator (14) has cryogen liquid pipeline through heat exchanger (18), the 3rd generator (3) and second throttle (15) and evaporator again (7) connect, the 4th generator (14) also has refrigerant steam channel to be connected with condenser (5), and heat exchanger (18) also has heated Medium pipeline and ft connection, form the 5th class absorption heat pump.
5. the 5th class absorption heat pump, be in the 5th class absorption heat pump described in claim 1, increase the 4th generator, Second throttle, the 3rd solution pump, the 3rd solution heat exchanger and heat exchanger, have weak solution pipeline through molten by absorber (4) Liquid pump (10) and solution heat exchanger (12) connect with generator (1) and are adjusted to absorber (4) and have weak solution pipeline through solution pump (10) connected with the 4th generator (14) with solution heat exchanger (12), the 4th generator (14) has concentrated solution pipeline through the 3rd again Solution pump (16) and the 3rd solution heat exchanger (17) are connected with generator (1), and generator (1) is had into concentrated solution pipeline through solution Heat exchanger (12) and the second solution heat exchanger (13) connect with the second generator (2) and are adjusted to generator (1) and have concentrated solution Pipeline is through the 3rd solution heat exchanger (17), solution heat exchanger (12) and the second solution heat exchanger (13) and the second generator (2) connect, there is refrigerant steam channel to be connected with condenser (5) in generator (1) and be adjusted to generator (1) and have refrigerant steam channel The 4th generator (14) has cryogen liquid pipeline through heat exchanger (18), the 3rd generator again after being connected with the 4th generator (14) (3) connected with evaporator (7) with second throttle (15), the 4th generator (14) also has refrigerant steam channel and condenser (5) Connection, heat exchanger (18) also has heated medium pipeline and ft connection, forms the 5th class absorption heat pump.
6. the 5th class absorption heat pump, is in any 5th class absorption heat pump described in claim 3-5, to cancel choke valve And second throttle, there is cryogen liquid pipeline to be connected with evaporator (7) through choke valve (8) in the 3rd generator (3) and be adjusted to the 3rd Generator (3) has cryogen liquid pipeline to be connected with evaporator (7), and the 3rd generator (3) is had into cryogen liquid pipeline through second throttle (15) connected with evaporator (7) and be adjusted to the 3rd generator (3) and there is cryogen liquid pipeline to be connected with evaporator (7), form the 5th class Absorption heat pump.
7. the 5th class absorption heat pump, be in the 5th class absorption heat pump described in claim 3, increase the 5th generator, 3rd choke valve, the 4th solution pump, the 4th solution heat exchanger and second heat exchanger, absorber (4) set up weak solution pipeline Connected with the 5th generator (19) through the 4th solution pump (21) and the 4th solution heat exchanger (22), the 5th generator (19) also has Concentrated solution pipeline is connected through the 4th solution heat exchanger (22) and the second solution heat exchanger (13) with the second generator (2), will 4th generator (14) has refrigerant steam channel to be connected with condenser (5) to be adjusted to the 4th generator (14) and have refrigerant steam channel The 5th generator (19) has cryogen liquid pipeline through second heat exchanger (23), the 3rd hair again after being connected with the 5th generator (19) Raw device (3) and the 3rd choke valve (20) are connected with evaporator (7), and the 5th generator (19) also has refrigerant steam channel and condenser (5) connect, the 4th generator (14) is had into cryogen liquid pipeline through heat exchanger (18), the 3rd generator (3) and second throttle (15) connected with evaporator (7) and be adjusted to the 4th generator (14) and have cryogen liquid pipeline through the 5th generator (19), heat exchanger (18), the 3rd generator (3) and second throttle (15) are connected with evaporator (7), and second heat exchanger (23) also has heated Medium pipeline and ft connection, form the 5th class absorption heat pump.
8. the 5th class absorption heat pump, be in the 5th class absorption heat pump described in claim 4, increase the 5th generator, 3rd choke valve, the 4th solution heat exchanger and second heat exchanger, have weak solution pipeline through solution pump by absorber (4) (10), solution heat exchanger (12) and the 3rd solution heat exchanger (17) connect with generator (1) and are adjusted to absorber (4) and have dilute Solution line is through solution pump (10), solution heat exchanger (12), the 4th solution heat exchanger (22) and the 3rd solution heat exchanger (17) connected with generator (1), the 4th generator (14) is had into concentrated solution pipeline through solution heat exchanger (12) and the second solution Heat exchanger (13) connected with the second generator (2) be adjusted to the 4th generator (14) have concentrated solution pipeline through the 4th solution heat hand over Parallel operation (22) is connected with the 5th generator (19), the 5th generator (19) have concentrated solution pipeline through solution heat exchanger (12) again and Second solution heat exchanger (13) is connected with the second generator (2), and the 4th generator (14) is had into refrigerant steam channel with condensation Device (5) connection is adjusted to the 5th generator after the 4th generator (14) has refrigerant steam channel to be connected with the 5th generator (19) (19) there is cryogen liquid pipeline again through second heat exchanger (23), the 3rd generator (3) and the 3rd choke valve (20) and evaporator (7) Connection, the 5th generator (19) also has refrigerant steam channel to be connected with condenser (5), the 4th generator (14) is had into cryogen liquid pipe Road connects with evaporator (7) and is adjusted to the 4th generator through heat exchanger (18), the 3rd generator (3) and second throttle (15) (14) have cryogen liquid pipeline through the 5th generator (19), heat exchanger (18), the 3rd generator (3) and second throttle (15) with Evaporator (7) is connected, and second heat exchanger (23) also has heated medium pipeline and ft connection, forms the 5th kind absorption type heat Pump.
