CN104807235A - Fifth type absorption heat pump - Google Patents

Fifth type absorption heat pump Download PDF

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

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

Abstract

The invention provides a fifth type absorption heat pump, and belongs to the technical field of absorption heat pumps and waste heat utilization. An absorber is communicated with a generator through a solution pump and a solution heat exchanger, the generator is communicated with a second generator through the solution heat exchanger and a second solution heat exchanger, the second generator is communicated with a third generator, the third generator is communicated with the absorber through a second solution pump and the second solution heat exchanger, the generator is communicated with a condenser through a cryogen vapor channel, the condenser is communicated with an evaporator through a cryogen liquid pipeline, the third generator and a throttle valve, the second generator and the third generator are communicated with the second condenser through cryogen vapor channels, the second condenser is communicated with the evaporator through a cryogen liquid pump, the evaporator is communicated with the absorber through a cryogen vapor channel, the generator is communicated with the outside through a driving heat medium pipeline, the absorber and the condenser are communicated with the outside through heated-medium pipelines, the evaporator and the second generator are communicated with the outside through waste heat medium pipelines, the second condenser is communicated with the outside through a cooling medium pipeline, and the fifth type absorption heat pump is formed.

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 heat pump technical field, there is three major types absorption heat pump, for driving the first-class absorption type heat pump of the temperature difference respectively with the temperature difference between high temperature driven thermal medium and heated medium, be the second-kind absorption-type heat pump driving the temperature difference with the temperature difference between waste heat medium and cold environment (cooling medium), and simultaneously with aforementioned two kinds of temperature difference for driving the 3rd class absorption heat pump of the temperature difference.According to existing understanding or viewpoint, in the absorption heat pump of this three types, high temperature driven Thermal release is irrational in cold environment (cooling medium), not yet has the absorption heat pump flow process that technical staff proposes to be correlated with so far.
In the 3rd class absorption heat pump that high-temperature hot load is provided, those skilled in the art encounter such technical barrier: in the absorption heat pump flow process being representative with TFE-TDE solution, refrigerant vapour latent heat is little, high-temperature generator release refrigerant vapour the cryogen liquid temp that formed after heated medium of heat release is high within the condenser, sensible heat is relatively large; This causes the performance index of absorption heat pump very low, unreasonable to utilizing of high-grade heat energy, affects the effective utilization to waste heat, and the 3rd class absorption heat pump is very limited in the application in high-temperature heat supply field.
Inventor recognizes the problems referred to above, and have developed the technology new departure solved the problem, developing and to comprise between waste heat medium and cold environment (cooling medium) temperature difference for drive the temperature difference, adding with high-temperature hot load two kinds of different temperature drops as driving the 5th class absorption heat pump of the temperature difference; The invention provides and utilize the 3rd generator and the second condenser to realize poor series the 5th class absorption heat pump being utilized as basis of cryogen liquid temperature.
Summary of the invention:
Main purpose of the present invention to provide the 5th class absorption heat pump, and concrete summary of the invention subitem is described below:
1. the 5th class absorption heat pump, formed primarily of generator, the second generator, the 3rd generator, absorber, condenser, the second condenser, evaporimeter, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, absorber has weak solution pipeline to be communicated with generator with solution heat exchanger through solution pump, generator also has concentrated solution pipeline to be communicated with the second generator with the second solution heat exchanger through solution heat exchanger, second generator also has concentrated solution pipeline to be communicated with the 3rd generator, 3rd generator also has concentrated solution pipeline to be communicated with absorber with the second solution heat exchanger through the second solution pump, generator also has refrigerant steam channel to be communicated with condenser, condenser also have cryogen liquid pipeline be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline to be communicated with evaporimeter through choke valve again, second generator and the 3rd generator also have refrigerant steam channel to be communicated with the second condenser respectively, second condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant steam channel to be communicated with absorber, generator also has driving heat medium pipeline and ft connection, absorber and condenser also have heated medium pipeline and ft connection respectively, evaporimeter and the second generator also have surplus heat medium pipeline and ft connection respectively, second condenser also has cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
2. the 5th class absorption heat pump, in the 5th class absorption heat pump described in the 1st, cancel choke valve, had by the 3rd generator cryogen liquid pipeline to be communicated with evaporimeter through choke valve and be adjusted to the 3rd generator and have cryogen liquid pipeline to be communicated with evaporimeter, formation the 5th class absorption heat pump.
3. the 5th class absorption heat pump, in the 5th class absorption heat pump described in the 1st, increase by the 4th generator, second throttle, 3rd solution pump, 3rd solution heat exchanger and heat exchanger, absorber is set up weak solution pipeline and is communicated with the 4th generator with the 3rd solution heat exchanger through the 3rd solution pump, 4th generator also has concentrated solution pipeline to be communicated with the second generator with the second solution heat exchanger through the 3rd solution heat exchanger, had by generator refrigerant steam channel to be communicated with condenser to be adjusted to generator have refrigerant steam channel be communicated with the 4th generator after the 4th generator have cryogen liquid pipeline again through heat exchanger, 3rd generator is communicated with evaporimeter with second throttle, 4th generator also has refrigerant steam channel to be communicated with condenser, heat exchanger also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
4. the 5th class absorption heat pump, in the 5th class absorption heat pump described in the 1st, increase by the 4th generator, second throttle, 3rd solution heat exchanger and heat exchanger, had by absorber weak solution pipeline to be communicated with generator through solution pump and solution heat exchanger to be adjusted to absorber and to have weak solution pipeline through solution pump, solution heat exchanger is communicated with generator with the 3rd solution heat exchanger, had by generator concentrated solution pipeline to be communicated with the second generator through solution heat exchanger and the second solution heat exchanger to be adjusted to generator and to have concentrated solution pipeline to be communicated with the 4th generator through the 3rd solution heat exchanger, 4th generator has concentrated solution pipeline to be communicated with the second generator with the second solution heat exchanger through solution heat exchanger again, had by generator refrigerant steam channel to be communicated with condenser to be adjusted to generator have refrigerant steam channel be communicated with the 4th generator after the 4th generator have cryogen liquid pipeline again through heat exchanger, 3rd generator is communicated with evaporimeter with second throttle, 4th generator also has refrigerant steam channel to be communicated with condenser, heat exchanger also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
5. the 5th class absorption heat pump, in the 5th class absorption heat pump described in the 1st, increase by the 4th generator, second throttle, 3rd solution pump, 3rd solution heat exchanger and heat exchanger, had by absorber weak solution pipeline to be communicated with generator through solution pump and solution heat exchanger to be adjusted to absorber and to have weak solution pipeline to be communicated with the 4th generator with solution heat exchanger through solution pump, 4th generator has concentrated solution pipeline to be communicated with generator with the 3rd solution heat exchanger through the 3rd solution pump again, had by generator concentrated solution pipeline to be communicated with the second generator through solution heat exchanger and the second solution heat exchanger to be adjusted to generator and to have concentrated solution pipeline through the 3rd solution heat exchanger, solution heat exchanger is communicated with the second generator with the second solution heat exchanger, had by generator refrigerant steam channel to be communicated with condenser to be adjusted to generator have refrigerant steam channel be communicated with the 4th generator after the 4th generator have cryogen liquid pipeline again through heat exchanger, 3rd generator is communicated with evaporimeter with second throttle, 4th generator also has refrigerant steam channel to be communicated with condenser, heat exchanger also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
6. the 5th class absorption heat pump, in arbitrary 5th class absorption heat pump described in 3-5 item, cancel choke valve and second throttle, had by 3rd generator cryogen liquid pipeline to be communicated with evaporimeter through choke valve to be adjusted to the 3rd generator and to have cryogen liquid pipeline to be communicated with evaporimeter, there is by 3rd generator cryogen liquid pipeline to be communicated with evaporimeter through second throttle to be adjusted to the 3rd generator and to have cryogen liquid pipeline to be communicated with evaporimeter, form the 5th class absorption heat pump.
7. the 5th class absorption heat pump, in the 5th class absorption heat pump described in the 3rd, increase by the 5th generator, 3rd choke valve, 4th solution pump, 4th solution heat exchanger and the second heat exchanger, absorber is set up weak solution pipeline and is communicated with the 5th generator with the 4th solution heat exchanger through the 4th solution pump, 5th generator also has concentrated solution pipeline to be communicated with the second generator with the second solution heat exchanger through the 4th solution heat exchanger, had by 4th generator refrigerant steam channel to be communicated with condenser to be adjusted to the 4th generator have refrigerant steam channel be communicated with the 5th generator after the 5th generator have cryogen liquid pipeline again through the second heat exchanger, 3rd generator is communicated with evaporimeter with the 3rd choke valve, 5th generator also has refrigerant steam channel to be communicated with condenser, 4th generator there is cryogen liquid pipeline through heat exchanger, 3rd generator and second throttle are communicated with evaporimeter and are adjusted to the 4th generator and have cryogen liquid pipeline through the 5th generator, heat exchanger, 3rd generator is communicated with evaporimeter with second throttle, second heat exchanger also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
8. the 5th class absorption heat pump, in the 5th class absorption heat pump described in the 4th, increase by the 5th generator, 3rd choke valve, 4th solution heat exchanger and the second heat exchanger, absorber there is weak solution pipeline through solution pump, solution heat exchanger and the 3rd solution heat exchanger are communicated with generator and are adjusted to absorber and have weak solution pipeline through solution pump, solution heat exchanger, 4th solution heat exchanger is communicated with generator with the 3rd solution heat exchanger, had by 4th generator concentrated solution pipeline to be communicated with the second generator through solution heat exchanger and the second solution heat exchanger to be adjusted to the 4th generator and to have concentrated solution pipeline to be communicated with the 5th generator through the 4th solution heat exchanger, 5th generator has concentrated solution pipeline to be communicated with the second generator with the second solution heat exchanger through solution heat exchanger again, had by 4th generator refrigerant steam channel to be communicated with condenser to be adjusted to the 4th generator have refrigerant steam channel be communicated with the 5th generator after the 5th generator have cryogen liquid pipeline again through the second heat exchanger, 3rd generator is communicated with evaporimeter with the 3rd choke valve, 5th generator also has refrigerant steam channel to be communicated with condenser, 4th generator there is cryogen liquid pipeline through heat exchanger, 3rd generator and second throttle are communicated with evaporimeter and are adjusted to the 4th generator and have cryogen liquid pipeline through the 5th generator, heat exchanger, 3rd generator is communicated with evaporimeter with second throttle, second heat exchanger also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
9. the 5th class absorption heat pump, in the 5th class absorption heat pump described in the 5th, increase by the 5th generator, 3rd choke valve, 4th solution pump, 4th solution heat exchanger and the second heat exchanger, had by absorber weak solution pipeline to be communicated with the 4th generator through solution pump and solution heat exchanger to be adjusted to absorber and to have weak solution pipeline to be communicated with the 5th generator with solution heat exchanger through solution pump, 5th generator has concentrated solution pipeline to be communicated with the 4th generator with the 4th solution heat exchanger through the 4th solution pump again, generator there is concentrated solution pipeline through the 3rd solution heat exchanger, solution heat exchanger and the second solution heat exchanger are communicated with the second generator and are adjusted to generator and have concentrated solution pipeline through the 3rd solution heat exchanger, 4th solution heat exchanger, solution heat exchanger is communicated with the second generator with the second solution heat exchanger, had by 4th generator refrigerant steam channel to be communicated with condenser to be adjusted to the 4th generator have refrigerant steam channel be communicated with the 5th generator after the 5th generator have cryogen liquid pipeline again through the second heat exchanger, 3rd generator is communicated with evaporimeter with the 3rd choke valve, 5th generator also has refrigerant steam channel to be communicated with condenser, 4th generator there is cryogen liquid pipeline through heat exchanger, 3rd generator and second throttle are communicated with evaporimeter and are adjusted to the 4th generator and have cryogen liquid pipeline through the 5th generator, heat exchanger, 3rd generator is communicated with evaporimeter with second throttle, second heat exchanger also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
10. the 5th class absorption heat pump, in arbitrary 5th class absorption heat pump described in 7-9 item, cancel choke valve, second throttle and the 3rd choke valve, had by 3rd generator cryogen liquid pipeline to be communicated with evaporimeter through choke valve to be adjusted to the 3rd generator and to have cryogen liquid pipeline to be communicated with evaporimeter, had by 3rd generator cryogen liquid pipeline to be communicated with evaporimeter through second throttle to be adjusted to the 3rd generator and to have cryogen liquid pipeline to be communicated with evaporimeter, had by 3rd generator cryogen liquid pipeline to be communicated with evaporimeter through the 3rd choke valve to be adjusted to the 3rd generator and to have cryogen liquid pipeline to be communicated with evaporimeter, form the 5th class absorption heat pump.
11. the 5th class absorption heat pumps, formed primarily of generator, the second generator, the 3rd generator, absorber, condenser, the second condenser, evaporimeter, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, the 4th generator, the 3rd solution heat exchanger and the second absorber, absorber has weak solution pipeline to be communicated with the second absorber through the 3rd solution heat exchanger, second absorber also has weak solution pipeline to be communicated with generator with solution heat exchanger through solution pump, generator also has concentrated solution pipeline to be communicated with the second generator with the second solution heat exchanger through solution heat exchanger, second generator also has concentrated solution pipeline to be communicated with the 3rd generator, 3rd generator has concentrated solution pipeline to be communicated with the 4th generator through the second solution heat exchanger, 4th generator also has concentrated solution pipeline to be communicated with absorber with the 3rd solution heat exchanger through the second solution pump, generator also has refrigerant steam channel to be communicated with condenser, condenser have cryogen liquid pipeline be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline to be communicated with evaporimeter with choke valve through the 4th generator again, second generator and the 3rd generator also have refrigerant steam channel to be communicated with the second condenser respectively, second condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, 4th generator also has refrigerant steam channel to be communicated with the second absorber, evaporimeter also has refrigerant steam channel to be communicated with absorber, generator also has driving heat medium pipeline and ft connection, absorber and condenser also have heated medium pipeline and ft connection respectively, evaporimeter and the second generator also have 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.
12. the 5th class absorption heat pumps, in the 5th class absorption heat pump described in the 11st, cancel choke valve, had by the 4th generator cryogen liquid pipeline to be communicated with evaporimeter through choke valve and be adjusted to the 4th generator and have cryogen liquid pipeline to be communicated with evaporimeter, formation the 5th class absorption heat pump.
13. the 5th class absorption heat pumps, in the 5th class absorption heat pump described in the 11st, increase by the 5th generator, second throttle, 3rd solution pump, 4th solution heat exchanger and heat exchanger, second absorber is set up weak solution pipeline and is communicated with the 5th generator with the 4th solution heat exchanger through the 3rd solution pump, 5th generator also has concentrated solution pipeline to be communicated with the second generator with the second solution heat exchanger through the 4th solution heat exchanger, had by generator refrigerant steam channel to be communicated with condenser to be adjusted to generator have refrigerant steam channel be communicated with the 5th generator after the 5th generator have cryogen liquid pipeline again through heat exchanger, 3rd generator, 4th generator is communicated with evaporimeter with second throttle, 5th generator also has refrigerant steam channel to be communicated with condenser, heat exchanger also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
14. the 5th class absorption heat pumps, in the 5th class absorption heat pump described in the 11st, increase by the 5th generator, second throttle, 4th solution heat exchanger and heat exchanger, had by second absorber weak solution pipeline to be communicated with generator through solution pump and solution heat exchanger to be adjusted to the second absorber and to have weak solution pipeline through solution pump, solution heat exchanger is communicated with generator with the 4th solution heat exchanger, had by generator concentrated solution pipeline to be communicated with the second generator through solution heat exchanger and the second solution heat exchanger to be adjusted to generator and to have concentrated solution pipeline to be communicated with the 5th generator through the 4th solution heat exchanger, 5th generator has concentrated solution pipeline to be communicated with the second generator with the second solution heat exchanger through solution heat exchanger again, had by generator refrigerant steam channel to be communicated with condenser to be adjusted to generator have refrigerant steam channel be communicated with the 5th generator after the 5th generator have cryogen liquid pipeline again through heat exchanger, 3rd generator, 4th generator is communicated with evaporimeter with second throttle, 5th generator also has refrigerant steam channel to be communicated with condenser, heat exchanger also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
15. the 5th class absorption heat pumps, in the 5th class absorption heat pump described in the 11st, increase by the 5th generator, second throttle, 3rd solution pump, 4th solution heat exchanger and heat exchanger, had by second absorber weak solution pipeline to be communicated with generator through solution pump and solution heat exchanger to be adjusted to the second absorber and to have weak solution pipeline to be communicated with the 5th generator with solution heat exchanger through solution pump, 5th generator has concentrated solution pipeline to be communicated with generator with the 4th solution heat exchanger through the 3rd solution pump again, had by generator concentrated solution pipeline to be communicated with the second generator through solution heat exchanger and the second solution heat exchanger to be adjusted to generator and to have concentrated solution pipeline through the 4th solution heat exchanger, solution heat exchanger is communicated with the second generator with the second solution heat exchanger, had by generator refrigerant steam channel to be communicated with condenser to be adjusted to generator have refrigerant steam channel be communicated with the 5th generator after the 5th generator have cryogen liquid pipeline again through heat exchanger, 3rd generator, 4th generator is communicated with evaporimeter with second throttle, 5th generator also has refrigerant steam channel to be communicated with condenser, heat exchanger also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
16. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in 13-15 item, cancel choke valve and second throttle, had by 4th generator cryogen liquid pipeline to be communicated with evaporimeter through choke valve to be adjusted to the 4th generator and to have cryogen liquid pipeline to be communicated with evaporimeter, there is by 4th generator cryogen liquid pipeline to be communicated with evaporimeter through second throttle to be adjusted to the 4th generator and to have cryogen liquid pipeline to be communicated with evaporimeter, form the 5th class absorption heat pump.
