CN105928246A - Class-V thermally-driven compression-absorption type heat pump - Google Patents

Class-V thermally-driven compression-absorption type heat pump Download PDF

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Publication number
CN105928246A
CN105928246A CN201610307491.3A CN201610307491A CN105928246A CN 105928246 A CN105928246 A CN 105928246A CN 201610307491 A CN201610307491 A CN 201610307491A CN 105928246 A CN105928246 A CN 105928246A
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generator
solution
heat exchanger
pump
connect
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CN105928246B (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
    • F25B25/00—Machines, plants or systems, using a combination of modes of operation covered by two or more of the groups F25B1/00 - F25B23/00
    • F25B25/02—Compression-sorption machines, plants, or systems
    • 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
    • F25B41/00—Fluid-circulation arrangements
    • F25B41/30—Expansion means; Dispositions thereof
    • 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
    • F25B2327/00—Refrigeration system using an engine for driving a compressor

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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 class-V thermally-driven compression-absorption type heat pump and belongs to the technical field of power and heat pumps. Solution circulation is formed by a generator, a second generator, an absorber, a solution pump, a solution heat exchanger and a second solution heat exchanger. The generator communicates with a condenser through a refrigerant steam channel. The condenser communicates with an evaporator through a refrigerant pump. The second generator communicates with a compressor, a high-temperature heat exchanger, an expansion machine and a second condenser sequentially through a refrigerant steam channel. The second condenser communicates with the evaporator by means of a refrigerant pipeline via the generator and a throttling valve. The evaporator communicates with the absorber through a refrigerant steam channel. The second generator and the high-temperature heat exchanger communicate with the outside through a high-temperature heat medium channel; the absorber and the second condenser communicate with the outside through a heated medium channel; the generator and the evaporator communicate with the outside through a low-temperature heat medium channel; and the condenser communicates with the outside through a cooling medium channel. The expansion machine is connected with the compressor and transmits power. Thus, the class-V thermally-driven compression-absorption type heat pump is formed.

Description

5th class thermal drivers compressing-absorbing type heat pump
Technical field:
The invention belongs to power, refrigeration and technical field of heat pumps.
Background technology:
Cold demand, heat demand and power demand, central with production for human lives common；In reality, people it is frequently necessary to profit Realize refrigeration, heat supply by high temperature heat or be converted into power, it is also desirable to utilizing power to carry out freezing or utilizing power and combine Low temperature heat energy carries out heat supply.During stating purpose in realization, many considerations will be faced or condition will limit, including the energy Type, grade and quantity, the type of user's request, grade and quantity, ambient temperature, the type of working media, equipment Flow process, structure and manufacturing cost etc..
Heat energy (temperature difference) with absorption heat pump technology as representative utilizes technology, utilizes high-temperature hot load to drive and realizes heat supply or system Cold；Being affected by the character of working media (solution and refrigerant medium), high-temperature hot load often cannot reasonably be applied to absorb In formula heat pump flowsheet, cause its application and range of application by bigger restriction；Also absorption heat pump technology cannot have been given play to cold The advantage that agent steam latent heat is big.
Utilize the compression heat pump technology that the grade between mechanical energy and heat energy is poor, there is certain motility；But in many situations Under, such compression heat pump is difficult to the Appropriate application to heat energy.Meanwhile, two kinds of heat pump techniques also have common weak point Heat energy cannot be realized to machinery transformation of energy heating or freezing simultaneously.
In order to play the technical advantage of absorption heat pump, from the angle significantly promoting Low Temperature Thermal load temperature, for utilization High-temperature hot load carries out heat supply or cooling, and considers take into account power drive or externally provide power demand, and the present invention proposes to comprise pressure The components such as contracting machine, decompressor and high-temperature heat exchanger, by the temperature difference between high temperature heat source and heated medium and cryogen liquid and environment it Between the temperature difference carry out utilizing simultaneously effectively, there is the 5th class thermal drivers compressing-absorbing type heat pump of comprehensive advantage.