9. the 5th class absorption heat pump, be in the 5th class absorption heat pump described in claim 5, increase the 5th generator, 3rd choke valve, the 4th solution pump, the 4th solution heat exchanger and second heat exchanger, have weak solution pipeline by absorber (4) Connected with the 4th generator (14) through solution pump (10) and solution heat exchanger (12) and be adjusted to absorber (4) and have weak solution pipeline Connected with the 5th generator (19) through solution pump (10) and solution heat exchanger (12), the 5th generator (19) has concentrated solution pipe again The solution pumps (21) of Lu Jing tetra- and the 4th solution heat exchanger (22) are connected with the 4th generator (14), and generator (1) is had Concentrated solution pipeline is through the 3rd solution heat exchanger (17), solution heat exchanger (12) and the second solution heat exchanger (13) and second Generator (2) connection is adjusted to generator (1) has concentrated solution pipeline to be handed over through the 3rd solution heat exchanger (17), the 4th solution heat Parallel operation (22), solution heat exchanger (12) and the second solution heat exchanger (13) are connected with the second generator (2), and the 4th is occurred Device (14) has refrigerant steam channel to be connected with condenser (5) to be adjusted to the 4th generator (14) and have refrigerant steam channel and the 5th hair The 5th generator (19) has cryogen liquid pipeline through second heat exchanger (23), the 3rd generator (3) again after raw device (19) connection Connected with evaporator (7) with the 3rd choke valve (20), the 5th generator (19) also has refrigerant steam channel with condenser (5) even It is logical, have cryogen liquid pipeline through heat exchanger (18), the 3rd generator (3) and second throttle (15) in the 4th generator (14) and Evaporator (7) connection is adjusted to the 4th generator (14) has cryogen liquid pipeline through the 5th generator (19), heat exchanger (18), the Three generators (3) and second throttle (15) are connected with evaporator (7), and second heat exchanger (23) also has heated medium pipeline With ft connection, the 5th class absorption heat pump is formed.
10. the 5th class absorption heat pump, is in any 5th class absorption heat pump described in claim 7-9, to cancel throttling Valve, second throttle and the 3rd choke valve, have cryogen liquid pipeline to connect through choke valve (8) and evaporator (7) in the 3rd generator (3) It is logical to be adjusted to the 3rd generator (3) and there is cryogen liquid pipeline to be connected with evaporator (7), the 3rd generator (3) there is into cryogen liquid pipeline Connected with evaporator (7) through second throttle (15) and be adjusted to the 3rd generator (3) and have cryogen liquid pipeline and evaporator (7) even It is logical, there is cryogen liquid pipeline to be connected with evaporator (7) through the 3rd choke valve (20) in the 3rd generator (3) and be adjusted to the 3rd generator (3) there is cryogen liquid pipeline to be connected with evaporator (7), form the 5th class absorption heat pump.
11. the 5th class absorption heat pumps, mainly by generator, the second generator, the 3rd generator, absorber, condenser, second Condenser, evaporator, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchange Device, the 4th generator, the 3rd solution heat exchanger and the second absorber are constituted；Absorber (4) has weak solution pipeline through the 3rd Solution heat exchanger (17) is connected with the second absorber (24), and the second absorber (24) also has weak solution pipeline through solution pump (10) Connected with solution heat exchanger (12) with generator (1), generator (1) also have concentrated solution pipeline through solution heat exchanger (12) and Second solution heat exchanger (13) is connected with the second generator (2), and the second generator (2) also has concentrated solution pipeline and the 3rd generation Device (3) is connected, and the 3rd generator (3) has concentrated solution pipeline to connect through the second solution heat exchanger (13) and the 4th generator (14) Logical, the 4th generator (14) also has concentrated solution pipeline through the second solution pump (11) and the 3rd solution heat exchanger (17) and absorber (4) connect, generator (1) also has refrigerant steam channel to be connected with condenser (5), and condenser (5) has cryogen liquid pipeline and the 3rd The 3rd generator (3) has cryogen liquid pipeline through the 4th generator (14) and choke valve (8) and evaporation again after generator (3) connection Device (7) is connected, and the second generator (2) and the 3rd generator (3) also have refrigerant steam channel with the second condenser (6) even respectively Logical, the second condenser (6) also has cryogen liquid pipeline to be connected with evaporator (7) through cryogen liquid pump (9), and the 4th generator (14) also has Refrigerant steam channel is connected with the second absorber (24), and evaporator (7) also has refrigerant steam channel to be connected with absorber (4), hair Raw device (1) also has driving heat medium pipeline and ft connection, and absorber (4) and condenser (5) also have heated medium pipe respectively Road and ft connection, evaporator (7) and the second generator (2) are also had a surplus heat medium pipeline and ft connection respectively, the second condensation Device (6) and the second absorber (24) also have cooling medium pipeline and ft connection respectively, form the 5th class absorption heat pump.
12. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in claim 11, to cancel choke valve, will 4th generator (14) has cryogen liquid pipeline to be connected with evaporator (7) through choke valve (8) to be adjusted to the 4th generator (14) and have cold Agent liquid pipeline is connected with evaporator (7), forms the 5th class absorption heat pump.
13. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in claim 11, to increase the 5th and occur Device, second throttle, the 3rd solution pump, the 4th solution heat exchanger and heat exchanger, the second absorber (24) set up weak solution Pipeline is connected through the 3rd solution pump (16) and the 4th solution heat exchanger (22) with the 5th generator (19), the 5th generator (19) Also concentrated solution pipeline connects through the 4th solution heat exchanger (22) and the second solution heat exchanger (13) with the second generator (2) It is logical, there is refrigerant steam channel to be connected with condenser (5) in generator (1) and be adjusted to generator (1) and have refrigerant steam channel and the Five generators (19) connection after the 5th generator (19) have again cryogen liquid pipeline through heat exchanger (18), the 3rd generator (3), 4th generator (14) and second throttle (15) are connected with evaporator (7), and the 5th generator (19) also has refrigerant steam channel Connected with condenser (5), heat exchanger (18) also has heated medium pipeline and ft connection, form the 5th kind absorption type heat Pump.
14. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in claim 11, to increase the 5th and occur Device, second throttle, the 4th solution heat exchanger and heat exchanger, have weak solution pipeline through solution pump by the second absorber (24) (10) connected with generator (1) and be adjusted to the second absorber (24) and have weak solution pipeline through solution pump with solution heat exchanger (12) (10), solution heat exchanger (12) and the 4th solution heat exchanger (22) are connected with generator (1), and generator (1) is had into dense molten Liquid pipeline is connected with the second generator (2) through solution heat exchanger (12) and the second solution heat exchanger (13) and is adjusted to generator (1) concentrated solution pipeline is connected with the 5th generator (19) through the 4th solution heat exchanger (22), the 5th generator (19) has again Concentrated solution pipeline is connected through solution heat exchanger (12) and the second solution heat exchanger (13) with the second generator (2), will be occurred Device (1) has refrigerant steam channel to be connected with condenser (5) to be adjusted to generator (1) and have refrigerant steam channel and the 5th generator (19) the 5th generator (19) has cryogen liquid pipeline to occur through heat exchanger (18), the 3rd generator (3), the 4th again after connecting Device (14) and second throttle (15) are connected with evaporator (7), and the 5th generator (19) also has refrigerant steam channel and condenser (5) connect, heat exchanger (18) also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
15. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in claim 11, to increase the 5th and occur Device, second throttle, the 3rd solution pump, the 4th solution heat exchanger and heat exchanger, have weak solution by the second absorber (24) Pipeline connects with generator (1) through solution pump (10) and solution heat exchanger (12) and is adjusted to the second absorber (24) and has weak solution Pipeline is connected through solution pump (10) and solution heat exchanger (12) with the 5th generator (19), and the 5th generator (19) has dense molten again Liquid pipeline is connected through the 3rd solution pump (16) and the 4th solution heat exchanger (22) with generator (1), and generator (1) is had into dense molten Liquid pipeline is connected with the second generator (2) through solution heat exchanger (12) and the second solution heat exchanger (13) and is adjusted to generator (1) there is concentrated solution pipeline through the 4th solution heat exchanger (22), solution heat exchanger (12) and the second solution heat exchanger (13) Connected with the second generator (2), there is refrigerant steam channel to be connected with condenser (5) in generator (1) and be adjusted to generator (1) and have The 5th generator (19) has cryogen liquid pipeline through heat exchanger again after refrigerant steam channel is connected with the 5th generator (19) (18), the 3rd generator (3), the 4th generator (14) and second throttle (15) are connected with evaporator (7), the 5th generator (19) refrigerant steam channel is connected with condenser (5), heat exchanger (18) also has heated medium pipeline and ft connection, Form the 5th class absorption heat pump.
16. the 5th class absorption heat pumps, are in any 5th class absorption heat pump described in claim 13-15, to cancel section Stream valve and second throttle, have cryogen liquid pipeline to be connected with evaporator (7) through choke valve (8) in the 4th generator (14) and are adjusted to 4th generator (14) has cryogen liquid pipeline to be connected with evaporator (7), and the 4th generator (14) is had into cryogen liquid pipeline through second Choke valve (15) connects with evaporator (7) and is adjusted to the 4th generator (14) and has cryogen liquid pipeline to be connected with evaporator (7), is formed 5th class absorption heat pump.
17. the 5th class absorption heat pumps, be in the 5th class absorption heat pump described in claim 1, increase the 4th generator, 3rd solution pump, the 3rd solution heat exchanger and the second absorber, have weak solution pipeline through solution pump (10) absorber (4) and Solution heat exchanger (12) connects with generator (1) and is adjusted to absorber (4) and has weak solution pipeline through solution pump (10) and the 3rd Solution heat exchanger (17) is connected with the second absorber (24), and the second absorber (24) has weak solution pipeline through the 3rd solution pump again (16) connected with generator (1) with solution heat exchanger (12), generator (1) is had into concentrated solution pipeline through solution heat exchanger (12) connected with the second generator (2) and be adjusted to generator (1) and have concentrated solution pipeline through molten with the second solution heat exchanger (13) Liquid heat exchanger (12) is connected with the 4th generator (14), and the 4th generator (14) has concentrated solution pipeline to be handed over through the 3rd solution heat again Parallel operation (17) and the second solution heat exchanger (13) are connected with the second generator (2), and the 4th generator (14) also has refrigerant vapour Passage is connected with the second absorber (24), and the 4th generator (14) also has driving heat medium pipeline and ft connection, and second absorbs Device (24) also has heated medium pipeline and ft connection, forms the 5th class absorption heat pump.
18. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in claim 17, to cancel choke valve, will 3rd generator (3) has cryogen liquid pipeline to be connected with evaporator (7) through choke valve (8) to be adjusted to the 3rd generator (3) and have cryogen Liquid pipeline is connected with evaporator (7), forms the 5th class absorption heat pump.
19. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in claim 17, to increase the 5th and occur Device, second throttle, the 4th solution pump, the 4th solution heat exchanger and heat exchanger, the second absorber (24) set up weak solution Pipeline is connected through the 4th solution pump (21) and the 4th solution heat exchanger (22) with the 5th generator (19), the 5th generator (19) Also concentrated solution pipeline is connected through the 4th solution heat exchanger (22) with the 4th generator (14), has cryogen to steam in generator (1) Vapour passage is connected with condenser (5) and is adjusted to after generator (1) has refrigerant steam channel to be connected with the 5th generator (19) Five generators (19) have cryogen liquid pipeline through heat exchanger (18), the 3rd generator (3) and second throttle (15) and evaporation again Device (7) is connected, and the 5th generator (19) also has refrigerant steam channel to be connected with condenser (5), and heat exchanger (18) also has and added Heat medium pipeline and ft connection, form the 5th class absorption heat pump.
20. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in claim 17, to increase the 5th and occur Device, second throttle, the 4th solution heat exchanger and heat exchanger, have weak solution pipeline molten through the 3rd second absorber (24) Liquid pump (16) and solution heat exchanger (12) connect with generator (1) and are adjusted to the second absorber (24) and have weak solution pipeline through Three solution pumps (16), solution heat exchanger (12) and the 4th solution heat exchanger (22) are connected with generator (1), by generator (1) there is concentrated solution pipeline to be connected with the 4th generator (14) through solution heat exchanger (12) to be adjusted to generator (1) and have concentrated solution Pipeline is connected through the 4th solution heat exchanger (22) with the 5th generator (19), and the 5th generator (19) has concentrated solution pipeline to pass through again Solution heat exchanger (12) is connected with the 4th generator (14), has refrigerant steam channel to be connected with condenser (5) in generator (1) The 5th generator (19) has cryogen liquid again after being adjusted to generator (1) and having refrigerant steam channel to be connected with the 5th generator (19) Pipeline is connected through heat exchanger (18), the 3rd generator (3) and second throttle (15) with evaporator (7), the 5th generator (19) refrigerant steam channel is connected with condenser (5), heat exchanger (18) also has heated medium pipeline and ft connection, Form the 5th class absorption heat pump.
21. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in claim 17, to increase the 5th and occur Device, second throttle, the 4th solution pump, the 4th solution heat exchanger and heat exchanger, have weak solution by the second absorber (24) Pipeline connects with generator (1) through the 3rd solution pump (16) and solution heat exchanger (12) and is adjusted to the second absorber (24) and has dilute Solution line is connected through the 3rd solution pump (16) and solution heat exchanger (12) with the 5th generator (19), the 5th generator (19) There is concentrated solution pipeline to be connected with generator (1) through the 4th solution pump (21) and the 4th solution heat exchanger (22) again, by generator (1) there is concentrated solution pipeline to be connected with the 4th generator (14) through solution heat exchanger (12) to be adjusted to generator (1) and have concentrated solution Pipeline is connected through the 4th solution heat exchanger (22) and solution heat exchanger (12) with the 4th generator (14), by generator (1) There is refrigerant steam channel to be connected with condenser (5) to be adjusted to generator (1) and have refrigerant steam channel and the 5th generator (19) even 5th generator (19) has cryogen liquid pipeline through heat exchanger (18), the 3rd generator (3) and second throttle again after logical (15) connected with evaporator (7), the 5th generator (19) also has refrigerant steam channel to be connected with condenser (5), heat exchanger (18) there are heated medium pipeline and ft connection, form the 5th class absorption heat pump.
22. the 5th class absorption heat pumps, are the 5th hairs in any 5th class absorption heat pump described in claim 19-21 Raw device (19) sets up driving heat medium pipeline and ft connection, forms the 5th class absorption heat pump.
23. the 5th class absorption heat pumps, are in any 5th class absorption heat pump described in claim 19-22, to cancel section Stream valve and second throttle, have cryogen liquid pipeline to be connected with evaporator (6) through choke valve (8) in the 3rd generator (3) and are adjusted to 3rd generator (3) has cryogen liquid pipeline to be connected with evaporator (7), and the 3rd generator (3) is had into cryogen liquid pipeline through second section Stream valve (15) connects with evaporator (7) and is adjusted to the 3rd generator (3) and has cryogen liquid pipeline to be connected with evaporator (7), formation the Five class absorption heat pumps.
24. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in claim 17, to increase the 5th and occur Device, the 4th solution heat exchanger and the 3rd absorber, have weak solution pipeline through solution pump (10) and the 3rd solution by absorber (4) Heat exchanger (17) connects with the second absorber (24) and is adjusted to absorber (4) and has weak solution pipeline through the 4th solution heat exchanger (22) connected with the 3rd absorber (25), the 3rd absorber (25) has weak solution pipeline through solution pump (10) and the 3rd solution heat again Exchanger (17) is connected with the second absorber (24), have concentrated solution pipeline through the second solution pump (11) in the 3rd generator (3) and Second solution heat exchanger (13) connects with absorber (4) and is adjusted to the 3rd generator (3) and has concentrated solution pipeline through the second solution Heat exchanger (13) is connected with the 5th generator (19), and the 5th generator (19) has concentrated solution pipeline through the second solution pump (11) again Connected with absorber (4) with the 4th solution heat exchanger (22), the 5th generator (19) also has refrigerant steam channel and the 3rd suction Device (25) connection is received, again there be the 3rd generator (3) after thering is cryogen liquid pipeline to be connected with the 3rd generator (3) condenser (5) Cryogen liquid pipeline connects with evaporator (7) through choke valve (8) and is adjusted to condenser (5) and has cryogen liquid pipeline and the 3rd generator (3) the 3rd generator (3) has cryogen liquid pipeline through the 5th generator (19) and choke valve (8) and evaporator (7) again after connecting Connection, the 3rd absorber (25) also has cooling medium pipeline and ft connection, forms the 5th class absorption heat pump.
25. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in claim 24, to cancel choke valve, will 5th generator (19) has cryogen liquid pipeline to be connected with evaporator (7) through choke valve (8) to be adjusted to the 5th generator (19) and have cold Agent liquid pipeline is connected with evaporator (7), forms the 5th class absorption heat pump.
26. the 5th class absorption heat pumps, mainly by generator, the second generator, the 3rd generator, absorber, condenser, second Condenser, evaporator, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchange Device, the 4th generator, the 3rd solution heat exchanger and the second absorber are constituted；Absorber (4) has weak solution pipeline through the 3rd Solution heat exchanger (17) is connected with the second absorber (24), and the second absorber (24) also has weak solution pipeline through solution pump (10) Connected with solution heat exchanger (12) with generator (1), generator (1) also have concentrated solution pipeline through solution heat exchanger (12) and Second solution heat exchanger (13) is connected with the second generator (2), and the second generator (2) also has concentrated solution pipeline and the 3rd generation Device (3) is connected, and the 3rd generator (3) has concentrated solution pipeline to connect through the second solution heat exchanger (13) and the 4th generator (14) Logical, the 4th generator (14) also has concentrated solution pipeline through the second solution pump (11) and the 3rd solution heat exchanger (17) and absorber (4) connect, generator (1) also has refrigerant steam channel to be connected with condenser (5), and condenser (5) has cryogen liquid pipeline and the 3rd The 3rd generator (3) has cryogen liquid pipeline to be connected with evaporator (7) through choke valve (8) again after generator (3) connection, the second hair Raw device (2) and the 3rd generator (3) also have refrigerant steam channel to be connected with the second condenser (6) respectively, and the second condenser (6) is also There is cryogen liquid pipeline to be connected with evaporator (7) through cryogen liquid pump (9), the 4th generator (14) also has refrigerant steam channel and second Absorber (24) is connected, and evaporator (7) also has refrigerant steam channel to be connected with absorber (4), and generator (1) also has driving heat to be situated between Matter pipeline and ft connection, absorber (4) and condenser (5) also have heated medium pipeline and ft connection, evaporator respectively (7), the second generator (2) and the 4th generator (14) are also had a surplus heat medium pipeline and ft connection, the second condenser (6) respectively Also there are cooling medium pipeline and ft connection respectively with the second absorber (24), form the 5th class absorption heat pump.
27. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in claim 26, to cancel choke valve, will 3rd generator (3) has cryogen liquid pipeline to be connected with evaporator (7) through choke valve (8) to be adjusted to the 3rd generator (3) and have cryogen Liquid pipeline is connected with evaporator (7), forms the 5th class absorption heat pump.
28. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in claim 11, to increase the 5th and occur Device, second throttle, the 3rd solution pump, the 4th solution heat exchanger and heat exchanger, the second absorber (24) set up weak solution Pipeline is connected through the 3rd solution pump (16) and the 4th solution heat exchanger (22) with the 5th generator (19), the 5th generator (19) Also concentrated solution pipeline connects through the 4th solution heat exchanger (22) and the second solution heat exchanger (13) with the second generator (2) It is logical, there is refrigerant steam channel to be connected with condenser (5) in generator (1) and be adjusted to generator (1) and have refrigerant steam channel and the The 5th generator (19) has cryogen liquid pipeline through heat exchanger (18), the 3rd generator (3) again after five generators (19) connection Connected with second throttle (15) with evaporator (7), the 5th generator (19) also has refrigerant steam channel with condenser (5) even Logical, heat exchanger (18) also has heated medium pipeline and ft connection, forms the 5th class absorption heat pump.
29. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in claim 11, to increase the 5th and occur Device, second throttle, the 4th solution heat exchanger and heat exchanger, have weak solution pipeline through solution pump by the second absorber (24) (10) connected with generator (1) and be adjusted to the second absorber (24) and have weak solution pipeline through solution pump with solution heat exchanger (12) (10), solution heat exchanger (12) and the 4th solution heat exchanger (22) are connected with generator (1), and generator (1) is had into dense molten Liquid pipeline is connected with the second generator (2) through solution heat exchanger (12) and the second solution heat exchanger (13) and is adjusted to generator (1) concentrated solution pipeline is connected with the 5th generator (19) through the 4th solution heat exchanger (22), the 5th generator (19) has again Concentrated solution pipeline is connected through solution heat exchanger (12) and the second solution heat exchanger (13) with the second generator (2), will be occurred Device (1) has refrigerant steam channel to be connected with condenser (5) to be adjusted to generator (1) and have refrigerant steam channel and the 5th generator (19) the 5th generator (19) has cryogen liquid pipeline through heat exchanger (18), the 3rd generator (3) and second section again after connecting Stream valve (15) is connected with evaporator (7), and the 5th generator (19) also has refrigerant steam channel to be connected with condenser (5), heat exchange Device (18) also has heated medium pipeline and ft connection, forms the 5th class absorption heat pump.
30. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in claim 11, to increase the 5th and occur Device, second throttle, the 3rd solution pump, the 4th solution heat exchanger and heat exchanger, have weak solution by the second absorber (24) Pipeline connects with generator (1) through solution pump (10) and solution heat exchanger (12) and is adjusted to the second absorber (24) and has weak solution Pipeline is connected through solution pump (10) and solution heat exchanger (12) with the 5th generator (19), and the 5th generator (19) has dense molten again Liquid pipeline is connected through the 3rd solution pump (16) and the 4th solution heat exchanger (22) with generator (1), and generator (1) is had into dense molten Liquid pipeline is connected with the second generator (2) through solution heat exchanger (12) and the second solution heat exchanger (13) and is adjusted to generator (1) there is concentrated solution pipeline through the 4th solution heat exchanger (22), solution heat exchanger (12) and the second solution heat exchanger (13) Connected with the second generator (2), there is refrigerant steam channel to be connected with condenser (5) in generator (1) and be adjusted to generator (1) and have The 5th generator (19) has cryogen liquid pipeline through heat exchanger again after refrigerant steam channel is connected with the 5th generator (19) (18), the 3rd generator (3) and second throttle (15) are connected with evaporator (7), and the 5th generator (19) also has refrigerant vapour Passage is connected with condenser (5), and heat exchanger (18) also has heated medium pipeline and ft connection, forms the 5th kind absorption type Heat pump.