17. the 5th class absorption heat pumps, in the 5th class absorption heat pump described in the 1st, increase by the 4th generator, 3rd solution pump, 3rd solution heat exchanger and the second absorber, had by absorber weak solution pipeline to be communicated with generator through solution pump and solution heat exchanger to be adjusted to absorber and to have weak solution pipeline to be communicated with the second absorber with the 3rd solution heat exchanger through solution pump, second absorber has weak solution pipeline to be communicated with generator with solution heat exchanger through the 3rd solution pump again, had by generator concentrated solution pipeline to be communicated with the second generator through solution heat exchanger and the second solution heat exchanger to be adjusted to generator and to have concentrated solution pipeline to be communicated with the 4th generator through solution heat exchanger, 4th generator has concentrated solution pipeline to be communicated with the second generator with the second solution heat exchanger through the 3rd solution heat exchanger again, 4th generator also has refrigerant steam channel to be communicated with the second absorber, 4th generator also has driving heat medium pipeline and ft connection, second absorber also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
18. the 5th class absorption heat pumps, in the 5th class absorption heat pump described in the 17th, cancel choke valve, had by the 3rd generator cryogen liquid pipeline to be communicated with evaporimeter through choke valve and be adjusted to the 3rd generator and have cryogen liquid pipeline to be communicated with evaporimeter, formation the 5th class absorption heat pump.
19. the 5th class absorption heat pumps, in the 5th class absorption heat pump described in the 17th, increase by the 5th generator, second throttle, 4th solution pump, 4th solution heat exchanger and heat exchanger, second absorber is set up weak solution pipeline and is communicated with the 5th generator with the 4th solution heat exchanger through the 4th solution pump, 5th generator also has concentrated solution pipeline to be communicated with the 4th generator through the 4th solution heat exchanger, had by generator refrigerant steam channel to be communicated with condenser to be adjusted to generator have refrigerant steam channel be communicated with the 5th generator after the 5th generator have cryogen liquid pipeline again through heat exchanger, 3rd generator is communicated with evaporimeter with second throttle, 5th generator also has refrigerant steam channel to be communicated with condenser, heat exchanger also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
20. the 5th class absorption heat pumps, in the 5th class absorption heat pump described in the 17th, increase by the 5th generator, second throttle, 4th solution heat exchanger and heat exchanger, had by second absorber weak solution pipeline to be communicated with generator through the 3rd solution pump and solution heat exchanger to be adjusted to the second absorber and to have weak solution pipeline through the 3rd solution pump, solution heat exchanger is communicated with generator with the 4th solution heat exchanger, had by generator concentrated solution pipeline to be communicated with the 4th generator through solution heat exchanger to be adjusted to generator and to have concentrated solution pipeline to be communicated with the 5th generator through the 4th solution heat exchanger, 5th generator has concentrated solution pipeline to be communicated with the 4th generator through solution heat exchanger again, had by generator refrigerant steam channel to be communicated with condenser to be adjusted to generator have refrigerant steam channel be communicated with the 5th generator after the 5th generator have cryogen liquid pipeline again through heat exchanger, 3rd generator is communicated with evaporimeter with second throttle, 5th generator also has refrigerant steam channel to be communicated with condenser, heat exchanger also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
21. the 5th class absorption heat pumps, in the 5th class absorption heat pump described in the 17th, increase by the 5th generator, second throttle, 4th solution pump, 4th solution heat exchanger and heat exchanger, had by second absorber weak solution pipeline to be communicated with generator through the 3rd solution pump and solution heat exchanger to be adjusted to the second absorber and to have weak solution pipeline to be communicated with the 5th generator with solution heat exchanger through the 3rd solution pump, 5th generator has concentrated solution pipeline to be communicated with generator with the 4th solution heat exchanger through the 4th solution pump again, had by generator concentrated solution pipeline to be communicated with the 4th generator through solution heat exchanger to be adjusted to generator and to have concentrated solution pipeline to be communicated with the 4th generator with solution heat exchanger through the 4th solution heat exchanger, had by generator refrigerant steam channel to be communicated with condenser to be adjusted to generator have refrigerant steam channel be communicated with the 5th generator after the 5th generator have cryogen liquid pipeline again through heat exchanger, 3rd generator is communicated with evaporimeter with second throttle, 5th generator also has refrigerant steam channel to be communicated with condenser, heat exchanger also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
22. the 5th class absorption heat pumps are in arbitrary 5th class absorption heat pump described in 19-21 item, and the 5th generator is set up and driven heat medium pipeline and ft connection, forms the 5th class absorption heat pump.
23. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in 19-22 item, cancel choke valve and second throttle, had by 3rd generator cryogen liquid pipeline to be communicated with evaporimeter through choke valve to be adjusted to the 3rd generator and to have cryogen liquid pipeline to be communicated with evaporimeter, there is by 3rd generator cryogen liquid pipeline to be communicated with evaporimeter through second throttle to be adjusted to the 3rd generator and to have cryogen liquid pipeline to be communicated with evaporimeter, form the 5th class absorption heat pump.
24. the 5th class absorption heat pumps, in the 5th class absorption heat pump described in the 17th, increase by the 5th generator, 4th solution heat exchanger and the 3rd absorber, had by absorber weak solution pipeline to be communicated with the second absorber through solution pump and the 3rd solution heat exchanger to be adjusted to absorber and to have weak solution pipeline to be communicated with the 3rd absorber through the 4th solution heat exchanger, 3rd absorber has weak solution pipeline to be communicated with the second absorber with the 3rd solution heat exchanger through solution pump again, had by 3rd generator concentrated solution pipeline to be communicated with absorber through the second solution pump and the second solution heat exchanger to be adjusted to the 3rd generator and to have concentrated solution pipeline to be communicated with the 5th generator through the second solution heat exchanger, 5th generator has concentrated solution pipeline to be communicated with absorber with the 4th solution heat exchanger through the second solution pump again, 5th generator also has refrigerant steam channel to be communicated with the 3rd absorber, condenser is had cryogen liquid pipeline be communicated with the 3rd generator after the 3rd generator have again cryogen liquid pipeline through choke valve to be communicated with evaporimeter be adjusted to condenser have cryogen liquid pipeline to be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline to be communicated with evaporimeter with choke valve through the 5th generator again, 3rd absorber also has cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
25. the 5th class absorption heat pumps, in the 5th class absorption heat pump described in the 24th, cancel choke valve, had by the 5th generator cryogen liquid pipeline to be communicated with evaporimeter through choke valve and be adjusted to the 5th generator and have cryogen liquid pipeline to be communicated with evaporimeter, formation the 5th class absorption heat pump.
26. the 5th class absorption heat pumps, formed primarily of generator, the second generator, the 3rd generator, absorber, condenser, the second condenser, evaporimeter, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, the 4th generator, the 3rd solution heat exchanger and the second absorber, absorber has weak solution pipeline to be communicated with the second absorber through the 3rd solution heat exchanger, second absorber also has weak solution pipeline to be communicated with generator with solution heat exchanger through solution pump, generator also has concentrated solution pipeline to be communicated with the second generator with the second solution heat exchanger through solution heat exchanger, second generator also has concentrated solution pipeline to be communicated with the 3rd generator, 3rd generator has concentrated solution pipeline to be communicated with the 4th generator through the second solution heat exchanger, 4th generator also has concentrated solution pipeline to be communicated with absorber with the 3rd solution heat exchanger through the second solution pump, generator also has refrigerant steam channel to be communicated with condenser, condenser have cryogen liquid pipeline be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline to be communicated with evaporimeter through choke valve again, second generator and the 3rd generator also have refrigerant steam channel to be communicated with the second condenser respectively, second condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, 4th generator also has refrigerant steam channel to be communicated with the second absorber, evaporimeter also has refrigerant steam channel to be communicated with absorber, generator also has driving heat medium pipeline and ft connection, absorber and condenser also have heated medium pipeline and ft connection respectively, evaporimeter, second generator and the 4th generator also have 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, in the 5th class absorption heat pump described in the 26th, cancel choke valve, had by the 3rd generator cryogen liquid pipeline to be communicated with evaporimeter through choke valve and be adjusted to the 3rd generator and have cryogen liquid pipeline to be communicated with evaporimeter, formation the 5th class absorption heat pump.
28. the 5th class absorption heat pumps, in the 5th class absorption heat pump described in the 11st, increase by the 5th generator, second throttle, 3rd solution pump, 4th solution heat exchanger and heat exchanger, second absorber is set up weak solution pipeline and is communicated with the 5th generator with the 4th solution heat exchanger through the 3rd solution pump, 5th generator also has concentrated solution pipeline to be communicated with the second generator with the second solution heat exchanger through the 4th solution heat exchanger, had by generator refrigerant steam channel to be communicated with condenser to be adjusted to generator have refrigerant steam channel be communicated with the 5th generator after the 5th generator have cryogen liquid pipeline again through heat exchanger, 3rd generator is communicated with evaporimeter with second throttle, 5th generator also has refrigerant steam channel to be communicated with condenser, heat exchanger also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
29. the 5th class absorption heat pumps, in the 5th class absorption heat pump described in the 11st, increase by the 5th generator, second throttle, 4th solution heat exchanger and heat exchanger, had by second absorber weak solution pipeline to be communicated with generator through solution pump and solution heat exchanger to be adjusted to the second absorber and to have weak solution pipeline through solution pump, solution heat exchanger is communicated with generator with the 4th solution heat exchanger, had by generator concentrated solution pipeline to be communicated with the second generator through solution heat exchanger and the second solution heat exchanger to be adjusted to generator and to have concentrated solution pipeline to be communicated with the 5th generator through the 4th solution heat exchanger, 5th generator has concentrated solution pipeline to be communicated with the second generator with the second solution heat exchanger through solution heat exchanger again, had by generator refrigerant steam channel to be communicated with condenser to be adjusted to generator have refrigerant steam channel be communicated with the 5th generator after the 5th generator have cryogen liquid pipeline again through heat exchanger, 3rd generator is communicated with evaporimeter with second throttle, 5th generator also has refrigerant steam channel to be communicated with condenser, heat exchanger also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
30. the 5th class absorption heat pumps, in the 5th class absorption heat pump described in the 11st, increase by the 5th generator, second throttle, 3rd solution pump, 4th solution heat exchanger and heat exchanger, had by second absorber weak solution pipeline to be communicated with generator through solution pump and solution heat exchanger to be adjusted to the second absorber and to have weak solution pipeline to be communicated with the 5th generator with solution heat exchanger through solution pump, 5th generator has concentrated solution pipeline to be communicated with generator with the 4th solution heat exchanger through the 3rd solution pump again, had by generator concentrated solution pipeline to be communicated with the second generator through solution heat exchanger and the second solution heat exchanger to be adjusted to generator and to have concentrated solution pipeline through the 4th solution heat exchanger, solution heat exchanger is communicated with the second generator with the second solution heat exchanger, had by generator refrigerant steam channel to be communicated with condenser to be adjusted to generator have refrigerant steam channel be communicated with the 5th generator after the 5th generator have cryogen liquid pipeline again through heat exchanger, 3rd generator is communicated with evaporimeter with second throttle, 5th generator also has refrigerant steam channel to be communicated with condenser, heat exchanger also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
31. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in 28-30 item, cancel choke valve and second throttle, had by 3rd generator cryogen liquid pipeline to be communicated with evaporimeter through choke valve to be adjusted to the 3rd generator and to have cryogen liquid pipeline to be communicated with evaporimeter, there is by 3rd generator cryogen liquid pipeline to be communicated with evaporimeter through second throttle to be adjusted to the 3rd generator and to have cryogen liquid pipeline to be communicated with evaporimeter, form the 5th class absorption heat pump.
32. the 5th class absorption heat pumps, in the 5th class absorption heat pump described in the 17th, increase by the 5th generator, 4th solution heat exchanger and the 3rd absorber, had by absorber weak solution pipeline to be communicated with the second absorber through solution pump and the 3rd solution heat exchanger to be adjusted to absorber and to have weak solution pipeline to be communicated with the 3rd absorber through the 4th solution heat exchanger, 3rd absorber has weak solution pipeline to be communicated with the second absorber with the 3rd solution heat exchanger through solution pump again, had by 3rd generator concentrated solution pipeline to be communicated with absorber through the second solution pump and the second solution heat exchanger to be adjusted to the 3rd generator and to have concentrated solution pipeline to be communicated with the 5th generator through the second solution heat exchanger, 5th generator has concentrated solution pipeline to be communicated with absorber with the 4th solution heat exchanger through the second solution pump again, 5th generator also has refrigerant steam channel to be communicated with the 3rd absorber, 5th generator also has surplus heat medium pipeline and ft connection, 3rd absorber also has cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
33. the 5th class absorption heat pumps, in the 5th class absorption heat pump described in the 32nd, cancel choke valve, had by the 3rd generator cryogen liquid pipeline to be communicated with evaporimeter through choke valve and be adjusted to the 3rd generator and have cryogen liquid pipeline to be communicated with evaporimeter, formation the 5th class absorption heat pump.
34. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in 1-33 item, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by evaporimeter refrigerant steam channel to be communicated with absorber to be adjusted to evaporimeter has refrigerant steam channel to be communicated with newly-increased absorber, newly-increased absorber also has weak solution pipeline to be communicated with newly-increased generator with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased generator also has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased generator also has refrigerant steam channel to be communicated with absorber, newly-increased generator also has driving heat medium pipeline and ft connection, newly-increased absorber also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
35. the 5th class absorption heat pumps, at 1-2, 11-12, 17-18, 24-27, in arbitrary 5th class absorption heat pump described in 32-33 item, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by generator refrigerant steam channel to be communicated with condenser to be adjusted to generator has refrigerant steam channel to be communicated with newly-increased absorber, newly-increased absorber also has weak solution pipeline to be communicated with newly-increased generator with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased generator also has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased generator also has refrigerant steam channel to be communicated with condenser, newly-increased generator also has driving heat medium pipeline and ft connection, newly-increased absorber also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
36. the 5th class absorption heat pumps are that the 3rd generator sets up waste heat medium pipeline and ft connection in arbitrary 5th class absorption heat pump described in 1-10,17-23,26-33 item, form the 5th class absorption heat pump.
37. the 5th class absorption heat pumps, be in arbitrary 5th class absorption heat pump described in 11-16 item, the 3rd generator 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, be in arbitrary 5th class absorption heat pump described in 11-16 item, the 3rd generator 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, be in arbitrary 5th class absorption heat pump described in 24-25 item, the 3rd generator 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, be in arbitrary 5th class absorption heat pump described in 24-25 item, the 3rd generator 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, in arbitrary 5th class absorption heat pump described in 36-40 item, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by evaporimeter refrigerant steam channel to be communicated with absorber to be adjusted to evaporimeter has refrigerant steam channel to be communicated with newly-increased absorber, newly-increased absorber also has weak solution pipeline to be communicated with newly-increased generator with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased generator also has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased generator also has refrigerant steam channel to be communicated with absorber, newly-increased generator also has driving heat medium pipeline and ft connection, newly-increased absorber also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
42. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in 1-33 item, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by 3rd generator refrigerant steam channel to be communicated with the second condenser to be adjusted to the 3rd generator has refrigerant steam channel to be communicated with newly-increased absorber, newly-increased absorber also has weak solution pipeline to be communicated with newly-increased generator with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased generator also has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased generator also has refrigerant steam channel to be communicated with the second condenser, newly-increased generator also has surplus heat medium pipeline and ft connection, 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, at 1-10, in arbitrary 5th class absorption heat pump described in 17-23 item, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by second generator refrigerant steam channel to be communicated with the second condenser to be adjusted to the second generator has refrigerant steam channel to be communicated with newly-increased absorber, newly-increased absorber also has weak solution pipeline to be communicated with newly-increased generator with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased generator also has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased generator also has refrigerant steam channel to be communicated with the second condenser, newly-increased generator also has surplus heat medium pipeline and ft connection, newly-increased absorber also has cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
44. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in the 43rd, being had by 3rd generator refrigerant steam channel to be communicated with the second condenser to be adjusted to the 3rd generator has refrigerant steam channel to be communicated with newly-increased absorber, forms the 5th class absorption heat pump.
45. the 5th class absorption heat pumps are that the 3rd generator sets up waste heat medium pipeline and ft connection in arbitrary 5th class absorption heat pump described in 42-44 item, form the 5th class absorption heat pump.
46. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in 11-16 item, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by 4th generator refrigerant steam channel to be communicated with the second absorber to be adjusted to the 4th generator has refrigerant steam channel to be communicated with newly-increased absorber, newly-increased absorber also has weak solution pipeline to be communicated with newly-increased generator with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased generator also has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased generator also has refrigerant steam channel to be communicated with the second absorber, newly-increased generator also has surplus heat medium pipeline and ft connection, 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 that the 3rd generator and the 4th generator set up waste heat medium pipeline and ft connection respectively in arbitrary 5th class absorption heat pump described in the 46th, form the 5th class absorption heat pump.
48. the 5th class absorption heat pumps are that the 3rd generator or the 4th generator set up waste heat medium pipeline and ft connection in arbitrary 5th class absorption heat pump described in the 46th, form the 5th class absorption heat pump.
49. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in 24-25 item, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by 5th generator refrigerant steam channel to be communicated with the 3rd absorber to be adjusted to the 5th generator has refrigerant steam channel to be communicated with newly-increased absorber, newly-increased absorber also has weak solution pipeline to be communicated with newly-increased generator with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased generator also has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased generator also has refrigerant steam channel to be communicated with the 3rd absorber, newly-increased generator also has surplus heat medium pipeline and ft connection, 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 that the 3rd generator and the 5th generator set up waste heat medium pipeline and ft connection respectively in arbitrary 5th class absorption heat pump described in the 49th, form the 5th class absorption heat pump.
51. the 5th class absorption heat pumps are that the 3rd generator or the 5th generator set up waste heat medium pipeline and ft connection in arbitrary 5th class absorption heat pump described in the 49th, form the 5th class absorption heat pump.
52. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in 26-31 item, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by 4th generator refrigerant steam channel to be communicated with the second absorber to be adjusted to the 4th generator has refrigerant steam channel to be communicated with newly-increased absorber, newly-increased absorber also has weak solution pipeline to be communicated with newly-increased generator with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased generator also has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased generator also has refrigerant steam channel to be communicated with the second absorber, newly-increased generator also has surplus heat medium pipeline and ft connection, 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, in arbitrary 5th class absorption heat pump described in 32-33 item, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by 5th generator refrigerant steam channel to be communicated with the 3rd absorber to be adjusted to the 5th generator has refrigerant steam channel to be communicated with newly-increased absorber, newly-increased absorber also has weak solution pipeline to be communicated with newly-increased generator with newly-increased solution heat exchanger through newly-increased solution pump, newly-increased generator also has concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased generator also has refrigerant steam channel to be communicated with the 3rd absorber, newly-increased generator also has surplus heat medium pipeline and ft connection, 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 that the 3rd generator sets up waste heat medium pipeline and ft connection in arbitrary 5th class absorption heat pump described in 52-53 item, form the 5th class absorption heat pump.
55. the 5th class absorption heat pumps, at 1-2, 17-18, 26-27, in arbitrary 5th class absorption heat pump described in 32-33 item, had surplus heat by second generator medium pipeline and ft connection is adjusted to the 3rd generator and has surplus heat medium pipeline and ft connection, condenser is had cryogen liquid pipeline be communicated with the 3rd generator after the 3rd generator have again cryogen liquid pipeline through choke valve to be communicated with evaporimeter be adjusted to condenser have cryogen liquid pipeline to be communicated with the second generator after the second generator have cryogen liquid pipeline to be communicated with evaporimeter through choke valve again, form the 5th class absorption heat pump.
56. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in 1-41 item, increase newly-increased condenser, newly-increased choke valve and new solubilization liquid choke valve, being had by second generator concentrated solution pipeline to be communicated with the 3rd generator to be adjusted to the second generator has concentrated solution pipeline to be communicated with the 3rd generator through new solubilization liquid choke valve, being had by second generator refrigerant steam channel to be communicated with the second condenser to be adjusted to the second generator has refrigerant steam channel to be communicated with newly-increased condenser, newly-increased condenser also has cryogen liquid pipeline to be communicated with the second condenser or evaporimeter through newly-increased choke valve, 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, in arbitrary 5th class absorption heat pump described in 1-41 item, increase newly-increased condenser, newly-increased cryogen liquid pump and new solubilization liquid choke valve, being had by second generator concentrated solution pipeline to be communicated with the 3rd generator to be adjusted to the second generator has concentrated solution pipeline to be communicated with the 3rd generator through new solubilization liquid choke valve, being had by second generator refrigerant steam channel to be communicated with the second condenser to be adjusted to the second generator has refrigerant steam channel to be communicated with newly-increased condenser, newly-increased condenser also has cryogen liquid pipeline to be communicated with evaporimeter through newly-increased cryogen liquid pump, newly-increased condenser also has cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
Essence of the present invention is further illustrated below in conjunction with 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, following effect will be brought:
1. decrease the thermic load be brought into by high temperature cryogen liquid in evaporimeter 7, decrease the negative effect to UTILIZATION OF VESIDUAL HEAT IN.
2. the 3rd generator 3 utilizes the thermic load of cryogen liquid to realize the raising of solution concentration, then relatively reduce the high-temperature hot load needed for generator 1, can improve the performance index of source pump comparatively significantly.
3. when environment (cooling medium) medium temperature is lower, effectively can utilize the temperature difference between cryogen liquid and cooling medium, improve the utilization rate driving thermic load and waste heat load.
(2) thermic load in high temperature driven thermal medium is discharged in refrigerant vapour by generator 1, a part is transferred in heated medium by condenser 5, another part by the 3rd generator 3 and the second condenser 6 heat release, is belonged to and utilizes new technology with high-temperature hot load substep temperature drop for driving the temperature difference of the temperature difference in cooling medium.
Accompanying drawing illustrates:
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-generator, 2-second generator, 3-the 3rd generator, 4-absorber, 5-condenser, 6-second condenser, 7-evaporimeter, 8-choke valve, 9-cryogen liquid pump, 10-solution pump, 11-second solution pump, 12-solution heat exchanger, 13-second solution heat exchanger, 14-the 4th generator, 15-second throttle, 16-the 3rd solution pump, 17-the 3rd solution heat exchanger, 18-heat exchanger, 19-the 5th generator, 20-the 3rd choke valve, 21-the 4th solution pump, 22-the 4th solution heat exchanger, 23-second heat exchanger, 24-second absorber, 25-the 3rd absorber, A-increases generator newly, and B-increases absorber newly, and C-increases solution pump newly, and D-increases solution heat exchanger newly, and E-increases condenser newly, and F-increases choke valve newly, the new solubilization liquid choke valve of G-.
Here it is noted that for the 5th class absorption heat pump shown in accompanying drawing 1, the choke valve 8 arranged in cryogen liquid pipeline, available gravitational pressure drop substitutes; When coolant temperature is lower, when the cryogen liquid temp flowing through the 3rd generator 3 is cooled to the evaporating temperature of evaporimeter 7 inside, choke valve 8 can not be set, and pressure reduction be used in the 3rd generator 3 inner heat exchanger pipeline.
Detailed description of the invention:
First be noted that in the statement of structure and flow process, do not repeat in inessential situation; Apparent flow process is not stated.The present invention is described in detail below in conjunction with accompanying drawing and example.
The 5th class absorption heat pump shown in Fig. 1 is achieved in that
(1), in structure, it formed primarily of generator, the second generator, the 3rd generator, absorber, condenser, the second condenser, evaporimeter, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, absorber 4 has weak solution pipeline to be communicated with generator 1 with solution heat exchanger 12 through solution pump 10, generator 1 also has concentrated solution pipeline to be communicated with the second generator 2 with the second solution heat exchanger 13 through solution heat exchanger 12, second generator 2 also has concentrated solution pipeline to be communicated with the 3rd generator 3, 3rd generator 3 also has concentrated solution pipeline to be communicated with absorber 4 with the second solution heat exchanger 13 through the second solution pump 11, generator 1 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 also have cryogen liquid pipeline be communicated with the 3rd generator 3 after the 3rd generator 3 have cryogen liquid pipeline to be communicated with evaporimeter 7 through choke valve 8 again, second generator 2 and the 3rd generator 3 also have refrigerant steam channel to be communicated with the second condenser 6 respectively, second condenser 6 also has cryogen liquid pipeline to be communicated with evaporimeter 7 through cryogen liquid pump 9, evaporimeter 7 also has refrigerant steam channel to be communicated with absorber 4, 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, evaporimeter 7 and the second generator 2 also have surplus heat medium pipeline and ft connection respectively, second condenser 6 also has cooling medium pipeline and ft connection.
(2) in flow process, the weak solution of absorber 4 enters generator 1 through solution pump 10 and solution heat exchanger 12, drive heat medium flow through generator 1, heating enters the solution release refrigerant vapour in it and provides to condenser 5, the concentrated solution of generator 1 enters the second generator 2 through solution heat exchanger 12 and the second solution heat exchanger 13, waste heat medium flows through the second generator 2, heating enters the solution release refrigerant vapour in it and provides to the second condenser 6, the concentrated solution of the second generator 2 enters the 3rd generator 3, heat absorption release refrigerant vapour also provides to the second condenser 6, the concentrated solution of the 3rd generator 3 enters absorber 4 through the second solution pump 11 and the second solution heat exchanger 13, absorb refrigerant vapour heat release in heated medium, the refrigerant vapour heat release of condenser 5 becomes cryogen liquid in heated medium, the cryogen liquid of condenser 5 flows through after the 3rd generator 3 heat release is lowered the temperature and enters evaporimeter 7 through choke valve 8 throttling again, the refrigerant vapour heat release of the second condenser 6 becomes cryogen liquid in cooling medium, and the cryogen liquid of the second condenser 6 enters evaporimeter 7 through cryogen liquid pump 9 pressurization, the cryogen liquid of evaporimeter 7 absorbs waste heat and becomes refrigerant vapour, and the refrigerant vapour that evaporimeter 7 produces is supplied to absorber 4, forms the 5th class absorption heat pump.
The 5th class absorption heat pump shown in Fig. 2 is achieved in that
(1) in structure, in the 5th class absorption heat pump shown in Fig. 1, increase by the 4th generator, second throttle, 3rd solution pump, 3rd solution heat exchanger and heat exchanger, absorber 4 is set up weak solution pipeline and is communicated with the 4th generator 14 with the 3rd solution heat exchanger 17 through the 3rd solution pump 16, 4th generator 14 also has concentrated solution pipeline to be communicated with the second generator 2 with the second solution heat exchanger 13 through the 3rd solution heat exchanger 17, had by generator 1 refrigerant steam channel to be communicated with condenser 5 to be adjusted to generator 1 have refrigerant steam channel be communicated with the 4th generator 14 after the 4th generator 14 have cryogen liquid pipeline again through heat exchanger 18, 3rd generator 3 is communicated with evaporimeter 7 with second throttle 15, 4th generator 14 also has refrigerant steam channel to be communicated with condenser 5, heat exchanger 18 also has heated medium pipeline and ft connection.
(2) in flow process, the refrigerant vapour that generator 1 produces is supplied to the 4th generator 14 and does to drive thermal medium, the part weak solution of absorber 4 enters the 4th generator 14 through the 3rd solution pump 16 and the 3rd solution heat exchanger 17, refrigerant vapour flows through the 4th generator 14, heating enters the solution release refrigerant vapour in it and provides to condenser 5, and the concentrated solution of the 4th generator 14 enters the second generator 2 through the 3rd solution heat exchanger 17 and the second solution heat exchanger 13; The refrigerant vapour heat release flowing through the 4th generator 14 flows through heat exchanger 18 and the 3rd generator 3 and progressively heat release cooling again after becoming cryogen liquid, the cryogen liquid after cooling enters evaporimeter 7 through second throttle 15 throttling, forms the 5th class absorption heat pump.
The 5th class absorption heat pump shown in Fig. 3 is achieved in that
(1) in structure, in the 5th class absorption heat pump shown in Fig. 1, increase by the 4th generator, second throttle, 3rd solution heat exchanger and heat exchanger, had by absorber 4 weak solution pipeline to be communicated with generator 1 through solution pump 10 and solution heat exchanger 12 to be adjusted to absorber 4 and to have weak solution pipeline through solution pump 10, solution heat exchanger 12 is communicated with generator 1 with the 3rd solution heat exchanger 17, had by generator 1 concentrated solution pipeline to be communicated with the second generator 2 through solution heat exchanger 12 and the second solution heat exchanger 13 to be adjusted to generator 1 and to have concentrated solution pipeline to be communicated with the 4th generator 14 through the 3rd solution heat exchanger 17, 4th generator 14 has concentrated solution pipeline to be communicated with the second generator 2 with the second solution heat exchanger 13 through solution heat exchanger 12 again, had by generator 1 refrigerant steam channel to be communicated with condenser 5 to be adjusted to generator 1 have refrigerant steam channel be communicated with the 4th generator 14 after the 4th generator 14 have cryogen liquid pipeline again through heat exchanger 18, 3rd generator 3 is communicated with evaporimeter 7 with second throttle 15, 4th generator 14 also has refrigerant steam channel to be communicated with condenser 5, heat exchanger 18 also has heated medium pipeline and ft connection.
(2) in flow process, the refrigerant vapour that generator 1 produces is supplied to the 4th generator 14 and does to drive thermal medium, the weak solution of absorber 4 enters generator 1 through solution pump 10, solution heat exchanger 12 and the 3rd solution heat exchanger 17, the concentrated solution of generator 1 enters the 4th generator 14 through the 3rd solution heat exchanger 17, refrigerant vapour flows through the 4th generator 14, heating enters the solution release refrigerant vapour in it and provides to condenser 5, and the concentrated solution of the 4th generator 14 enters the second generator 2 through solution heat exchanger 12 and the second solution heat exchanger 13; The refrigerant vapour heat release flowing through the 4th generator 14 flows through heat exchanger 18 and the 3rd generator 3 and progressively heat release cooling again after becoming cryogen liquid, the cryogen liquid after cooling enters evaporimeter 7 through second throttle 15 throttling, forms the 5th class absorption heat pump.
The 5th class absorption heat pump shown in Fig. 4 is achieved in that
(1) in structure, in the 5th class absorption heat pump shown in Fig. 1, increase by the 4th generator, second throttle, 3rd solution pump, 3rd solution heat exchanger and heat exchanger, had by absorber 4 weak solution pipeline to be communicated with generator 1 through solution pump 10 and solution heat exchanger 12 to be adjusted to absorber 4 and to have weak solution pipeline to be communicated with the 4th generator 14 with solution heat exchanger 12 through solution pump 10, 4th generator 14 has concentrated solution pipeline to be communicated with generator 1 with the 3rd solution heat exchanger 17 through the 3rd solution pump 16 again, had by generator 1 concentrated solution pipeline to be communicated with the second generator 2 through solution heat exchanger 12 and the second solution heat exchanger 13 to be adjusted to generator 1 and to have concentrated solution pipeline through the 3rd solution heat exchanger 17, solution heat exchanger 12 is communicated with the second generator 2 with the second solution heat exchanger 13, had by generator 1 refrigerant steam channel to be communicated with condenser 5 to be adjusted to generator 1 have refrigerant steam channel be communicated with the 4th generator 14 after the 4th generator 14 have cryogen liquid pipeline again through heat exchanger 18, 3rd generator 3 is communicated with evaporimeter 7 with second throttle 15, 4th generator 14 also has refrigerant steam channel to be communicated with condenser 5, heat exchanger 18 also has heated medium pipeline and ft connection.
(2) in flow process, the refrigerant vapour that generator 1 produces is supplied to the 4th generator 14 and does to drive thermal medium, the weak solution of absorber 4 enters the 4th generator 14 through solution pump 10 and solution heat exchanger 12, refrigerant vapour flows through the 4th generator 14, heating enters the solution release refrigerant vapour in it and provides to condenser 5, the concentrated solution of the 4th generator 14 enters generator 1 through the 3rd solution pump 16 and the 3rd solution heat exchanger 17, the concentrated solution of generator 1 is through the 3rd solution heat exchanger 17, solution heat exchanger 12 and the second solution heat exchanger 13 enter the second generator 2, the refrigerant vapour heat release flowing through the 4th generator 14 flows through heat exchanger 18 and the 3rd generator 3 and progressively heat release cooling again after becoming cryogen liquid, the cryogen liquid after cooling enters evaporimeter 7 through second throttle 15 throttling, forms the 5th class absorption heat pump.
The 5th class absorption heat pump shown in Fig. 5 is achieved in that
(1) in structure, in the 5th class absorption heat pump shown in Fig. 2, increase by the 5th generator, 3rd choke valve, 4th solution pump, 4th solution heat exchanger and the second heat exchanger, absorber 4 is set up weak solution pipeline and is communicated with the 5th generator 19 with the 4th solution heat exchanger 22 through the 4th solution pump 21, 5th generator 19 also has concentrated solution pipeline to be communicated with the second generator 2 with the second solution heat exchanger 13 through the 4th solution heat exchanger 22, had by 4th generator 14 refrigerant steam channel to be communicated with condenser 5 to be adjusted to the 4th generator 14 have refrigerant steam channel be communicated with the 5th generator 19 after the 5th generator 19 have cryogen liquid pipeline again through the second heat exchanger 23, 3rd generator 3 is communicated with evaporimeter 7 with the 3rd choke valve 20, 5th generator 19 also has refrigerant steam channel to be communicated with condenser 5, 4th generator 14 there is cryogen liquid pipeline through heat exchanger 18, 3rd generator 3 and second throttle 15 are communicated with evaporimeter 7 and are adjusted to the 4th generator 14 and have cryogen liquid pipeline through the 5th generator 19, heat exchanger 18, 3rd generator 3 is communicated with evaporimeter 7 with second throttle 15, second heat exchanger 23 also has heated medium pipeline and ft connection.