Summary of the invention:
Present invention is primarily intended to provide series the 5th class thermal drivers compressing-absorbing type heat pump, concrete summary of the invention subitem illustrates such as Under:
1. the 5th class thermal drivers compressing-absorbing type heat pump, mainly by generator, the second generator, absorber, compressor, swollen Swollen machine, condenser, the second condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, solution heat exchanger, second molten Liquid heat exchanger and high-temperature heat exchanger are formed；Generator has concentrated solution pipeline molten through solution pump, solution heat exchanger and second Liquid heat exchanger and the connection of the second generator, the second generator also has concentrated solution pipeline through the second solution heat exchanger with absorber even Logical, absorber also has weak solution pipeline to connect with generator through solution heat exchanger, and generator also has refrigerant steam channel and condensation Device connect, condenser also has cryogen liquid pipeline to connect with vaporizer through cryogen liquid pump, the second generator also have refrigerant steam channel and Compressor connects, and compressor also has refrigerant steam channel to connect with decompressor through high-temperature heat exchanger, and decompressor also has refrigerant vapour Passage and the connection of the second condenser, after the second condenser also has cryogen liquid pipeline to connect with generator, generator has cryogen liquid pipe again Road connects with vaporizer through choke valve, and vaporizer also has refrigerant steam channel to connect with absorber, and the second generator and high-temperature hot are handed over Parallel operation have the most respectively high temperature thermal medium passage and ft connection, absorber and the second condenser have the most respectively heated medium passage with Ft connection, generator and vaporizer have low-temperature heat medium passage and ft connection the most respectively, and condenser also has coolant guiding channel With ft connection, decompressor connects compressor and transmits power, forms the 5th class thermal drivers compressing-absorbing type heat pump.
2. the 5th class thermal drivers compressing-absorbing type heat pump, mainly by generator, the second generator, absorber, compressor, swollen Swollen machine, condenser, the second condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, solution heat exchanger, second molten Liquid heat exchanger, high-temperature heat exchanger and regenerator are formed；Generator has concentrated solution pipeline through solution pump, solution heat exchanger Connect with the second solution heat exchanger and the second generator, the second generator also have concentrated solution pipeline through the second solution heat exchanger with Absorber connects, and absorber also has weak solution pipeline to connect with generator through solution heat exchanger, and generator also has refrigerant vapour to lead to Road connects with condenser, and condenser also has cryogen liquid pipeline to connect with vaporizer through cryogen liquid pump, and the second generator also has cryogen to steam Vapour passage connects with compressor, and compressor also has refrigerant steam channel to connect with decompressor with high-temperature heat exchanger through regenerator, swollen Swollen machine also has refrigerant steam channel to connect through regenerator and the second condenser, and the second condenser also has cryogen liquid pipeline with generator even After Tong, generator has cryogen liquid pipeline to connect with vaporizer through choke valve again, and vaporizer also has refrigerant steam channel with absorber even Logical, the second generator and high-temperature heat exchanger also have high temperature thermal medium passage and ft connection, absorber and the second condenser also to divide Heated medium passage and ft connection, generator and vaporizer is not had to have low-temperature heat medium passage and ft connection the most respectively, cold Condenser also has coolant guiding channel and ft connection, and decompressor connects compressor and transmits power, and formation the 5th class thermal drivers compression- Absorption heat pump.
3. the 5th class thermal drivers compressing-absorbing type heat pump, mainly by generator, the second generator, absorber, compressor, swollen Swollen machine, condenser, the second condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, solution heat exchanger, second molten Liquid heat exchanger, high-temperature heat exchanger, the second compressor and the second high-temperature heat exchanger are formed；Generator has concentrated solution pipeline Connecting through solution pump, solution heat exchanger and the second solution heat exchanger and the second generator, the second generator also has concentrated solution pipe Road the second solution heat exchanger connects with absorber, and absorber also has weak solution pipeline to connect with generator through solution heat exchanger, Generator also has refrigerant steam channel to connect with condenser, and condenser also has cryogen liquid pipeline to connect with vaporizer through cryogen liquid pump, Second generator also has refrigerant steam channel to connect with compressor, and compressor also has refrigerant steam channel through high-temperature heat exchanger and Two compressor connections, the second compressor also has refrigerant steam channel to connect with decompressor through the second high-temperature heat exchanger, and decompressor is also Have refrigerant steam channel to connect with the second condenser, the second condenser also have cryogen liquid pipeline to connect with generator after generator again Having cryogen liquid pipeline to connect with vaporizer through choke valve, vaporizer also has refrigerant steam channel to connect with absorber, the second generator, High-temperature heat exchanger and the second high-temperature heat exchanger have high temperature thermal medium passage and ft connection, absorber and the second condensation the most respectively Device has heated medium passage and ft connection, generator and vaporizer to have low-temperature heat medium passage to connect with outside the most respectively the most respectively Logical, condenser also has coolant guiding channel and ft connection, and decompressor connects compressor and the second compressor and transmits power, shape Become the 5th class thermal drivers compressing-absorbing type heat pump.