31. the 5th class absorption heat pumps, are in any 5th class absorption heat pump described in claim 28-30, to cancel section Stream valve and second throttle, have cryogen liquid pipeline to be connected with evaporator (7) through choke valve (8) in the 3rd generator (3) and are adjusted to 3rd generator (3) has cryogen liquid pipeline to be connected with evaporator (7), and the 3rd generator (3) is had into cryogen liquid pipeline through second section Stream valve (15) connects with evaporator (7) and is adjusted to the 3rd generator (3) and has cryogen liquid pipeline to be connected with evaporator (7), formation the Five class absorption heat pumps.
32. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in claim 17, to increase the 5th and occur Device, the 4th solution heat exchanger and the 3rd absorber, have weak solution pipeline through solution pump (10) and the 3rd solution by absorber (4) Heat exchanger (17) connects with the second absorber (24) and is adjusted to absorber (4) and has weak solution pipeline through the 4th solution heat exchanger (22) connected with the 3rd absorber (25), the 3rd absorber (25) has weak solution pipeline through solution pump (10) and the 3rd solution heat again Exchanger (17) is connected with the second absorber (24), have concentrated solution pipeline through the second solution pump (11) in the 3rd generator (3) and Second solution heat exchanger (13) connects with absorber (4) and is adjusted to the 3rd generator (3) and has concentrated solution pipeline through the second solution Heat exchanger (13) is connected with the 5th generator (19), and the 5th generator (19) has concentrated solution pipeline through the second solution pump (11) again Connected with absorber (4) with the 4th solution heat exchanger (22), the 5th generator (19) also has refrigerant steam channel and the 3rd suction Device (25) connection is received, the 5th generator (19) also has surplus heat medium pipeline and ft connection, and the 3rd absorber (25) also has cooling Medium pipeline and ft connection, form the 5th class absorption heat pump.
33. the 5th class absorption heat pumps, are in the 5th class absorption heat pump described in claim 32, to cancel choke valve, will 3rd generator (3) has cryogen liquid pipeline to be connected with evaporator (7) through choke valve (8) to be adjusted to the 3rd generator (3) and have cryogen Liquid pipeline is connected with evaporator (7), forms the 5th class absorption heat pump.
34. the 5th class absorption heat pumps, are in any 5th class absorption heat pump described in claim 1-33, to increase newly-increased Generator, newly-increased absorber, new solubilization liquid pump and newly-increased solution heat exchanger, evaporator (7) is had refrigerant steam channel and inhaled Receipts device (4) connection is adjusted to evaporator (7) has refrigerant steam channel to be connected with newly-increased absorber (B), and newly-increased absorber (B) also has Weak solution pipeline is connected through new solubilization liquid 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 with newly-increased absorber (B) through newly-increased solution heat exchanger (D), increase generator (A) newly also cold Agent steam channel is connected with absorber (4), and newly-increased generator (A) also has driving heat medium pipeline and ft connection, increases newly and absorbs Device (B) also has heated medium pipeline and ft connection, forms the 5th class absorption heat pump.
35. the 5th class absorption heat pumps, are in any 5th described in claim 1-2,11-12,17-18,24-27,32-33 In class absorption heat pump, increase newly-increased generator, newly-increased absorber, new solubilization liquid pump and newly-increased solution heat exchanger, will occur Device (1) has refrigerant steam channel to be connected with condenser (5) to be adjusted to generator (1) and have refrigerant steam channel with newly-increased absorber (B) connect, newly-increased absorber (B) also have weak solution pipeline through new solubilization liquid pump (C) and newly-increased solution heat exchanger (D) with increase newly Generator (A) is connected, and newly-increased generator (A) also has concentrated solution pipeline through newly-increased solution heat exchanger (D) and newly-increased absorber (B) Connection, newly-increased generator (A) also has refrigerant steam channel to be connected with condenser (5), and newly-increased generator (A) also has driving thermal medium Pipeline and ft connection, newly-increased absorber (B) also have heated medium pipeline and ft connection, form the 5th kind absorption type heat Pump.
36. the 5th class absorption heat pumps, are in any 5th kind absorption type heat described in claim 1-10,17-23,26-33 In pump, the 3rd generator (3) sets up waste heat medium pipeline and ft connection, forms the 5th class absorption heat pump.
37. the 5th class absorption heat pumps, are the 3rd hairs in any 5th class absorption heat pump described in claim 11-16 Raw device (3) and the 4th generator (14) set up waste heat medium pipeline and ft connection respectively, form the 5th class absorption heat pump.
38. the 5th class absorption heat pumps, are the 3rd hairs in any 5th class absorption heat pump described in claim 11-16 Raw device (3) or the 4th generator (14) set up waste heat medium pipeline and ft connection, form the 5th class absorption heat pump.
39. the 5th class absorption heat pumps, are the 3rd hairs in any 5th class absorption heat pump described in claim 24-25 Raw device (3) and the 5th generator (19) set up waste heat medium pipeline and ft connection respectively, form the 5th class absorption heat pump.