(2) in flow process, the refrigerant vapour that 4th generator 14 produces and cryogen liquid are supplied to the 5th generator 19 and do 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 enters the solution release refrigerant vapour in it and provides to condenser 5, and the concentrated solution of the 5th generator 19 enters the second generator 2 through the 4th solution heat exchanger 22 and the second solution heat exchanger 13; The refrigerant vapour heat release flowing through the 5th generator 19 is again through the second heat exchanger 23 and the 3rd generator 3 and progressively heat release cooling after becoming cryogen liquid, and the cryogen liquid after cooling enters evaporimeter 7 through the 3rd choke valve 20 throttling; After heat exchanger 18, the 3rd generator 3 and second throttle 15, enter evaporimeter 7 again after flowing through the cryogen liquid heat release cooling of the 5th generator 19, form the 5th class absorption heat pump.
The 5th class absorption heat pump shown in Fig. 6 is achieved in that
(1) in structure, in the 5th class absorption heat pump shown in Fig. 3, increase by the 5th generator, 3rd choke valve, 4th solution heat exchanger and the second heat exchanger, absorber 4 there is weak solution pipeline through solution pump 10, solution heat exchanger 12 and the 3rd solution heat exchanger 17 are communicated with generator 1 and are adjusted to absorber 4 and have weak solution pipeline through solution pump 10, solution heat exchanger 12, 4th solution heat exchanger 22 is communicated with generator 1 with the 3rd solution heat exchanger 17, had by 4th generator 14 concentrated solution pipeline to be communicated with the second generator 2 through solution heat exchanger 12 and the second solution heat exchanger 13 to be adjusted to the 4th generator 14 and to have concentrated solution pipeline to be communicated with the 5th generator 19 through the 4th solution heat exchanger 22, 5th generator 19 has concentrated solution pipeline to be communicated with the second generator 2 with the second solution heat exchanger 13 through solution heat exchanger 12 again, had by 4th generator 14 refrigerant steam channel to be communicated with condenser 5 to be adjusted to the 4th generator 14 have refrigerant steam channel be communicated with the 5th generator 19 after the 5th generator 19 have cryogen liquid pipeline again through the second heat exchanger 23, 3rd generator 3 is communicated with evaporimeter 7 with the 3rd choke valve 20, 5th generator 19 also has refrigerant steam channel to be communicated with condenser 5, 4th generator 14 there is cryogen liquid pipeline through heat exchanger 18, 3rd generator 3 and second throttle 15 are communicated with evaporimeter 7 and are adjusted to the 4th generator 14 and have cryogen liquid pipeline through the 5th generator 19, heat exchanger 18, 3rd generator 3 is communicated with evaporimeter 7 with second throttle 15, second heat exchanger 23 also has heated medium pipeline and ft connection.
(2) in flow process, the refrigerant vapour that 4th generator 14 produces and cryogen liquid are supplied to the 5th generator 19 and do to drive thermal medium, the weak solution of absorber 4 is through solution pump 10, solution heat exchanger 12, 4th solution heat exchanger 22 and the 3rd solution heat exchanger 17 enter generator 1, the concentrated solution of generator 1 enters the 4th generator 14 through the 3rd solution heat exchanger 17, the concentrated solution of the 4th generator 14 enters the 5th generator 19 through the 4th solution heat exchanger 22, refrigerant vapour and cryogen liquid flow through the 5th generator 19, heating enters the solution release refrigerant vapour in it and provides to condenser 5, the concentrated solution of the 5th generator 19 enters the second generator 2 through solution heat exchanger 12 and the second solution heat exchanger 13, the refrigerant vapour heat release flowing through the 5th generator 19 is again through the second heat exchanger 23 and the 3rd generator 3 and progressively heat release cooling after becoming cryogen liquid, and the cryogen liquid after cooling enters evaporimeter 7 through the 3rd choke valve 20 throttling, after heat exchanger 18, the 3rd generator 3 and second throttle 15, enter evaporimeter 7 again after flowing through the cryogen liquid heat release cooling of the 5th generator 19, form the 5th class absorption heat pump.
The 5th class absorption heat pump shown in Fig. 7 is achieved in that
(1) in structure, in the 5th class absorption heat pump shown in Fig. 4, increase by the 5th generator, 3rd choke valve, 4th solution pump, 4th solution heat exchanger and the second heat exchanger, had by absorber 4 weak solution pipeline to be communicated with the 4th generator 14 through solution pump 10 and solution heat exchanger 12 to be adjusted to absorber 4 and to have weak solution pipeline to be communicated with the 5th generator 19 with solution heat exchanger 12 through solution pump 10, 5th generator 19 has concentrated solution pipeline to be communicated with the 4th generator 14 with the 4th solution heat exchanger 22 through the 4th solution pump 21 again, generator 1 there is concentrated solution pipeline through the 3rd solution heat exchanger 17, solution heat exchanger 12 and the second solution heat exchanger 13 are communicated with the second generator 2 and are adjusted to generator 1 and have concentrated solution pipeline through the 3rd solution heat exchanger 17, 4th solution heat exchanger 22, solution heat exchanger 12 is communicated with the second generator 2 with the second solution heat exchanger 13, had by 4th generator 14 refrigerant steam channel to be communicated with condenser 5 to be adjusted to the 4th generator 14 have refrigerant steam channel be communicated with the 5th generator 19 after the 5th generator 19 have cryogen liquid pipeline again through the second heat exchanger 23, 3rd generator 3 is communicated with evaporimeter 7 with the 3rd choke valve 20, 5th generator 19 also has refrigerant steam channel to be communicated with condenser 5, 4th generator 14 there is cryogen liquid pipeline through heat exchanger 18, 3rd generator 3 and second throttle 15 are communicated with evaporimeter 7 and are adjusted to the 4th generator 14 and have cryogen liquid pipeline through the 5th generator 19, heat exchanger 18, 3rd generator 3 is communicated with evaporimeter 7 with second throttle 15, second heat exchanger 23 also has heated medium pipeline and ft connection.
(2) in flow process, the refrigerant vapour that 4th generator 14 produces and cryogen liquid are supplied to the 5th generator 19 and do 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 cryogen liquid flow through the 5th generator 19, heating enters the solution release refrigerant vapour in it and provides to condenser 5, the concentrated solution of the 5th generator 19 enters the 4th generator 14 through the 4th solution pump 21 and the 4th solution heat exchanger 22, the concentrated solution of the 4th generator 14 enters generator 1 through the 3rd solution pump 16 and the 3rd solution heat exchanger 17, the concentrated solution of generator 1 is through the 3rd solution heat exchanger 17, 4th solution heat exchanger 22, solution heat exchanger 12 and the second solution heat exchanger 13 enter the second generator 2, the refrigerant vapour heat release flowing through the 5th generator 19 is again through the second heat exchanger 23 and the 3rd generator 3 and progressively heat release cooling after becoming cryogen liquid, and the cryogen liquid after cooling enters evaporimeter 7 through the 3rd choke valve 20 throttling, after heat exchanger 18, the 3rd generator 3 and second throttle 15, enter evaporimeter 7 again after flowing through the cryogen liquid heat release cooling of the 5th generator 19, form the 5th class absorption heat pump.
The 5th class absorption heat pump shown in Fig. 8 is achieved in that
(1), in structure, it formed primarily of generator, the second generator, the 3rd generator, absorber, condenser, the second condenser, evaporimeter, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, the 4th generator, the 3rd solution heat exchanger and the second absorber, absorber 4 has weak solution pipeline to be communicated with the second absorber 24 through the 3rd solution heat exchanger 17, second absorber 24 also has weak solution pipeline to be communicated with generator 1 with solution heat exchanger 12 through solution pump 10, generator 1 also has concentrated solution pipeline to be communicated with the second generator 2 with the second solution heat exchanger 13 through solution heat exchanger 12, second generator 2 also has concentrated solution pipeline to be communicated with the 3rd generator 3, 3rd generator 3 has concentrated solution pipeline to be communicated with the 4th generator 14 through the second solution heat exchanger 13, 4th generator 14 also has concentrated solution pipeline to be communicated with absorber 4 with the 3rd solution heat exchanger 17 through the second solution pump 11, generator 1 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 have cryogen liquid pipeline be communicated with the 3rd generator 3 after the 3rd generator 3 have cryogen liquid pipeline to be communicated with evaporimeter 7 with choke valve 8 through the 4th generator 14 again, second generator 2 and the 3rd generator 3 also have refrigerant steam channel to be communicated with the second condenser 6 respectively, second condenser 6 also has cryogen liquid pipeline to be communicated with evaporimeter 7 through cryogen liquid pump 9, 4th generator 14 also has refrigerant steam channel to be communicated with the second absorber 24, evaporimeter 7 also has refrigerant steam channel to be communicated with absorber 4, 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, evaporimeter 7 and the second generator 2 also have surplus heat medium pipeline and ft connection respectively, second condenser 6 and the second absorber 24 also have cooling medium pipeline and ft connection respectively, 4th generator 14 also has surplus heat medium pipeline and ft connection.
(2) in flow process, the weak solution of absorber 4 enters the second absorber 24 through the 3rd solution heat exchanger 17, absorb refrigerant vapour heat release in cooling medium, the weak solution of the second absorber 24 enters generator 1 through solution pump 10 and solution heat exchanger 12, drive heat medium flow through generator 1, heating enters the solution release refrigerant vapour in it and provides to condenser 5, the concentrated solution of generator 1 enters the second generator 2 through solution heat exchanger 12 and the second solution heat exchanger 13, waste heat medium flows through the second generator 2, heating enters the solution release refrigerant vapour in it and provides to the second condenser 6, the concentrated solution of the second generator 2 enters the 3rd generator 3, heat absorption release refrigerant vapour also provides to the second condenser 6, the concentrated solution of the 3rd generator 3 enters the 4th generator 14 through the second solution heat exchanger 13, cryogen liquid and waste heat medium flow through the 4th generator 14, heating enters the solution release refrigerant vapour in it and provides to the second absorber 24, the concentrated solution of the 4th generator 14 enters absorber 4 through the second solution pump 11 and the 3rd solution heat exchanger 17, absorb refrigerant vapour heat release in heated medium, the refrigerant vapour heat release of condenser 5 becomes cryogen liquid in heated medium, the cryogen liquid of condenser 5 flows through the 3rd generator 3 and the 4th generator 14 successively and progressively enters evaporimeter 7 through choke valve 8 throttling again after heat release cooling, the refrigerant vapour heat release of the second condenser 6 becomes cryogen liquid in cooling medium, and the cryogen liquid of the second condenser 6 enters evaporimeter 7 through cryogen liquid pump 9 pressurization, the cryogen liquid of evaporimeter 7 absorbs waste heat and becomes refrigerant vapour, and the refrigerant vapour that evaporimeter 7 produces is supplied to absorber 4, forms the 5th class absorption heat pump.
The 5th class absorption heat pump shown in Fig. 9 is achieved in that
(1) in structure, in the 5th class absorption heat pump shown in Fig. 8, increase by the 5th generator, second throttle, 3rd solution pump, 4th solution heat exchanger and heat exchanger, second absorber 24 is set up weak solution pipeline and is communicated with the 5th generator 19 with the 4th solution heat exchanger 22 through the 3rd solution pump 16, 5th generator 19 also has concentrated solution pipeline to be communicated with the second generator 2 with the second solution heat exchanger 13 through the 4th solution heat exchanger 22, had by generator 1 refrigerant steam channel to be communicated with condenser 5 to be adjusted to generator 1 have refrigerant steam channel be communicated with the 5th generator 19 after the 5th generator 19 have cryogen liquid pipeline again through heat exchanger 18, 3rd generator 3, 4th generator 14 is communicated with evaporimeter 7 with second throttle 15, 5th generator 19 also has refrigerant steam channel to be communicated with condenser 5, heat exchanger 18 also has heated medium pipeline and ft connection.
(2) in flow process, the refrigerant vapour that generator 1 produces is supplied to the 5th generator 19 and does to drive thermal medium, the part weak solution of the second absorber 24 enters the 5th generator 19 through the 3rd solution pump 16 and the 4th solution heat exchanger 22, refrigerant vapour flows through the 5th generator 19, heating enters the solution release refrigerant vapour in it and provides to condenser 5, the concentrated solution of the 5th generator 19 enters the second generator 2 through the 4th solution heat exchanger 22 and the second solution heat exchanger 13, the refrigerant vapour heat release flowing through the 5th generator 19 becomes cryogen liquid, cryogen liquid flows through heat exchanger 18 successively, evaporimeter 7 is entered through second throttle 15 throttling again after 3rd generator 3 and the 4th generator 14 heat release cooling, form the 5th class absorption heat pump.
The 5th class absorption heat pump shown in Figure 10 is achieved in that
(1) in structure, in the 5th class absorption heat pump shown in Fig. 8, increase by the 5th generator, second throttle, 4th solution heat exchanger and heat exchanger, had by second absorber 24 weak solution pipeline to be communicated with generator 1 through solution pump 10 and solution heat exchanger 12 to be adjusted to the second absorber 24 and to have weak solution pipeline through solution pump 10, solution heat exchanger 12 is communicated with generator 1 with the 4th solution heat exchanger 22, had by generator 1 concentrated solution pipeline to be communicated with the second generator 2 through solution heat exchanger 12 and the second solution heat exchanger 13 to be adjusted to generator 1 and to have concentrated solution pipeline to be communicated with the 5th generator 19 through the 4th solution heat exchanger 22, 5th generator 19 has concentrated solution pipeline to be communicated with the second generator 2 with the second solution heat exchanger 13 through solution heat exchanger 12 again, had by generator 1 refrigerant steam channel to be communicated with condenser 5 to be adjusted to generator 1 have refrigerant steam channel be communicated with the 5th generator 19 after the 5th generator 19 have cryogen liquid pipeline again through heat exchanger 18, 3rd generator 3, 4th generator 14 is communicated with evaporimeter 7 with second throttle 15, 5th generator 19 also has refrigerant steam channel to be communicated with condenser 5, heat exchanger 18 also has heated medium pipeline and ft connection.
(2) in flow process, the refrigerant vapour that generator 1 produces is supplied to the 5th generator 19 and does to drive thermal medium, the weak solution of the second absorber 24 is through solution pump 10, solution heat exchanger 12 and the 4th solution heat exchanger 22 enter generator 1, the concentrated solution of generator 1 enters the 5th generator 19 through the 4th solution heat exchanger 22, refrigerant vapour flows through the 5th generator 19, heating enters the solution release refrigerant vapour in it and provides to condenser 5, the concentrated solution of the 5th generator 19 enters the second generator 2 through solution heat exchanger 12 and the second solution heat exchanger 13, the refrigerant vapour heat release flowing through the 5th generator 19 flows through heat exchanger 18 after becoming cryogen liquid again, 3rd generator 3 and the 4th generator 14 be progressively heat release cooling also, cryogen liquid after cooling enters evaporimeter 7 through second throttle 15 throttling, form the 5th class absorption heat pump.
The 5th class absorption heat pump shown in Figure 11 is achieved in that
(1) in structure, in the 5th class absorption heat pump shown in Fig. 8, increase by the 5th generator, second throttle, 3rd solution pump, 4th solution heat exchanger and heat exchanger, had by second absorber 24 weak solution pipeline to be communicated with generator 1 through solution pump 10 and solution heat exchanger 12 to be adjusted to the second absorber 24 and to have weak solution pipeline to be communicated with the 5th generator 19 with solution heat exchanger 12 through solution pump 10, 5th generator 19 has concentrated solution pipeline to be communicated with generator 1 with the 4th solution heat exchanger 22 through the 3rd solution pump 16 again, had by generator 1 concentrated solution pipeline to be communicated with the second generator 2 through solution heat exchanger 12 and the second solution heat exchanger 13 to be adjusted to generator 1 and to have concentrated solution pipeline through the 4th solution heat exchanger 22, solution heat exchanger 12 is communicated with the second generator 2 with the second solution heat exchanger 13, had by generator 1 refrigerant steam channel to be communicated with condenser 5 to be adjusted to generator 1 have refrigerant steam channel be communicated with the 5th generator 19 after the 5th generator 19 have cryogen liquid pipeline again through heat exchanger 18, 3rd generator 3, 4th generator 14 is communicated with evaporimeter 7 with second throttle 15, 5th generator 19 also has refrigerant steam channel to be communicated with condenser 5, heat exchanger 18 also has heated medium pipeline and ft connection.