4. the 5th class thermal drivers compressing-absorbing type heat pump, mainly by generator, the second generator, absorber, compressor, swollen Swollen machine, condenser, the second condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, solution heat exchanger, second molten Liquid heat exchanger, high-temperature heat exchanger, the second high-temperature heat exchanger and the second decompressor are formed；Generator has concentrated solution pipeline Connecting through solution pump, solution heat exchanger and the second solution heat exchanger and the second generator, the second generator also has concentrated solution pipe Road the second solution heat exchanger connects with absorber, and absorber also has weak solution pipeline to connect with generator through solution heat exchanger, Generator also has refrigerant steam channel to connect with condenser, and condenser also has cryogen liquid pipeline to connect with vaporizer through cryogen liquid pump, Second generator also has refrigerant steam channel to connect with compressor, and compressor also has refrigerant steam channel through high-temperature heat exchanger and Two decompressor connections, the second decompressor also has refrigerant steam channel to connect with decompressor through the second high-temperature heat exchanger, and decompressor is also Have refrigerant steam channel to connect with the second condenser, the second condenser also have cryogen liquid pipeline to connect with generator after generator again Having cryogen liquid pipeline to connect with vaporizer through choke valve, vaporizer also has refrigerant steam channel to connect with absorber, the second generator, High-temperature heat exchanger and the second high-temperature heat exchanger have high temperature thermal medium passage and ft connection, absorber and the second condensation the most respectively Device has heated medium passage and ft connection, generator and vaporizer to have low-temperature heat medium passage to connect with outside the most respectively the most respectively Logical, condenser also has coolant guiding channel and ft connection, decompressor and the second decompressor connect compressor and transmit power, shape Become the 5th class thermal drivers compressing-absorbing type heat pump.
5. the 5th class thermal drivers compressing-absorbing type heat pump, is at the described arbitrary 5th class thermal drivers compressing-absorbing type of 1-4 item In heat pump, cancel choke valve, generator has cryogen liquid pipeline connect with vaporizer through choke valve and is adjusted to generator and has cryogen liquid Pipeline connects with vaporizer, forms the 5th class thermal drivers compressing-absorbing type heat pump.
6. the 5th class thermal drivers compressing-absorbing type heat pump, is at the described arbitrary 5th class thermal drivers compressing-absorbing type of 1-4 item In heat pump, increase the 3rd generator, second throttle, the second solution pump, the 3rd solution heat exchanger and heater, generator Set up concentrated solution pipeline to connect through the second solution pump, solution heat exchanger and the 3rd solution heat exchanger and the 3rd generator, the 3rd Generator also has concentrated solution pipeline to connect with absorber through the 3rd solution heat exchanger, the second generator is had refrigerant steam channel with Compressor connection is adjusted to the 3rd generator after the second generator has refrigerant steam channel to connect with the 3rd generator cryogen liquid again Pipeline connects with vaporizer with second throttle through heater, generator, and the 3rd generator also has refrigerant steam channel and compressor Connection, heater also has heated medium passage and ft connection, forms the 5th class thermal drivers compressing-absorbing type heat pump.
7. the 5th class thermal drivers compressing-absorbing type heat pump, is at the described arbitrary 5th class thermal drivers compressing-absorbing type of 1-4 item In heat pump, increase the 3rd generator, second throttle, the 3rd solution heat exchanger and heater, generator is had concentrated solution pipe Road is adjusted to generator has concentrated solution pipe through solution pump, solution heat exchanger and the second solution heat exchanger and the connection of the second generator Road connects through solution pump, solution heat exchanger, the second solution heat exchanger and the 3rd solution heat exchanger and the second generator, will Second generator has concentrated solution pipeline to connect with absorber through the second solution heat exchanger to be adjusted to the second generator and have concentrated solution pipeline Connect through the 3rd solution heat exchanger and the 3rd generator, the 3rd generator have again concentrated solution pipeline through the second solution heat exchanger with Absorber connects, and the second generator has refrigerant steam channel connect with compressor and is adjusted to the second generator and has refrigerant steam channel After connecting with the 3rd generator, the 3rd generator has cryogen liquid pipeline again through heater, generator and second throttle and vaporizer Connection, the 3rd generator also has refrigerant steam channel to connect with compressor, and heater also has heated medium passage and ft connection, Form the 5th class thermal drivers compressing-absorbing type heat pump.
8. the 5th class thermal drivers compressing-absorbing type heat pump, is at the described arbitrary 5th class thermal drivers compressing-absorbing type of 1-4 item In heat pump, increase the 3rd generator, second throttle, the second solution pump, the 3rd solution heat exchanger and heater, will occur Device has concentrated solution pipeline to be adjusted to generation through solution pump, solution heat exchanger and the second solution heat exchanger and the connection of the second generator Device has concentrated solution pipeline to connect through solution pump, solution heat exchanger and the second solution heat exchanger and the 3rd generator, and the 3rd occurs Device has concentrated solution pipeline again through the second solution pump and the 3rd solution heat exchanger and the connection of the second generator, has dense by the second generator Solution line connects with absorber through the second solution heat exchanger and is adjusted to the second generator and has concentrated solution pipeline to hand over through the 3rd solution heat Parallel operation and the second solution heat exchanger connect with absorber, have refrigerant steam channel to connect with compressor in the second generator and are adjusted to After second generator has refrigerant steam channel to connect with the 3rd generator, the 3rd generator has cryogen liquid pipeline through heater again, sends out Raw device connects with vaporizer with second throttle, and the 3rd generator also has refrigerant steam channel to connect with compressor, and heater also has Heated medium passage and ft connection, form the 5th class thermal drivers compressing-absorbing type heat pump.