40. the 5th class absorption heat pumps, are the 3rd hairs in any 5th class absorption heat pump described in claim 24-25 Raw device (3) or the 5th generator (19) set up waste heat medium pipeline and ft connection, form the 5th class absorption heat pump.
41. the 5th class absorption heat pumps, are in any 5th class absorption heat pump described in claim 36-40, to increase new Increase generator, newly-increased absorber, new solubilization liquid pump and newly-increased solution heat exchanger, by evaporator (7) have refrigerant steam channel with Absorber (4) connection is adjusted to evaporator (7) has refrigerant steam channel to be connected with newly-increased absorber (B), increases absorber (B) newly also There is weak solution pipeline to be connected with newly-increased generator (A) through new solubilization liquid pump (C) and newly-increased solution heat exchanger (D), increase newly and occur Device (A) also has concentrated solution pipeline to be connected with newly-increased absorber (B) through newly-increased solution heat exchanger (D), and newly-increased generator (A) also has Refrigerant steam channel is connected with absorber (4), and newly-increased generator (A) also has driving heat medium pipeline and ft connection, increases newly and inhales Receive device (B) and also have heated medium pipeline and ft connection, form the 5th class absorption heat pump.
42. the 5th class absorption heat pumps, are in any 5th class absorption heat pump described in claim 1-33, to increase newly-increased Generator, newly-increased absorber, new solubilization liquid pump and newly-increased solution heat exchanger, have refrigerant steam channel by the 3rd generator (3) Connected with the second condenser (6) and be adjusted to the 3rd generator (3) 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 with newly-increased generator (A) through new solubilization liquid pump (C) and newly-increased solution heat exchanger (D) Logical, newly-increased generator (A) also has concentrated solution pipeline to be connected with newly-increased absorber (B) through newly-increased solution heat exchanger (D), new additional issue Raw device (A) also has refrigerant steam channel to be connected with the second condenser (6), increase newly generator (A) also have surplus heat medium pipeline with it is outer Portion connects, and newly-increased absorber (B) also has cooling medium pipeline and ft connection, forms the 5th class absorption heat pump.
43. the 5th class absorption heat pumps, are in any 5th class absorption heat pump described in claim 1-10,17-23, to increase Plus newly-increased generator, newly-increased absorber, new solubilization liquid pump and newly-increased solution heat exchanger, there is cryogen to steam in the second generator (2) Vapour passage connects with the second condenser (6) and is adjusted to the second generator (2) and has refrigerant steam channel and newly-increased absorber (B) even Logical, newly-increased absorber (B) also has weak solution pipeline through new solubilization liquid pump (C) and newly-increased solution heat exchanger (D) and newly-increased generation Device (A) is connected, and newly-increased generator (A) also has concentrated solution pipeline to connect through newly-increased solution heat exchanger (D) and newly-increased absorber (B) Logical, newly-increased generator (A) also has refrigerant steam channel to be connected with the second condenser (6), increases generator (A) newly and also has surplus heat medium Pipeline and ft connection, newly-increased absorber (B) also have cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
44. the 5th class absorption heat pumps, are in any 5th class absorption heat pump described in claim 43, the 3rd is occurred Device (3) has refrigerant steam channel to be connected with the second condenser (6) to be adjusted to the 3rd generator (3) and have refrigerant steam channel and newly-increased Absorber (B) is connected, and forms the 5th class absorption heat pump.
45. the 5th class absorption heat pumps, are the 3rd hairs in any 5th class absorption heat pump described in claim 42-44 Raw device (3) sets up waste heat medium pipeline and ft connection, forms the 5th class absorption heat pump.
46. the 5th class absorption heat pumps, are in any 5th class absorption heat pump described in claim 11-16, to increase new Increase generator, newly-increased absorber, new solubilization liquid pump and newly-increased solution heat exchanger, there is refrigerant vapour to lead in the 4th generator (14) Road connects with the second absorber (24) and is adjusted to the 4th generator (14) and has refrigerant steam channel to be connected with newly-increased absorber (B), Newly-increased absorber (B) also has weak solution pipeline through new solubilization liquid pump (C) and newly-increased solution heat exchanger (D) and newly-increased generator (A) connect, newly-increased generator (A) also has concentrated solution pipeline to be connected with newly-increased absorber (B) through newly-increased solution heat exchanger (D), Newly-increased generator (A) also has refrigerant steam channel to be connected with the second absorber (24), increases generator (A) newly and also has surplus heat medium tube Road and ft connection, newly-increased absorber (B) also have cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
47. the 5th class absorption heat pumps, are the 3rd generators in any 5th class absorption heat pump described in claim 46 (3) and the 4th generator (14) sets up waste heat medium pipeline and ft connection respectively, the 5th class absorption heat pump is formed.
48. the 5th class absorption heat pumps, are the 3rd generators in any 5th class absorption heat pump described in claim 46 (3) or the 4th generator (14) sets up waste heat medium pipeline and ft connection, the 5th class absorption heat pump is formed.
49. the 5th class absorption heat pumps, are in any 5th class absorption heat pump described in claim 24-25, to increase new Increase generator, newly-increased absorber, new solubilization liquid pump and newly-increased solution heat exchanger, there is refrigerant vapour to lead in the 5th generator (19) Road connects with the 3rd absorber (25) and is adjusted to the 5th generator (19) and has refrigerant steam channel to be connected with newly-increased absorber (B), Newly-increased absorber (B) also has weak solution pipeline through new solubilization liquid pump (C) and newly-increased solution heat exchanger (D) and newly-increased generator (A) connect, newly-increased generator (A) also has concentrated solution pipeline to be connected with newly-increased absorber (B) through newly-increased solution heat exchanger (D), Newly-increased generator (A) also has refrigerant steam channel to be connected with the 3rd absorber (25), increases generator (A) newly and also has surplus heat medium tube Road and ft connection, newly-increased absorber (B) also have cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
50. the 5th class absorption heat pumps, are the 3rd generators in any 5th class absorption heat pump described in claim 49 (3) and the 5th generator (19) sets up waste heat medium pipeline and ft connection respectively, the 5th class absorption heat pump is formed.