(2) in flow process, the refrigerant vapour that generator 1 produces is supplied to the 5th generator 19 and does to drive thermal medium, the weak solution of the second absorber 24 enters the 5th generator 19 through solution pump 10 and solution heat exchanger 12, refrigerant vapour flows through the 5th generator 19, heating enters the solution release refrigerant vapour in it and provides to condenser 5, the concentrated solution of the 5th generator 19 enters generator 1 through the 3rd solution pump 16 and the 4th solution heat exchanger 22, the concentrated solution of generator 1 is through the 4th solution heat exchanger 22, solution heat exchanger 12 and the second solution heat exchanger 13 enter the second generator 2, the refrigerant vapour heat release flowing through the 5th generator 19 flows through heat exchanger 18, the 3rd generator 3 and the 4th generator 14 after becoming cryogen liquid and progressively heat release cooling again, cryogen liquid after cooling enters evaporimeter 7 through second throttle 15 throttling, forms the 5th class absorption heat pump.
The 5th class absorption heat pump shown in Figure 12 is achieved in that
(1) in structure, in the 5th class absorption heat pump shown in Fig. 1, increase by the 4th generator, 3rd solution pump, 3rd solution heat exchanger and the second absorber, had by absorber 4 weak solution pipeline to be communicated with generator 1 through solution pump 10 and solution heat exchanger 12 to be adjusted to absorber 4 and to have weak solution pipeline to be communicated with the second absorber 24 with the 3rd solution heat exchanger 17 through solution pump 10, second absorber 24 has weak solution pipeline to be communicated with generator 1 with solution heat exchanger 12 through the 3rd solution pump 16 again, had by generator 1 concentrated solution pipeline to be communicated with the second generator 2 through solution heat exchanger 12 and the second solution heat exchanger 13 to be adjusted to generator 1 and to have concentrated solution pipeline to be communicated with the 4th generator 14 through solution heat exchanger 12, 4th generator 14 has concentrated solution pipeline to be communicated with the second generator 2 with the second solution heat exchanger 13 through the 3rd solution heat exchanger 17 again, 4th generator 14 also has refrigerant steam channel to be communicated with the second absorber 24, 4th generator 14 also has driving heat medium pipeline and ft connection, second absorber 24 also has heated medium pipeline and ft connection.
(2) in flow process, the weak solution of absorber 4 enters the second absorber 24 through solution pump 10 and the 3rd solution heat exchanger 17, absorb refrigerant vapour heat release in heated medium, the weak solution of the second absorber 24 enters generator 1 through the 3rd solution pump 16 and solution heat exchanger 12, the concentrated solution of generator 1 enters the 4th generator 14 through solution heat exchanger 12, drive heat medium flow through the 4th generator 14, heating enters the solution release refrigerant vapour in it and is supplied to the second absorber 24, the concentrated solution of the 4th generator 14 enters the second generator 2 through the 3rd solution heat exchanger 17 and the second solution heat exchanger 13, form the 5th class absorption heat pump.
The 5th class absorption heat pump shown in Figure 13 is achieved in that
(1) in structure, in the 5th class absorption heat pump shown in Figure 12, increase by the 5th generator, second throttle, 4th solution pump, 4th solution heat exchanger and heat exchanger, second absorber 24 is set up weak solution pipeline and is communicated with the 5th generator 19 with the 4th solution heat exchanger 22 through the 4th solution pump 21, 5th generator 19 also has concentrated solution pipeline to be communicated with the 4th generator 14 through the 4th solution heat exchanger 22, had by generator 1 refrigerant steam channel to be communicated with condenser 5 to be adjusted to generator 1 have refrigerant steam channel be communicated with the 5th generator 19 after the 5th generator 19 have cryogen liquid pipeline again through heat exchanger 18, 3rd generator 3 is communicated with evaporimeter 7 with second throttle 15, 5th generator 19 also has refrigerant steam channel to be communicated with condenser 5, heat exchanger 18 also has heated medium pipeline and ft connection.
(2) in flow process, the refrigerant vapour that generator 1 produces is supplied to the 5th generator 19 and does to drive thermal medium, the part weak solution of the second absorber 24 enters the 5th generator 19 through the 4th solution pump 21 and the 4th solution heat exchanger 22, refrigerant vapour flows through the 5th generator 19, heating enters the solution release refrigerant vapour in it and provides to condenser 5, and the concentrated solution of the 5th generator 19 enters the 4th generator 14 through the 4th solution heat exchanger 22; The refrigerant vapour heat release flowing through the 5th generator 19 becomes cryogen liquid, and cryogen liquid enters evaporimeter 7 through second throttle 15 throttling after flowing through heat exchanger 18 and the 3rd generator 3 heat release cooling successively again, forms the 5th class absorption heat pump.
The 5th class absorption heat pump shown in Figure 14 is achieved in that
(1) in structure, in the 5th class absorption heat pump shown in Figure 12, increase by the 5th generator, second throttle, 4th solution heat exchanger and heat exchanger, had by second absorber 24 weak solution pipeline to be communicated with generator 1 through the 3rd solution pump 16 and solution heat exchanger 12 to be adjusted to the second absorber 24 and to have weak solution pipeline through the 3rd solution pump 16, solution heat exchanger 12 is communicated with generator 1 with the 4th solution heat exchanger 22, had by generator 1 concentrated solution pipeline to be communicated with the 4th generator 14 through solution heat exchanger 12 to be adjusted to generator 1 and to have concentrated solution pipeline to be communicated with the 5th generator 19 through the 4th solution heat exchanger 22, 5th generator 19 has concentrated solution pipeline to be communicated with the 4th generator 14 through solution heat exchanger 12 again, had by generator 1 refrigerant steam channel to be communicated with condenser 5 to be adjusted to generator 1 have refrigerant steam channel be communicated with the 5th generator 19 after the 5th generator 19 have cryogen liquid pipeline again through heat exchanger 18, 3rd generator 3 is communicated with evaporimeter 7 with second throttle 15, 5th generator 19 also has refrigerant steam channel to be communicated with condenser 5, 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 process, the refrigerant vapour driving thermal medium and generator 1 to produce provides thermic load to the 5th generator 19, the weak solution of the second absorber 24 is through the 3rd solution pump 16, solution heat exchanger 12 and the 4th solution heat exchanger 22 enter generator 1, the concentrated solution of generator 1 enters the 5th generator 19 through the 4th solution heat exchanger 22, thermal medium and refrigerant vapour is driven to flow through the 5th generator 19, heating enters the solution release refrigerant vapour in it and provides to condenser 5, the concentrated solution of the 5th generator 19 enters the 4th generator 14 through solution heat exchanger 12, the refrigerant vapour heat release flowing through the 5th generator 19 flows through heat exchanger 18 and the 3rd generator 3 and progressively heat release cooling again after becoming cryogen liquid, the cryogen liquid after cooling enters evaporimeter 7 through second throttle 15 throttling, forms the 5th class absorption heat pump.
The 5th class absorption heat pump shown in Figure 15 is achieved in that
(1) in structure, in the 5th class absorption heat pump shown in Figure 12, increase by the 5th generator, second throttle, 4th solution pump, 4th solution heat exchanger and heat exchanger, had by second absorber 24 weak solution pipeline to be communicated with generator 1 through the 3rd solution pump 16 and solution heat exchanger 12 to be adjusted to the second absorber 24 and to have weak solution pipeline to be communicated with the 5th generator 19 with solution heat exchanger 12 through the 3rd solution pump 16, 5th generator 19 has concentrated solution pipeline to be communicated with generator 1 with the 4th solution heat exchanger 22 through the 4th solution pump 21 again, had by generator 1 concentrated solution pipeline to be communicated with the 4th generator 14 through solution heat exchanger 12 to be adjusted to generator 1 and to have concentrated solution pipeline to be communicated with the 4th generator 14 with solution heat exchanger 12 through the 4th solution heat exchanger 22, had by generator 1 refrigerant steam channel to be communicated with condenser 5 to be adjusted to generator 1 have refrigerant steam channel be communicated with the 5th generator 19 after the 5th generator 19 have cryogen liquid pipeline again through heat exchanger 18, 3rd generator 3 is communicated with evaporimeter 7 with second throttle 15, 5th generator 19 also has refrigerant steam channel to be communicated with condenser 5, heat exchanger 18 also has heated medium pipeline and ft connection.
(2) in flow process, the refrigerant vapour that generator 1 produces is supplied to the 5th generator 19 and does to drive thermal medium, the weak solution of the second absorber 24 enters the 5th generator 19 through the 3rd solution pump 16 and solution heat exchanger 12, refrigerant vapour flows through the 5th generator 19, heating enters the solution release refrigerant vapour in it and provides to condenser 5, the concentrated solution of the 5th generator 19 enters generator 1 through the 4th solution pump 21 and the 4th solution heat exchanger 22, and the concentrated solution of generator 1 enters the 4th generator 14 through the 4th solution heat exchanger 22 and solution heat exchanger 12; The refrigerant vapour heat release flowing through the 5th generator 19 flows through heat exchanger 18 and the 3rd generator 3 and progressively heat release cooling again after becoming cryogen liquid, the cryogen liquid after cooling enters evaporimeter 7 through second throttle 15 throttling, forms the 5th class absorption heat pump.
The 5th class absorption heat pump shown in Figure 16 is achieved in that
(1) in structure, in the 5th class absorption heat pump shown in Figure 12, increase by the 5th generator, 4th solution heat exchanger and the 3rd absorber, had by absorber 4 weak solution pipeline to be communicated with the second absorber 24 through solution pump 10 and the 3rd solution heat exchanger 17 to be adjusted to absorber 4 and to have weak solution pipeline to be communicated with the 3rd absorber 25 through the 4th solution heat exchanger 22,3rd absorber 25 has weak solution pipeline to be communicated with the second absorber 24 with the 3rd solution heat exchanger 17 through solution pump 10 again, had by 3rd generator 3 concentrated solution pipeline to be communicated with absorber 4 through the second solution pump 11 and the second solution heat exchanger 13 to be adjusted to the 3rd generator 3 and to have concentrated solution pipeline to be communicated with the 5th generator 19 through the second solution heat exchanger 13,5th generator 19 has concentrated solution pipeline to be communicated with absorber 4 with the 4th solution heat exchanger 22 through the second solution pump 11 again, 5th generator 19 also has refrigerant steam channel to be communicated with the 3rd absorber 25, condenser 5 is had cryogen liquid pipeline be communicated with the 3rd generator 3 after the 3rd generator 3 have again cryogen liquid pipeline through choke valve 8 to be communicated with evaporimeter 7 be adjusted to condenser 5 have cryogen liquid pipeline to be communicated with the 3rd generator 3 after the 3rd generator 3 have cryogen liquid pipeline to be communicated with evaporimeter 7 with choke valve 8 through the 5th generator 19 again, 5th generator 19 also has surplus heat medium pipeline and ft connection, 3rd absorber 25 also has cooling medium pipeline and ft connection.
(2) in flow process, the weak solution of absorber 4 enters the 3rd absorber 25 through the 4th solution heat exchanger 22, absorb refrigerant vapour and heat release in cooling medium, the weak solution of the 3rd absorber 25 enters the second absorber 24 through solution pump 10 and the 3rd solution heat exchanger 17; The concentrated solution of the 3rd generator 3 enters the 5th generator 19 through the second solution heat exchanger 13, cryogen liquid and waste heat medium flow through the 5th generator 19, heating enters the solution release refrigerant vapour in it and provides to the 3rd absorber 25, and the concentrated solution of the 5th generator 19 enters absorber 4 through the second solution pump 11 and the 4th solution heat exchanger 22; The cryogen liquid of condenser 5 flows through the 3rd generator 3 and the also progressively heat release cooling of the 5th generator 19 successively, and the cryogen liquid after cooling enters evaporimeter 7 through choke valve 8 throttling, forms the 5th class absorption heat pump.
The 5th class absorption heat pump shown in Figure 17 is achieved in that
(1), in structure, it formed primarily of generator, the second generator, the 3rd generator, absorber, condenser, the second condenser, evaporimeter, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, the 4th generator, the 3rd solution heat exchanger and the second absorber, absorber 4 has weak solution pipeline to be communicated with the second absorber 24 through the 3rd solution heat exchanger 17, second absorber 24 also has weak solution pipeline to be communicated with generator 1 with solution heat exchanger 12 through solution pump 10, generator 1 also has concentrated solution pipeline to be communicated with the second generator 2 with the second solution heat exchanger 13 through solution heat exchanger 12, second generator 2 also has concentrated solution pipeline to be communicated with the 3rd generator 3, 3rd generator 3 has concentrated solution pipeline to be communicated with the 4th generator 14 through the second solution heat exchanger 13, 4th generator 14 also has concentrated solution pipeline to be communicated with absorber 4 with the 3rd solution heat exchanger 17 through the second solution pump 11, generator 1 also has refrigerant steam channel to be communicated with condenser 5, condenser 5 have cryogen liquid pipeline be communicated with the 3rd generator 3 after the 3rd generator 3 have cryogen liquid pipeline to be communicated with evaporimeter 7 through choke valve 8 again, second generator 2 and the 3rd generator 3 also have refrigerant steam channel to be communicated with the second condenser 6 respectively, second condenser 6 also has cryogen liquid pipeline to be communicated with evaporimeter 7 through cryogen liquid pump 9, 4th generator 14 also has refrigerant steam channel to be communicated with the second absorber 24, evaporimeter 7 also has refrigerant steam channel to be communicated with absorber 4, 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, evaporimeter 7, second generator 2 and the 4th generator 14 also have surplus heat medium pipeline and ft connection respectively, second condenser 6 and the second absorber 24 also have cooling medium pipeline and ft connection respectively.
(2) in flow process, the weak solution of absorber 4 enters the second absorber 24 through the 3rd solution heat exchanger 17, absorb refrigerant vapour heat release in cooling medium, the weak solution of the second absorber 24 enters generator 1 through solution pump 10 and solution heat exchanger 12, drive heat medium flow through generator 1, heating enters the solution release refrigerant vapour in it and provides to condenser 5, the concentrated solution of generator 1 enters the second generator 2 through solution heat exchanger 12 and the second solution heat exchanger 13, waste heat medium flows through the second generator 2, heating enters the solution release refrigerant vapour in it and provides to the second condenser 6, the concentrated solution of the second generator 2 enters the 3rd generator 3, heat absorption release refrigerant vapour also provides to the second condenser 6, the concentrated solution of the 3rd generator 3 enters the 4th generator 14 through the second solution heat exchanger 13, waste heat medium flows through the 4th generator 14, heating enters the solution release refrigerant vapour in it and provides to the second absorber 24, the concentrated solution of the 4th generator 14 enters absorber 4 through the second solution pump 11 and the 3rd solution heat exchanger 17, absorb refrigerant vapour heat release in heated medium, the refrigerant vapour heat release of condenser 5 becomes cryogen liquid in heated medium, the cryogen liquid of condenser 5 flows through after the 3rd generator 3 heat release is lowered the temperature and enters evaporimeter 7 through choke valve 8 throttling again, the refrigerant vapour heat release of the second condenser 6 becomes cryogen liquid in cooling medium, and the cryogen liquid of the second condenser 6 enters evaporimeter 7 through cryogen liquid pump 9 pressurization, the cryogen liquid of evaporimeter 7 absorbs waste heat and becomes refrigerant vapour, and the refrigerant vapour that evaporimeter 7 produces is supplied to absorber 4, forms the 5th class absorption heat pump.
The 5th class absorption heat pump shown in Figure 18 is achieved in that
(1) in structure, in the 5th class absorption heat pump shown in Figure 12, increase by the 5th generator, 4th solution heat exchanger and the 3rd absorber, had by absorber 4 weak solution pipeline to be communicated with the second absorber 24 through solution pump 10 and the 3rd solution heat exchanger 17 to be adjusted to absorber 4 and to have weak solution pipeline to be communicated with the 3rd absorber 25 through the 4th solution heat exchanger 22,3rd absorber 25 has weak solution pipeline to be communicated with the second absorber 24 with the 3rd solution heat exchanger 17 through solution pump 10 again, had by 3rd generator 3 concentrated solution pipeline to be communicated with absorber 4 through the second solution pump 11 and the second solution heat exchanger 13 to be adjusted to the 3rd generator 3 and to have concentrated solution pipeline to be communicated with the 5th generator 19 through the second solution heat exchanger 13,5th generator 19 has concentrated solution pipeline to be communicated with absorber 4 with the 4th solution heat exchanger 22 through the second solution pump 11 again, 5th generator 19 also has refrigerant steam channel to be communicated with the 3rd absorber 25,5th generator 19 also has surplus heat medium pipeline and ft connection, 3rd absorber 25 also has cooling medium pipeline and ft connection.
(2) in flow process, the weak solution of absorber 4 enters the 3rd absorber 25 through the 4th solution heat exchanger 22, absorb refrigerant vapour and heat release in cooling medium, the weak solution of the 3rd absorber 25 enters the second absorber 24 through solution pump 10 and the 3rd solution heat exchanger 17; The concentrated solution of the 3rd generator 3 enters the 5th generator 19 through the second solution heat exchanger 13, waste heat medium flows through the 5th generator 19, heating enters the solution release refrigerant vapour in it and provides 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, forms the 5th class absorption heat pump.
The 5th class absorption heat pump shown in Figure 19 is achieved in that
(1) in structure, in the 5th class absorption heat pump shown in Fig. 1, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by evaporimeter 7 refrigerant steam channel to be communicated with absorber 4 to be adjusted to evaporimeter 7 has refrigerant steam channel to be communicated with newly-increased absorber B, newly-increased absorber B also has weak solution pipeline to be communicated with newly-increased generator A with newly-increased solution heat exchanger D through newly-increased solution pump C, newly-increased generator A also has concentrated solution pipeline to be communicated with newly-increased absorber B through newly-increased solution heat exchanger D, newly-increased generator A also has refrigerant steam channel to be communicated with absorber 4, newly-increased generator A also has driving heat medium pipeline and ft connection, newly-increased absorber B also has heated medium pipeline and ft connection.
(2) in flow process, the refrigerant vapour that evaporimeter 7 produces enters newly-increased absorber B, the weak solution of newly-increased absorber B enters newly-increased generator A through newly-increased solution pump C and newly-increased solution heat exchanger D, heat medium flow is driven to enter the solution release refrigerant vapour in it through newly-increased generator A, heating and provide to absorber 4, the concentrated solution of newly-increased generator A enters newly-increased absorber B through newly-increased solution heat exchanger D, absorb refrigerant vapour and heat release in heated medium, form the 5th class absorption heat pump.
The 5th class absorption heat pump shown in Figure 20 is achieved in that
(1) in structure, in the 5th class absorption heat pump shown in Fig. 1, being had by generator 1 refrigerant steam channel to be communicated with condenser 5 to be adjusted to generator 1 has refrigerant steam channel to be communicated with newly-increased absorber B, newly-increased absorber B also has weak solution pipeline to be communicated with newly-increased generator A with newly-increased solution heat exchanger D through newly-increased solution pump C, newly-increased generator A also has concentrated solution pipeline to be communicated with newly-increased absorber B through newly-increased solution heat exchanger D, newly-increased generator A also has refrigerant steam channel to be communicated with condenser 5, newly-increased generator A also has driving heat medium pipeline and ft connection, newly-increased absorber B also has heated medium pipeline and ft connection.
(2) in flow process, the refrigerant vapour that generator 1 produces enters newly-increased absorber B, the weak solution of newly-increased absorber B enters newly-increased generator A through newly-increased solution pump C and newly-increased solution heat exchanger D, heat medium flow is driven to enter the solution release refrigerant vapour in it through newly-increased generator A, heating and provide to condenser 5, the concentrated solution of newly-increased generator A enters newly-increased absorber B through newly-increased solution heat exchanger D, absorb refrigerant vapour and heat release in heated medium, form the 5th class absorption heat pump.
The 5th class absorption heat pump shown in Figure 21 is achieved in that
In the 5th class absorption heat pump shown in Fig. 1, the 3rd generator 3 sets up waste heat medium pipeline and ft connection; Cryogen liquid and waste heat medium flow through the 3rd generator 3, and heating enters the solution release refrigerant vapour in it and provides to the second condenser 6, forms the 5th class absorption heat pump.
The 5th class absorption heat pump shown in Figure 22 is achieved in that
(1) in structure, in the 5th class absorption heat pump shown in Fig. 1, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by second generator 2 refrigerant steam channel to be communicated with the second condenser 6 to be adjusted to the second generator 2 has refrigerant steam channel to be communicated with newly-increased absorber B, newly-increased absorber B also has weak solution pipeline to be communicated with newly-increased generator A with newly-increased solution heat exchanger D through newly-increased solution pump C, newly-increased generator A also has concentrated solution pipeline to be communicated with newly-increased absorber B through newly-increased solution heat exchanger D, newly-increased generator A also has refrigerant steam channel to be communicated with the second condenser 6, newly-increased generator A also has surplus heat medium pipeline and ft connection, newly-increased absorber B also has cooling medium pipeline and ft connection.
(2) in flow process, the refrigerant vapour that second generator 2 produces enters newly-increased absorber B, the weak solution of newly-increased absorber B enters newly-increased generator A through newly-increased solution pump C and newly-increased solution heat exchanger D, waste heat medium flows through newly-increased generator A, heating enters the solution release refrigerant vapour in it and provides to the second condenser 6, the concentrated solution of newly-increased generator A enters newly-increased absorber B through newly-increased solution heat exchanger D, absorb refrigerant vapour and heat release in cooling medium, form the 5th class absorption heat pump.
The 5th class absorption heat pump shown in Figure 23 is achieved in that
In the 5th class absorption heat pump shown in Figure 19, being had by the 3rd generator 3 refrigerant steam channel to be communicated with the second condenser 6 to be adjusted to the 3rd generator 3 has refrigerant steam channel to be communicated with newly-increased absorber B, forms the 5th class absorption heat pump.
The 5th class absorption heat pump shown in Figure 24 is achieved in that
In the 5th class absorption heat pump shown in Fig. 1, had surplus heat by second generator 2 medium pipeline and ft connection is adjusted to the 3rd generator 3 and has surplus heat medium pipeline and ft connection, condenser 5 is had cryogen liquid pipeline be communicated with the 3rd generator 3 after the 3rd generator 3 have again cryogen liquid pipeline through choke valve 8 to be communicated with evaporimeter 7 be adjusted to condenser 5 have cryogen liquid pipeline to be communicated with the second generator 2 after the second generator 2 have cryogen liquid pipeline to be communicated with evaporimeter 7 through choke valve 8 again, form the 5th class absorption heat pump.
The 5th class absorption heat pump shown in Figure 25 is achieved in that
(1) in structure, in the 5th class absorption heat pump shown in Fig. 1, increase newly-increased condenser, newly-increased choke valve and new solubilization liquid choke valve, being had by second generator 2 concentrated solution pipeline to be communicated with the 3rd generator 3 to be adjusted to the second generator 2 has concentrated solution pipeline to be communicated with the 3rd generator 3 through new solubilization liquid choke valve G, being had by second generator 2 refrigerant steam channel to be communicated with the second condenser 6 to be adjusted to the second generator 2 has refrigerant steam channel to be communicated with newly-increased condenser E, newly-increased condenser E also has cryogen liquid pipeline to be communicated with the second condenser 6 through newly-increased choke valve F, newly-increased condenser E also has cooling medium pipeline and ft connection.
(2) in flow process, the concentrated solution of the second generator 2 enters the 3rd generator 3 through new solubilization liquid choke valve G reducing pressure by regulating flow, the refrigerant vapour that second generator 2 produces enters newly-increased condenser E, heat release becomes cryogen liquid in cooling medium, the cryogen liquid of newly-increased condenser E enters the second condenser 6 through newly-increased choke valve F reducing pressure by regulating flow, forms the 5th class absorption heat pump.
The effect that the technology of the present invention can realize---the 5th class absorption heat pump proposed by the invention, has following effect and advantage:
(1) propose new approaches, new ideas and new technology that the temperature difference utilizes, will development and the application of absorption heat pump technology be promoted.
(2) high temperature cryogen liquid can be solved well to the negative effect of UTILIZATION OF VESIDUAL HEAT IN degree, especially to the absorption heat pump flow process being Typical Representative with TFE-TDE solution, performance index and the utilization efficiency of heat energy of absorption heat pump can be significantly improved.
(3) effectively utilize the temperature difference between cryogen liquid and environment, effectively reduce the high temperature driven thermic load needed for generator, improve the value of high temperature driven thermic load.
(4) input of high temperature driven thermic load can be reduced, or improve the degree of UTILIZATION OF VESIDUAL HEAT IN, maybe can utilize the residual heat resources of lower temperature.
(5) provide multiple concrete technical scheme, numerous different actual state can be tackled, have the wider scope of application.
(6) enriched the type of absorption heat pump, extended the range of application of absorption heat pump, be conducive to adopting absorption heat pump to realize making full use of of the temperature difference better.

Claims (57)

1. the 5th class absorption heat pump, formed primarily of generator, the second generator, the 3rd generator, absorber, condenser, the second condenser, evaporimeter, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger; absorber (4) has weak solution pipeline to be communicated with generator (1) with solution heat exchanger (12) through solution pump (10), generator (1) also has concentrated solution pipeline to be communicated with the second generator (2) with the second solution heat exchanger (13) through solution heat exchanger (12), second generator (2) also has concentrated solution pipeline to be communicated with the 3rd generator (3), 3rd generator (3) also has concentrated solution pipeline to be communicated with absorber (4) with the second solution heat exchanger (13) through the second solution pump (11), generator (1) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) also have cryogen liquid pipeline be communicated with the 3rd generator (3) after the 3rd generator (3) have cryogen liquid pipeline to be communicated with evaporimeter (7) through choke valve (8) again, second generator (2) also has refrigerant steam channel to be communicated with the second condenser (6) with the 3rd generator (3) respectively, second condenser (6) also has cryogen liquid pipeline to be communicated with evaporimeter (7) through cryogen liquid pump (9), evaporimeter (7) also has refrigerant steam channel to be communicated with absorber (4), 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, evaporimeter (7) and the second generator (2) also have surplus heat medium pipeline and ft connection respectively, second condenser (6) also has cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
2. the 5th class absorption heat pump, in the 5th class absorption heat pump according to claim 1, cancel choke valve, there is by 3rd generator (3) cryogen liquid pipeline to be communicated with evaporimeter (7) through choke valve (8) to be adjusted to the 3rd generator (3) and to have cryogen liquid pipeline to be communicated with evaporimeter (7), form the 5th class absorption heat pump.
3. the 5th class absorption heat pump, in the 5th class absorption heat pump according to claim 1, increase by the 4th generator, second throttle, 3rd solution pump, 3rd solution heat exchanger and heat exchanger, absorber (4) is set up weak solution pipeline and is communicated with the 4th generator (14) with the 3rd solution heat exchanger (17) through the 3rd solution pump (16), 4th generator (14) also has concentrated solution pipeline to be communicated with the second generator (2) with the second solution heat exchanger (13) through the 3rd solution heat exchanger (17), had by generator (1) refrigerant steam channel to be communicated with condenser (5) to be adjusted to generator (1) have refrigerant steam channel be communicated with the 4th generator (14) after the 4th generator (14) have cryogen liquid pipeline again through heat exchanger (18), 3rd generator (3) is communicated with evaporimeter (7) with second throttle (15), 4th generator (14) also has refrigerant steam channel to be communicated with condenser (5), heat exchanger (18) also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
4. the 5th class absorption heat pump, in the 5th class absorption heat pump according to claim 1, increase by the 4th generator, second throttle, 3rd solution heat exchanger and heat exchanger, had by absorber (4) weak solution pipeline to be communicated with generator (1) through solution pump (10) and solution heat exchanger (12) to be adjusted to absorber (4) and to have weak solution pipeline through solution pump (10), solution heat exchanger (12) is communicated with generator (1) with the 3rd solution heat exchanger (17), had by generator (1) concentrated solution pipeline to be communicated with the second generator (2) through solution heat exchanger (12) and the second solution heat exchanger (13) to be adjusted to generator (1) and to have concentrated solution pipeline to be communicated with the 4th generator (14) through the 3rd solution heat exchanger (17), 4th generator (14) has concentrated solution pipeline to be communicated with the second generator (2) with the second solution heat exchanger (13) through solution heat exchanger (12) again, had by generator (1) refrigerant steam channel to be communicated with condenser (5) to be adjusted to generator (1) have refrigerant steam channel be communicated with the 4th generator (14) after the 4th generator (14) have cryogen liquid pipeline again through heat exchanger (18), 3rd generator (3) is communicated with evaporimeter (7) with second throttle (15), 4th generator (14) also has refrigerant steam channel to be communicated with condenser (5), 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, in the 5th class absorption heat pump according to claim 1, increase by the 4th generator, second throttle, 3rd solution pump, 3rd solution heat exchanger and heat exchanger, had by absorber (4) weak solution pipeline to be communicated with generator (1) through solution pump (10) and solution heat exchanger (12) to be adjusted to absorber (4) and to have weak solution pipeline to be communicated with the 4th generator (14) with solution heat exchanger (12) through solution pump (10), 4th generator (14) has concentrated solution pipeline to be communicated with generator (1) with the 3rd solution heat exchanger (17) through the 3rd solution pump (16) again, had by generator (1) concentrated solution pipeline to be communicated with the second generator (2) through solution heat exchanger (12) and the second solution heat exchanger (13) to be adjusted to generator (1) and to have concentrated solution pipeline through the 3rd solution heat exchanger (17), solution heat exchanger (12) is communicated with the second generator (2) with the second solution heat exchanger (13), had by generator (1) refrigerant steam channel to be communicated with condenser (5) to be adjusted to generator (1) have refrigerant steam channel be communicated with the 4th generator (14) after the 4th generator (14) have cryogen liquid pipeline again through heat exchanger (18), 3rd generator (3) is communicated with evaporimeter (7) with second throttle (15), 4th generator (14) also has refrigerant steam channel to be communicated with condenser (5), heat exchanger (18) also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
6. the 5th class absorption heat pump, in arbitrary 5th class absorption heat pump described in claim 3-5, cancel choke valve and second throttle, had by 3rd generator (3) cryogen liquid pipeline to be communicated with evaporimeter (7) through choke valve (8) to be adjusted to the 3rd generator (3) and to have cryogen liquid pipeline to be communicated with evaporimeter (7), had by 3rd generator (3) cryogen liquid pipeline to be communicated with evaporimeter (7) through second throttle (15) to be adjusted to the 3rd generator (3) and to have cryogen liquid pipeline to be communicated with evaporimeter (7), form the 5th class absorption heat pump.
7. the 5th class absorption heat pump, in the 5th class absorption heat pump according to claim 3, increase by the 5th generator, 3rd choke valve, 4th solution pump, 4th solution heat exchanger and the second heat exchanger, absorber (4) is set up weak solution pipeline and is communicated with the 5th generator (19) with the 4th solution heat exchanger (22) through the 4th solution pump (21), 5th generator (19) also has concentrated solution pipeline to be communicated with the second generator (2) with the second solution heat exchanger (13) through the 4th solution heat exchanger (22), had by 4th generator (14) refrigerant steam channel to be communicated with condenser (5) to be adjusted to the 4th generator (14) have refrigerant steam channel be communicated with the 5th generator (19) after the 5th generator (19) have cryogen liquid pipeline again through the second heat exchanger (23), 3rd generator (3) is communicated with evaporimeter (7) with the 3rd choke valve (20), 5th generator (19) also has refrigerant steam channel to be communicated with condenser (5), 4th generator (14) there is cryogen liquid pipeline through heat exchanger (18), 3rd generator (3) and second throttle (15) are communicated with evaporimeter (7) and are adjusted to the 4th generator (14) and have cryogen liquid pipeline through the 5th generator (19), heat exchanger (18), 3rd generator (3) is communicated with evaporimeter (7) with second throttle (15), 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, in the 5th class absorption heat pump according to claim 4, increase by the 5th generator, 3rd choke valve, 4th solution heat exchanger and the second heat exchanger, absorber (4) there is weak solution pipeline through solution pump (10), solution heat exchanger (12) and the 3rd solution heat exchanger (17) are communicated with generator (1) and are adjusted to absorber (4) and have weak solution pipeline through solution pump (10), solution heat exchanger (12), 4th solution heat exchanger (22) is communicated with generator (1) with the 3rd solution heat exchanger (17), had by 4th generator (14) concentrated solution pipeline to be communicated with the second generator (2) through solution heat exchanger (12) and the second solution heat exchanger (13) to be adjusted to the 4th generator (14) and to have concentrated solution pipeline to be communicated with the 5th generator (19) through the 4th solution heat exchanger (22), 5th generator (19) has concentrated solution pipeline to be communicated with the second generator (2) with the second solution heat exchanger (13) through solution heat exchanger (12) again, had by 4th generator (14) refrigerant steam channel to be communicated with condenser (5) to be adjusted to the 4th generator (14) have refrigerant steam channel be communicated with the 5th generator (19) after the 5th generator (19) have cryogen liquid pipeline again through the second heat exchanger (23), 3rd generator (3) is communicated with evaporimeter (7) with the 3rd choke valve (20), 5th generator (19) also has refrigerant steam channel to be communicated with condenser (5), 4th generator (14) there is cryogen liquid pipeline through heat exchanger (18), 3rd generator (3) and second throttle (15) are communicated with evaporimeter (7) and are adjusted to the 4th generator (14) and have cryogen liquid pipeline through the 5th generator (19), heat exchanger (18), 3rd generator (3) is communicated with evaporimeter (7) with second throttle (15), second heat exchanger (23) also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
9. the 5th class absorption heat pump, in the 5th class absorption heat pump according to claim 5, increase by the 5th generator, 3rd choke valve, 4th solution pump, 4th solution heat exchanger and the second heat exchanger, had by absorber (4) weak solution pipeline to be communicated with the 4th generator (14) through solution pump (10) and solution heat exchanger (12) to be adjusted to absorber (4) and to have weak solution pipeline to be communicated with the 5th generator (19) with solution heat exchanger (12) through solution pump (10), 5th generator (19) has concentrated solution pipeline to be communicated with the 4th generator (14) with the 4th solution heat exchanger (22) through the 4th solution pump (21) again, generator (1) there is concentrated solution pipeline through the 3rd solution heat exchanger (17), solution heat exchanger (12) and the second solution heat exchanger (13) are communicated with the second generator (2) and are adjusted to generator (1) and have concentrated solution pipeline through the 3rd solution heat exchanger (17), 4th solution heat exchanger (22), solution heat exchanger (12) is communicated with the second generator (2) with the second solution heat exchanger (13), had by 4th generator (14) refrigerant steam channel to be communicated with condenser (5) to be adjusted to the 4th generator (14) have refrigerant steam channel be communicated with the 5th generator (19) after the 5th generator (19) have cryogen liquid pipeline again through the second heat exchanger (23), 3rd generator (3) is communicated with evaporimeter (7) with the 3rd choke valve (20), 5th generator (19) also has refrigerant steam channel to be communicated with condenser (5), 4th generator (14) there is cryogen liquid pipeline through heat exchanger (18), 3rd generator (3) and second throttle (15) are communicated with evaporimeter (7) and are adjusted to the 4th generator (14) and have cryogen liquid pipeline through the 5th generator (19), heat exchanger (18), 3rd generator (3) is communicated with evaporimeter (7) with second throttle (15), second heat exchanger (23) also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
10. the 5th class absorption heat pump, in arbitrary 5th class absorption heat pump described in claim 7-9, cancel choke valve, second throttle and the 3rd choke valve, had by 3rd generator (3) cryogen liquid pipeline to be communicated with evaporimeter (7) through choke valve (8) to be adjusted to the 3rd generator (3) and to have cryogen liquid pipeline to be communicated with evaporimeter (7), had by 3rd generator (3) cryogen liquid pipeline to be communicated with evaporimeter (7) through second throttle (15) to be adjusted to the 3rd generator (3) and to have cryogen liquid pipeline to be communicated with evaporimeter (7), had by 3rd generator (3) cryogen liquid pipeline to be communicated with evaporimeter (7) through the 3rd choke valve (20) to be adjusted to the 3rd generator (3) and to have cryogen liquid pipeline to be communicated with evaporimeter (7), form the 5th class absorption heat pump.