51. the 5th class absorption heat pumps, are the 3rd generators in any 5th class absorption heat pump described in claim 49 (3) or the 5th generator (19) sets up waste heat medium pipeline and ft connection, the 5th class absorption heat pump is formed.
52. the 5th class absorption heat pumps, are in any 5th class absorption heat pump described in claim 26-31, to increase new Increase generator, newly-increased absorber, new solubilization liquid pump and newly-increased solution heat exchanger, there is refrigerant vapour to lead in the 4th generator (14) Road connects with the second absorber (24) and is adjusted to the 4th generator (14) and has refrigerant steam channel to be connected with newly-increased absorber (B), Newly-increased absorber (B) also has weak solution pipeline through new solubilization liquid pump (C) and newly-increased solution heat exchanger (D) and newly-increased generator (A) connect, newly-increased generator (A) also has concentrated solution pipeline to be connected with newly-increased absorber (B) through newly-increased solution heat exchanger (D), Newly-increased generator (A) also has refrigerant steam channel to be connected with the second absorber (24), increases generator (A) newly and also has surplus heat medium tube Road and ft connection, newly-increased absorber (B) also have cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
53. the 5th class absorption heat pumps, are in any 5th class absorption heat pump described in claim 32-33, to increase new Increase generator, newly-increased absorber, new solubilization liquid pump and newly-increased solution heat exchanger, there is refrigerant vapour to lead in the 5th generator (19) Road connects with the 3rd absorber (25) and is adjusted to the 5th generator (19) and has refrigerant steam channel to be connected with newly-increased absorber (B), Newly-increased absorber (B) also has weak solution pipeline through new solubilization liquid pump (C) and newly-increased solution heat exchanger (D) and newly-increased generator (A) connect, newly-increased generator (A) also has concentrated solution pipeline to be connected with newly-increased absorber (B) through newly-increased solution heat exchanger (D), Newly-increased generator (A) also has refrigerant steam channel to be connected with the 3rd absorber (25), increases generator (A) newly and also has surplus heat medium tube Road and ft connection, newly-increased absorber (B) also have cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
54. the 5th class absorption heat pumps, are the 3rd hairs in any 5th class absorption heat pump described in claim 52-53 Raw device (3) sets up waste heat medium pipeline and ft connection, forms the 5th class absorption heat pump.
55. the 5th class absorption heat pumps, are absorbed in any 5th class described in claim 1-2,17-18,26-27,32-33 In formula heat pump, have a surplus heat medium pipeline and ft connection of the second generator (2) is adjusted to the 3rd generator (3) and had a surplus thermal medium Pipeline and ft connection, the 3rd generator (3) is again after having cryogen liquid pipeline to be connected with the 3rd generator (3) condenser (5) There is cryogen liquid pipeline to be connected with evaporator (7) through choke valve (8) to be adjusted to condenser (5) and have cryogen liquid pipeline and the second generator (2) the second generator (2) has cryogen liquid pipeline to be connected with evaporator (7) through choke valve (8) again after connecting, and forms the 5th class and inhales Receipts formula heat pump.
56. the 5th class absorption heat pumps, are in any 5th class absorption heat pump described in claim 1-41, to increase newly-increased Condenser, newly-increased choke valve and new solubilization liquid choke valve, have concentrated solution pipeline and the 3rd generator (3) by the second generator (2) Connection is adjusted to the second generator (2) has concentrated solution pipeline to be connected with the 3rd generator (3) through new solubilization liquid choke valve (G), will Second generator (2) have refrigerant steam channel connected with the second condenser (6) be adjusted to the second generator (2) have refrigerant vapour lead to Road is connected with newly-increased condenser (E), and newly-increased condenser (E) also has cryogen liquid pipeline through newly-increased choke valve (F) and the second condenser (6) or evaporator (7) connection, newly-increased condenser (E) also has cooling medium pipeline and ft connection, forms the 5th kind absorption type heat Pump.
57. the 5th class absorption heat pumps, are in any 5th class absorption heat pump described in claim 1-41, to increase newly-increased Condenser, newly-increased cryogen liquid pump and new solubilization liquid choke valve, have concentrated solution pipeline and the 3rd generator by the second generator (2) (3) connection is adjusted to the second generator (2) has concentrated solution pipeline to be connected with the 3rd generator (3) through new solubilization liquid choke valve (G), There is refrigerant steam channel to be connected with the second condenser (6) in the second generator (2) to be adjusted to the second generator (2) and have refrigerant vapour Passage is connected with newly-increased condenser (E), and newly-increased condenser (E) also has cryogen liquid pipeline through newly-increased cryogen liquid pump and evaporator (7) Connection, newly-increased condenser (E) also has cooling medium pipeline and ft connection, forms the 5th class absorption heat pump.
CN201510140717.0A 2014-03-24 2015-03-22 5th class absorption heat pump Active CN104807235B (en)

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CN106403364B (en) * 2015-10-18 2020-05-29 李华玉 Fifth type thermal driving compression-absorption heat pump
CN106403365B (en) * 2015-10-18 2020-03-17 李华玉 Fifth type thermal driving compression-absorption heat pump
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