11. the 5th class absorption heat pumps, formed primarily of generator, the second generator, the 3rd generator, absorber, condenser, the second condenser, evaporimeter, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, the 4th generator, the 3rd solution heat exchanger and the second absorber; absorber (4) has weak solution pipeline to be communicated with the second absorber (24) through the 3rd solution heat exchanger (17), second absorber (24) also has weak solution pipeline to be communicated with generator (1) with solution heat exchanger (12) through solution pump (10), generator (1) also has concentrated solution pipeline to be communicated with the second generator (2) with the second solution heat exchanger (13) through solution heat exchanger (12), second generator (2) also has concentrated solution pipeline to be communicated with the 3rd generator (3), 3rd generator (3) has concentrated solution pipeline to be communicated with the 4th generator (14) through the second solution heat exchanger (13), 4th generator (14) also has concentrated solution pipeline to be communicated with absorber (4) with the 3rd solution heat exchanger (17) through the second solution pump (11), generator (1) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) have cryogen liquid pipeline be communicated with the 3rd generator (3) after the 3rd generator (3) have cryogen liquid pipeline to be communicated with evaporimeter (7) with choke valve (8) through the 4th generator (14) again, second generator (2) also has refrigerant steam channel to be communicated with the second condenser (6) with the 3rd generator (3) respectively, second condenser (6) also has cryogen liquid pipeline to be communicated with evaporimeter (7) through cryogen liquid pump (9), 4th generator (14) also has refrigerant steam channel to be communicated with the second absorber (24), evaporimeter (7) also has refrigerant steam channel to be communicated with absorber (4), 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, evaporimeter (7) and the second generator (2) also have surplus heat medium pipeline and ft connection respectively, second condenser (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, in the 5th class absorption heat pump according to claim 11, cancel choke valve, there is by 4th generator (14) cryogen liquid pipeline to be communicated with evaporimeter (7) through choke valve (8) to be adjusted to the 4th generator (14) and to have cryogen liquid pipeline to be communicated with evaporimeter (7), form the 5th class absorption heat pump.
13. the 5th class absorption heat pumps, in the 5th class absorption heat pump according to claim 11, increase by the 5th generator, second throttle, 3rd solution pump, 4th solution heat exchanger and heat exchanger, second absorber (24) is set up weak solution pipeline and is communicated with the 5th generator (19) with the 4th solution heat exchanger (22) through the 3rd solution pump (16), 5th generator (19) also has concentrated solution pipeline to be communicated with the second generator (2) with the second solution heat exchanger (13) through the 4th solution heat exchanger (22), had by generator (1) refrigerant steam channel to be communicated with condenser (5) to be adjusted to generator (1) have refrigerant steam channel be communicated with the 5th generator (19) after the 5th generator (19) have cryogen liquid pipeline again through heat exchanger (18), 3rd generator (3), 4th generator (14) is communicated with evaporimeter (7) with second throttle (15), 5th generator (19) also has refrigerant steam channel to be communicated with condenser (5), heat exchanger (18) also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
14. the 5th class absorption heat pumps, in the 5th class absorption heat pump according to claim 11, increase by the 5th generator, second throttle, 4th solution heat exchanger and heat exchanger, had by second absorber (24) weak solution pipeline to be communicated with generator (1) through solution pump (10) and solution heat exchanger (12) to be adjusted to the second absorber (24) and to have weak solution pipeline through solution pump (10), solution heat exchanger (12) is communicated with generator (1) with the 4th solution heat exchanger (22), had by generator (1) concentrated solution pipeline to be communicated with the second generator (2) through solution heat exchanger (12) and the second solution heat exchanger (13) to be adjusted to generator (1) and to have concentrated solution pipeline to be communicated with the 5th generator (19) through the 4th solution heat exchanger (22), 5th generator (19) has concentrated solution pipeline to be communicated with the second generator (2) with the second solution heat exchanger (13) through solution heat exchanger (12) again, had by generator (1) refrigerant steam channel to be communicated with condenser (5) to be adjusted to generator (1) have refrigerant steam channel be communicated with the 5th generator (19) after the 5th generator (19) have cryogen liquid pipeline again through heat exchanger (18), 3rd generator (3), 4th generator (14) is communicated with evaporimeter (7) with second throttle (15), 5th generator (19) also has refrigerant steam channel to be communicated with condenser (5), 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, in the 5th class absorption heat pump according to claim 11, increase by the 5th generator, second throttle, 3rd solution pump, 4th solution heat exchanger and heat exchanger, had by second absorber (24) weak solution pipeline to be communicated with generator (1) through solution pump (10) and solution heat exchanger (12) to be adjusted to the second absorber (24) and to have weak solution pipeline to be communicated with the 5th generator (19) with solution heat exchanger (12) through solution pump (10), 5th generator (19) has concentrated solution pipeline to be communicated with generator (1) with the 4th solution heat exchanger (22) through the 3rd solution pump (16) again, had by generator (1) concentrated solution pipeline to be communicated with the second generator (2) through solution heat exchanger (12) and the second solution heat exchanger (13) to be adjusted to generator (1) and to have concentrated solution pipeline through the 4th solution heat exchanger (22), solution heat exchanger (12) is communicated with the second generator (2) with the second solution heat exchanger (13), had by generator (1) refrigerant steam channel to be communicated with condenser (5) to be adjusted to generator (1) have refrigerant steam channel be communicated with the 5th generator (19) after the 5th generator (19) have cryogen liquid pipeline again through heat exchanger (18), 3rd generator (3), 4th generator (14) is communicated with evaporimeter (7) with second throttle (15), 5th generator (19) also has refrigerant steam channel to be communicated 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, in arbitrary 5th class absorption heat pump described in claim 13-15, cancel choke valve and second throttle, had by 4th generator (14) cryogen liquid pipeline to be communicated with evaporimeter (7) through choke valve (8) to be adjusted to the 4th generator (14) and to have cryogen liquid pipeline to be communicated with evaporimeter (7), had by 4th generator (14) cryogen liquid pipeline to be communicated with evaporimeter (7) through second throttle (15) to be adjusted to the 4th generator (14) and to have cryogen liquid pipeline to be communicated with evaporimeter (7), form the 5th class absorption heat pump.
17. the 5th class absorption heat pumps, in the 5th class absorption heat pump according to claim 1, increase by the 4th generator, 3rd solution pump, 3rd solution heat exchanger and the second absorber, had by absorber (4) weak solution pipeline to be communicated with generator (1) through solution pump (10) and solution heat exchanger (12) to be adjusted to absorber (4) and to have weak solution pipeline to be communicated with the second absorber (24) with the 3rd solution heat exchanger (17) through solution pump (10), second absorber (24) has weak solution pipeline to be communicated with generator (1) with solution heat exchanger (12) through the 3rd solution pump (16) again, had by generator (1) concentrated solution pipeline to be communicated with the second generator (2) through solution heat exchanger (12) and the second solution heat exchanger (13) to be adjusted to generator (1) and to have concentrated solution pipeline to be communicated with the 4th generator (14) through solution heat exchanger (12), 4th generator (14) has concentrated solution pipeline to be communicated with the second generator (2) with the second solution heat exchanger (13) through the 3rd solution heat exchanger (17) again, 4th generator (14) also has refrigerant steam channel to be communicated with the second absorber (24), 4th generator (14) also has driving heat medium pipeline and ft connection, second absorber (24) also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
18. the 5th class absorption heat pumps, in the 5th class absorption heat pump according to claim 17, cancel choke valve, there is by 3rd generator (3) cryogen liquid pipeline to be communicated with evaporimeter (7) through choke valve (8) to be adjusted to the 3rd generator (3) and to have cryogen liquid pipeline to be communicated with evaporimeter (7), form the 5th class absorption heat pump.
19. the 5th class absorption heat pumps, in the 5th class absorption heat pump according to claim 17, increase by the 5th generator, second throttle, 4th solution pump, 4th solution heat exchanger and heat exchanger, second absorber (24) is set up weak solution pipeline and is communicated with the 5th generator (19) with the 4th solution heat exchanger (22) through the 4th solution pump (21), 5th generator (19) also has concentrated solution pipeline to be communicated with the 4th generator (14) through the 4th solution heat exchanger (22), had by generator (1) refrigerant steam channel to be communicated with condenser (5) to be adjusted to generator (1) have refrigerant steam channel be communicated with the 5th generator (19) after the 5th generator (19) have cryogen liquid pipeline again through heat exchanger (18), 3rd generator (3) is communicated with evaporimeter (7) with second throttle (15), 5th generator (19) also has refrigerant steam channel to be communicated with condenser (5), heat exchanger (18) also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
20. the 5th class absorption heat pumps, in the 5th class absorption heat pump according to claim 17, increase by the 5th generator, second throttle, 4th solution heat exchanger and heat exchanger, had by second absorber (24) weak solution pipeline to be communicated with generator (1) through the 3rd solution pump (16) and solution heat exchanger (12) to be adjusted to the second absorber (24) and to have weak solution pipeline through the 3rd solution pump (16), solution heat exchanger (12) is communicated with generator (1) with the 4th solution heat exchanger (22), had by generator (1) concentrated solution pipeline to be communicated with the 4th generator (14) through solution heat exchanger (12) to be adjusted to generator (1) and to have concentrated solution pipeline to be communicated with the 5th generator (19) through the 4th solution heat exchanger (22), 5th generator (19) has concentrated solution pipeline to be communicated with the 4th generator (14) through solution heat exchanger (12) again, had by generator (1) refrigerant steam channel to be communicated with condenser (5) to be adjusted to generator (1) have refrigerant steam channel be communicated with the 5th generator (19) after the 5th generator (19) have cryogen liquid pipeline again through heat exchanger (18), 3rd generator (3) is communicated with evaporimeter (7) with second throttle (15), 5th generator (19) also has refrigerant steam channel to be communicated 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, in the 5th class absorption heat pump according to claim 17, increase by the 5th generator, second throttle, 4th solution pump, 4th solution heat exchanger and heat exchanger, had by second absorber (24) weak solution pipeline to be communicated with generator (1) through the 3rd solution pump (16) and solution heat exchanger (12) to be adjusted to the second absorber (24) and to have weak solution pipeline to be communicated with the 5th generator (19) with solution heat exchanger (12) through the 3rd solution pump (16), 5th generator (19) has concentrated solution pipeline to be communicated with generator (1) with the 4th solution heat exchanger (22) through the 4th solution pump (21) again, had by generator (1) concentrated solution pipeline to be communicated with the 4th generator (14) through solution heat exchanger (12) to be adjusted to generator (1) and to have concentrated solution pipeline to be communicated with the 4th generator (14) with solution heat exchanger (12) through the 4th solution heat exchanger (22), had by generator (1) refrigerant steam channel to be communicated with condenser (5) to be adjusted to generator (1) have refrigerant steam channel be communicated with the 5th generator (19) after the 5th generator (19) have cryogen liquid pipeline again through heat exchanger (18), 3rd generator (3) is communicated with evaporimeter (7) with second throttle (15), 5th generator (19) also has refrigerant steam channel to be communicated with condenser (5), heat exchanger (18) also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
22. the 5th class absorption heat pumps are in arbitrary 5th class absorption heat pump described in claim 19-21, and the 5th generator (19) is set up and driven heat medium pipeline and ft connection, forms the 5th class absorption heat pump.
23. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in claim 19-22, cancel choke valve and second throttle, had by 3rd generator (3) cryogen liquid pipeline to be communicated with evaporimeter (6) through choke valve (8) to be adjusted to the 3rd generator (3) and to have cryogen liquid pipeline to be communicated with evaporimeter (7), had by 3rd generator (3) cryogen liquid pipeline to be communicated with evaporimeter (7) through second throttle (15) to be adjusted to the 3rd generator (3) and to have cryogen liquid pipeline to be communicated with evaporimeter (7), form the 5th class absorption heat pump.
24. the 5th class absorption heat pumps, in the 5th class absorption heat pump according to claim 17, increase by the 5th generator, 4th solution heat exchanger and the 3rd absorber, had by absorber (4) weak solution pipeline to be communicated with the second absorber (24) through solution pump (10) and the 3rd solution heat exchanger (17) to be adjusted to absorber (4) and to have weak solution pipeline to be communicated with the 3rd absorber (25) through the 4th solution heat exchanger (22), 3rd absorber (25) has weak solution pipeline to be communicated with the second absorber (24) with the 3rd solution heat exchanger (17) through solution pump (10) again, had by 3rd generator (3) concentrated solution pipeline to be communicated with absorber (4) through the second solution pump (11) and the second solution heat exchanger (13) to be adjusted to the 3rd generator (3) and to have concentrated solution pipeline to be communicated with the 5th generator (19) through the second solution heat exchanger (13), 5th generator (19) has concentrated solution pipeline to be communicated with absorber (4) with the 4th solution heat exchanger (22) through the second solution pump (11) again, 5th generator (19) also has refrigerant steam channel to be communicated with the 3rd absorber (25), condenser (5) is had cryogen liquid pipeline be communicated with the 3rd generator (3) after the 3rd generator (3) have again cryogen liquid pipeline through choke valve (8) to be communicated with evaporimeter (7) be adjusted to condenser (5) have cryogen liquid pipeline to be communicated with the 3rd generator (3) after the 3rd generator (3) have cryogen liquid pipeline to be communicated with evaporimeter (7) with choke valve (8) through the 5th generator (19) again, 3rd absorber (25) also has cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
25. the 5th class absorption heat pumps, in the 5th class absorption heat pump according to claim 24, cancel choke valve, there is by 5th generator (19) cryogen liquid pipeline to be communicated with evaporimeter (7) through choke valve (8) to be adjusted to the 5th generator (19) and to have cryogen liquid pipeline to be communicated with evaporimeter (7), form the 5th class absorption heat pump.
26. the 5th class absorption heat pumps, formed primarily of generator, the second generator, the 3rd generator, absorber, condenser, the second condenser, evaporimeter, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, the 4th generator, the 3rd solution heat exchanger and the second absorber; absorber (4) has weak solution pipeline to be communicated with the second absorber (24) through the 3rd solution heat exchanger (17), second absorber (24) also has weak solution pipeline to be communicated with generator (1) with solution heat exchanger (12) through solution pump (10), generator (1) also has concentrated solution pipeline to be communicated with the second generator (2) with the second solution heat exchanger (13) through solution heat exchanger (12), second generator (2) also has concentrated solution pipeline to be communicated with the 3rd generator (3), 3rd generator (3) has concentrated solution pipeline to be communicated with the 4th generator (14) through the second solution heat exchanger (13), 4th generator (14) also has concentrated solution pipeline to be communicated with absorber (4) with the 3rd solution heat exchanger (17) through the second solution pump (11), generator (1) also has refrigerant steam channel to be communicated with condenser (5), condenser (5) have cryogen liquid pipeline be communicated with the 3rd generator (3) after the 3rd generator (3) have cryogen liquid pipeline to be communicated with evaporimeter (7) through choke valve (8) again, second generator (2) also has refrigerant steam channel to be communicated with the second condenser (6) with the 3rd generator (3) respectively, second condenser (6) also has cryogen liquid pipeline to be communicated with evaporimeter (7) through cryogen liquid pump (9), 4th generator (14) also has refrigerant steam channel to be communicated with the second absorber (24), evaporimeter (7) also has refrigerant steam channel to be communicated with absorber (4), 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, evaporimeter (7), second generator (2) and the 4th generator (14) also have surplus heat medium pipeline and ft connection respectively, second condenser (6) and the second absorber (24) also have cooling medium pipeline and ft connection respectively, form the 5th class absorption heat pump.
27. the 5th class absorption heat pumps, in the 5th class absorption heat pump according to claim 26, cancel choke valve, there is by 3rd generator (3) cryogen liquid pipeline to be communicated with evaporimeter (7) through choke valve (8) to be adjusted to the 3rd generator (3) and to have cryogen liquid pipeline to be communicated with evaporimeter (7), form the 5th class absorption heat pump.
28. the 5th class absorption heat pumps, in the 5th class absorption heat pump according to claim 11, increase by the 5th generator, second throttle, 3rd solution pump, 4th solution heat exchanger and heat exchanger, second absorber (24) is set up weak solution pipeline and is communicated with the 5th generator (19) with the 4th solution heat exchanger (22) through the 3rd solution pump (16), 5th generator (19) also has concentrated solution pipeline to be communicated with the second generator (2) with the second solution heat exchanger (13) through the 4th solution heat exchanger (22), had by generator (1) refrigerant steam channel to be communicated with condenser (5) to be adjusted to generator (1) have refrigerant steam channel be communicated with the 5th generator (19) after the 5th generator (19) have cryogen liquid pipeline again through heat exchanger (18), 3rd generator (3) is communicated with evaporimeter (7) with second throttle (15), 5th generator (19) also has refrigerant steam channel to be communicated with condenser (5), heat exchanger (18) also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
29. the 5th class absorption heat pumps, in the 5th class absorption heat pump according to claim 11, increase by the 5th generator, second throttle, 4th solution heat exchanger and heat exchanger, had by second absorber (24) weak solution pipeline to be communicated with generator (1) through solution pump (10) and solution heat exchanger (12) to be adjusted to the second absorber (24) and to have weak solution pipeline through solution pump (10), solution heat exchanger (12) is communicated with generator (1) with the 4th solution heat exchanger (22), had by generator (1) concentrated solution pipeline to be communicated with the second generator (2) through solution heat exchanger (12) and the second solution heat exchanger (13) to be adjusted to generator (1) and to have concentrated solution pipeline to be communicated with the 5th generator (19) through the 4th solution heat exchanger (22), 5th generator (19) has concentrated solution pipeline to be communicated with the second generator (2) with the second solution heat exchanger (13) through solution heat exchanger (12) again, had by generator (1) refrigerant steam channel to be communicated with condenser (5) to be adjusted to generator (1) have refrigerant steam channel be communicated with the 5th generator (19) after the 5th generator (19) have cryogen liquid pipeline again through heat exchanger (18), 3rd generator (3) is communicated with evaporimeter (7) with second throttle (15), 5th generator (19) also has refrigerant steam channel to be communicated with condenser (5), heat exchanger (18) also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
30. the 5th class absorption heat pumps, in the 5th class absorption heat pump according to claim 11, increase by the 5th generator, second throttle, 3rd solution pump, 4th solution heat exchanger and heat exchanger, had by second absorber (24) weak solution pipeline to be communicated with generator (1) through solution pump (10) and solution heat exchanger (12) to be adjusted to the second absorber (24) and to have weak solution pipeline to be communicated with the 5th generator (19) with solution heat exchanger (12) through solution pump (10), 5th generator (19) has concentrated solution pipeline to be communicated with generator (1) with the 4th solution heat exchanger (22) through the 3rd solution pump (16) again, had by generator (1) concentrated solution pipeline to be communicated with the second generator (2) through solution heat exchanger (12) and the second solution heat exchanger (13) to be adjusted to generator (1) and to have concentrated solution pipeline through the 4th solution heat exchanger (22), solution heat exchanger (12) is communicated with the second generator (2) with the second solution heat exchanger (13), had by generator (1) refrigerant steam channel to be communicated with condenser (5) to be adjusted to generator (1) have refrigerant steam channel be communicated with the 5th generator (19) after the 5th generator (19) have cryogen liquid pipeline again through heat exchanger (18), 3rd generator (3) is communicated with evaporimeter (7) with second throttle (15), 5th generator (19) also has refrigerant steam channel to be communicated with condenser (5), heat exchanger (18) also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
31. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in claim 28-30, cancel choke valve and second throttle, had by 3rd generator (3) cryogen liquid pipeline to be communicated with evaporimeter (7) through choke valve (8) to be adjusted to the 3rd generator (3) and to have cryogen liquid pipeline to be communicated with evaporimeter (7), had by 3rd generator (3) cryogen liquid pipeline to be communicated with evaporimeter (7) through second throttle (15) to be adjusted to the 3rd generator (3) and to have cryogen liquid pipeline to be communicated with evaporimeter (7), form the 5th class absorption heat pump.
32. the 5th class absorption heat pumps, in the 5th class absorption heat pump according to claim 17, increase by the 5th generator, 4th solution heat exchanger and the 3rd absorber, had by absorber (4) weak solution pipeline to be communicated with the second absorber (24) through solution pump (10) and the 3rd solution heat exchanger (17) to be adjusted to absorber (4) and to have weak solution pipeline to be communicated with the 3rd absorber (25) through the 4th solution heat exchanger (22), 3rd absorber (25) has weak solution pipeline to be communicated with the second absorber (24) with the 3rd solution heat exchanger (17) through solution pump (10) again, had by 3rd generator (3) concentrated solution pipeline to be communicated with absorber (4) through the second solution pump (11) and the second solution heat exchanger (13) to be adjusted to the 3rd generator (3) and to have concentrated solution pipeline to be communicated with the 5th generator (19) through the second solution heat exchanger (13), 5th generator (19) has concentrated solution pipeline to be communicated with absorber (4) with the 4th solution heat exchanger (22) through the second solution pump (11) again, 5th generator (19) also has refrigerant steam channel to be communicated with the 3rd absorber (25), 5th generator (19) also has surplus heat medium pipeline and ft connection, 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, in the 5th class absorption heat pump according to claim 32, cancel choke valve, there is by 3rd generator (3) cryogen liquid pipeline to be communicated with evaporimeter (7) through choke valve (8) to be adjusted to the 3rd generator (3) and to have cryogen liquid pipeline to be communicated with evaporimeter (7), form the 5th class absorption heat pump.
34. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in claim 1-33, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by evaporimeter (7) refrigerant steam channel to be communicated with absorber (4) to be adjusted to evaporimeter (7) has refrigerant steam channel to be communicated with newly-increased absorber (B), newly-increased absorber (B) also has weak solution pipeline to be communicated with newly-increased generator (A) with newly-increased solution heat exchanger (D) through newly-increased solution pump (C), newly-increased generator (A) also has concentrated solution pipeline to be communicated with newly-increased absorber (B) through newly-increased solution heat exchanger (D), newly-increased generator (A) also has refrigerant steam channel to be communicated with absorber (4), newly-increased generator (A) also has driving heat medium pipeline and ft connection, newly-increased absorber (B) also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
35. the 5th class absorption heat pumps, at claim 1-2, 11-12, 17-18, 24-27, in arbitrary 5th class absorption heat pump described in 32-33, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by generator (1) refrigerant steam channel to be communicated with condenser (5) to be adjusted to generator (1) has refrigerant steam channel to be communicated with newly-increased absorber (B), newly-increased absorber (B) also has weak solution pipeline to be communicated with newly-increased generator (A) with newly-increased solution heat exchanger (D) through newly-increased solution pump (C), newly-increased generator (A) also has concentrated solution pipeline to be communicated with newly-increased absorber (B) through newly-increased solution heat exchanger (D), newly-increased generator (A) also has refrigerant steam channel to be communicated with condenser (5), newly-increased generator (A) also has driving heat medium pipeline and ft connection, newly-increased absorber (B) also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
36. the 5th class absorption heat pumps are that the 3rd generator (3) sets up waste heat medium pipeline and ft connection in arbitrary 5th class absorption heat pump described in claim 1-10,17-23,26-33, form the 5th class absorption heat pump.
37. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in claim 11-16,3rd generator (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, in arbitrary 5th class absorption heat pump described in claim 11-16,3rd generator (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, in arbitrary 5th class absorption heat pump described in claim 24-25,3rd generator (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, in arbitrary 5th class absorption heat pump described in claim 24-25,3rd generator (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, in arbitrary 5th class absorption heat pump described in claim 36-40, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by evaporimeter (7) refrigerant steam channel to be communicated with absorber (4) to be adjusted to evaporimeter (7) has refrigerant steam channel to be communicated with newly-increased absorber (B), newly-increased absorber (B) also has weak solution pipeline to be communicated with newly-increased generator (A) with newly-increased solution heat exchanger (D) through newly-increased solution pump (C), newly-increased generator (A) also has concentrated solution pipeline to be communicated with newly-increased absorber (B) through newly-increased solution heat exchanger (D), newly-increased generator (A) also has refrigerant steam channel to be communicated with absorber (4), newly-increased generator (A) also has driving heat medium pipeline and ft connection, newly-increased absorber (B) also has heated medium pipeline and ft connection, form the 5th class absorption heat pump.
42. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in claim 1-33, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by 3rd generator (3) refrigerant steam channel to be communicated with the second condenser (6) to be adjusted to the 3rd generator (3) has refrigerant steam channel to be communicated with newly-increased absorber (B), newly-increased absorber (B) also has weak solution pipeline to be communicated with newly-increased generator (A) with newly-increased solution heat exchanger (D) through newly-increased solution pump (C), newly-increased generator (A) also has concentrated solution pipeline to be communicated with newly-increased absorber (B) through newly-increased solution heat exchanger (D), newly-increased generator (A) also has refrigerant steam channel to be communicated with the second condenser (6), newly-increased generator (A) also has surplus heat medium pipeline and ft connection, newly-increased absorber (B) also has cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
43. the 5th class absorption heat pumps, at claim 1-10, in arbitrary 5th class absorption heat pump described in 17-23, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by second generator (2) refrigerant steam channel to be communicated with the second condenser (6) to be adjusted to the second generator (2) has refrigerant steam channel to be communicated with newly-increased absorber (B), newly-increased absorber (B) also has weak solution pipeline to be communicated with newly-increased generator (A) with newly-increased solution heat exchanger (D) through newly-increased solution pump (C), newly-increased generator (A) also has concentrated solution pipeline to be communicated with newly-increased absorber (B) through newly-increased solution heat exchanger (D), newly-increased generator (A) also has refrigerant steam channel to be communicated with the second condenser (6), newly-increased generator (A) also has surplus heat medium pipeline and ft connection, newly-increased absorber (B) also has cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
44. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump according to claim 43, being had by 3rd generator (3) refrigerant steam channel to be communicated with the second condenser (6) to be adjusted to the 3rd generator (3) has refrigerant steam channel to be communicated with newly-increased absorber (B), forms the 5th class absorption heat pump.
45. the 5th class absorption heat pumps are that the 3rd generator (3) sets up waste heat medium pipeline and ft connection in arbitrary 5th class absorption heat pump described in claim 42-44, form the 5th class absorption heat pump.
46. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in claim 11-16, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by 4th generator (14) refrigerant steam channel to be communicated with the second absorber (24) to be adjusted to the 4th generator (14) has refrigerant steam channel to be communicated with newly-increased absorber (B), newly-increased absorber (B) also has weak solution pipeline to be communicated with newly-increased generator (A) with newly-increased solution heat exchanger (D) through newly-increased solution pump (C), newly-increased generator (A) also has concentrated solution pipeline to be communicated with newly-increased absorber (B) through newly-increased solution heat exchanger (D), newly-increased generator (A) also has refrigerant steam channel to be communicated with the second absorber (24), newly-increased generator (A) also has surplus heat medium pipeline and ft connection, newly-increased absorber (B) also has cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
47. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump according to claim 46,3rd generator (3) and the 4th generator (14) set up waste heat medium pipeline and ft connection respectively, form the 5th class absorption heat pump.
48. the 5th class absorption heat pumps, be in arbitrary 5th class absorption heat pump according to claim 46, the 3rd generator (3) or the 4th generator (14) set up waste heat medium pipeline and ft connection, form the 5th class absorption heat pump.
49. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in claim 24-25, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by 5th generator (19) refrigerant steam channel to be communicated with the 3rd absorber (25) to be adjusted to the 5th generator (19) has refrigerant steam channel to be communicated with newly-increased absorber (B), newly-increased absorber (B) also has weak solution pipeline to be communicated with newly-increased generator (A) with newly-increased solution heat exchanger (D) through newly-increased solution pump (C), newly-increased generator (A) also has concentrated solution pipeline to be communicated with newly-increased absorber (B) through newly-increased solution heat exchanger (D), newly-increased generator (A) also has refrigerant steam channel to be communicated with the 3rd absorber (25), newly-increased generator (A) also has surplus heat medium pipeline and ft connection, newly-increased absorber (B) also has cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
50. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump according to claim 49,3rd generator (3) and the 5th generator (19) set up waste heat medium pipeline and ft connection respectively, form the 5th class absorption heat pump.
51. the 5th class absorption heat pumps, be in arbitrary 5th class absorption heat pump according to claim 49, the 3rd generator (3) or the 5th generator (19) set up waste heat medium pipeline and ft connection, form the 5th class absorption heat pump.
52. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in claim 26-31, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by 4th generator (14) refrigerant steam channel to be communicated with the second absorber (24) to be adjusted to the 4th generator (14) has refrigerant steam channel to be communicated with newly-increased absorber (B), newly-increased absorber (B) also has weak solution pipeline to be communicated with newly-increased generator (A) with newly-increased solution heat exchanger (D) through newly-increased solution pump (C), newly-increased generator (A) also has concentrated solution pipeline to be communicated with newly-increased absorber (B) through newly-increased solution heat exchanger (D), newly-increased generator (A) also has refrigerant steam channel to be communicated with the second absorber (24), newly-increased generator (A) also has surplus heat medium pipeline and ft connection, newly-increased absorber (B) also has cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
53. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in claim 32-33, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, being had by 5th generator (19) refrigerant steam channel to be communicated with the 3rd absorber (25) to be adjusted to the 5th generator (19) has refrigerant steam channel to be communicated with newly-increased absorber (B), newly-increased absorber (B) also has weak solution pipeline to be communicated with newly-increased generator (A) with newly-increased solution heat exchanger (D) through newly-increased solution pump (C), newly-increased generator (A) also has concentrated solution pipeline to be communicated with newly-increased absorber (B) through newly-increased solution heat exchanger (D), newly-increased generator (A) also has refrigerant steam channel to be communicated with the 3rd absorber (25), newly-increased generator (A) also has surplus heat medium pipeline and ft connection, newly-increased absorber (B) also has cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
54. the 5th class absorption heat pumps are that the 3rd generator (3) sets up waste heat medium pipeline and ft connection in arbitrary 5th class absorption heat pump described in claim 52-53, form the 5th class absorption heat pump.
55. the 5th class absorption heat pumps, at claim 1-2, 17-18, 26-27, in arbitrary 5th class absorption heat pump described in 32-33, had surplus heat by second generator (2) medium pipeline and ft connection is adjusted to the 3rd generator (3) and has surplus heat medium pipeline and ft connection, condenser (5) is had cryogen liquid pipeline be communicated with the 3rd generator (3) after the 3rd generator (3) have again cryogen liquid pipeline through choke valve (8) to be communicated with evaporimeter (7) be adjusted to condenser (5) have cryogen liquid pipeline to be communicated with the second generator (2) after the second generator (2) have cryogen liquid pipeline to be communicated with evaporimeter (7) through choke valve (8) again, form the 5th class absorption heat pump.
56. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in claim 1-41, increase newly-increased condenser, newly-increased choke valve and new solubilization liquid choke valve, being had by second generator (2) concentrated solution pipeline to be communicated with the 3rd generator (3) to be adjusted to the second generator (2) has concentrated solution pipeline to be communicated with the 3rd generator (3) through new solubilization liquid choke valve (G), being had by second generator (2) refrigerant steam channel to be communicated with the second condenser (6) to be adjusted to the second generator (2) has refrigerant steam channel to be communicated with newly-increased condenser (E), newly-increased condenser (E) also has cryogen liquid pipeline to be communicated with the second condenser (6) or evaporimeter (7) through newly-increased choke valve (F), newly-increased condenser (E) also has cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
57. the 5th class absorption heat pumps, in arbitrary 5th class absorption heat pump described in claim 1-41, increase newly-increased condenser, newly-increased cryogen liquid pump and new solubilization liquid choke valve, being had by second generator (2) concentrated solution pipeline to be communicated with the 3rd generator (3) to be adjusted to the second generator (2) has concentrated solution pipeline to be communicated with the 3rd generator (3) through new solubilization liquid choke valve (G), being had by second generator (2) refrigerant steam channel to be communicated with the second condenser (6) to be adjusted to the second generator (2) has refrigerant steam channel to be communicated with newly-increased condenser (E), newly-increased condenser (E) also has cryogen liquid pipeline to be communicated with evaporimeter (7) through newly-increased cryogen liquid pump, newly-increased condenser (E) also has cooling medium pipeline and ft connection, form the 5th class absorption heat pump.
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