9. the 5th class thermal drivers compressing-absorbing type heat pump, is in the described arbitrary 5th class thermal drivers compressing-absorbing type heat of 6-8 item In pump, the 3rd generator sets up high temperature thermal medium pipeline and ft connection, forms the 5th class thermal drivers compressing-absorbing type heat pump.
10. the 5th class thermal drivers compressing-absorbing type heat pump, is at the described arbitrary 5th class thermal drivers compressing-absorbing type of 6-9 item In heat pump, cancel choke valve and second throttle, generator has cryogen liquid pipeline connect with vaporizer through choke valve and is adjusted to Raw device has cryogen liquid pipeline to connect with vaporizer, generator has cryogen liquid pipeline connect with vaporizer through second throttle and is adjusted to Generator has cryogen liquid pipeline to connect with vaporizer, forms the 5th class thermal drivers compressing-absorbing type heat pump.
11. the 5th class thermal drivers compressing-absorbing type heat pumps, are at the described arbitrary 5th class thermal drivers compressing-absorbing type of 1-4 item In heat pump, increase the 3rd generator, the second solution pump, the 3rd solution heat exchanger and the second absorber, generator is had dense molten Liquid pipeline is adjusted to generator has dense molten through solution pump, solution heat exchanger and the second solution heat exchanger and the connection of the second generator Liquid pipeline connects through solution heat exchanger and the second absorber, and the second absorber has weak solution pipeline again through solution pump and the second solution Heat exchanger and the connection of the second generator, have concentrated solution pipeline to connect with absorber through the second solution heat exchanger in the second generator Being adjusted to the second generator has concentrated solution pipeline to connect through the second solution heat exchanger and the 3rd generator, and the 3rd generator has dense again Solution line connects with absorber through the second solution pump and the 3rd solution heat exchanger, absorber has weak solution pipeline through solution heat Exchanger connects with generator and is adjusted to absorber and has weak solution pipeline through the 3rd solution heat exchanger and solution heat exchanger and generation Device connects, and generator has cryogen liquid pipeline connect with vaporizer through choke valve and is adjusted to generator and has cryogen liquid pipeline through the 3rd Raw device connects with vaporizer with choke valve, and the 3rd generator also has refrigerant steam channel to connect with the second absorber, the second absorber Also have coolant guiding channel and ft connection, form the 5th class thermal drivers compressing-absorbing type heat pump.
12. the 5th class thermal drivers compressing-absorbing type heat pumps, are at the 11st described arbitrary 5th class thermal drivers compressing-absorbing type In heat pump, cancel choke valve, the 3rd generator has cryogen liquid pipeline connect with vaporizer through choke valve and is adjusted to the 3rd generator There is cryogen liquid pipeline to connect with vaporizer, form the 5th class thermal drivers compressing-absorbing type heat pump.
13. the 5th class thermal drivers compressing-absorbing type heat pumps, are at the 11st described arbitrary 5th class thermal drivers compressing-absorbing type In heat pump, increasing the 4th generator, second throttle, the 3rd solution pump, the 4th solution heat exchanger and heater, second inhales Receiving device to set up weak solution pipeline and connect with the 4th generator through the 3rd solution pump and the 4th solution heat exchanger, the 4th generator is also Concentrated solution pipeline connects through the 4th solution heat exchanger and the 3rd generator, and the second generator is had refrigerant steam channel and compressor Connection is adjusted to the 4th generator after the second generator has refrigerant steam channel to connect with the 4th generator cryogen liquid pipeline warp again Heater, generator, the 3rd generator connect with vaporizer with second throttle, the 4th generator also have refrigerant steam channel with Compressor connects, and heater also has heated medium passage and ft connection, forms the 5th class thermal drivers compressing-absorbing type heat pump.
14. the 5th class thermal drivers compressing-absorbing type heat pumps, are at the 11st described arbitrary 5th class thermal drivers compressing-absorbing type In heat pump, increase the 4th generator, second throttle, the 4th solution heat exchanger and heater, the second absorber is had dilute molten Liquid pipeline is adjusted to the second absorber has weak solution pipeline through molten through solution pump and the second solution heat exchanger and the connection of the second generator Liquid pump, the second solution heat exchanger and the 4th solution heat exchanger and the connection of the second generator, have concentrated solution pipe by the second generator Road the second solution heat exchanger and the connection of the 3rd generator are adjusted to the second generator and have concentrated solution pipeline through the 4th solution heat exchange Device and the connection of the 4th generator, the 4th generator has concentrated solution pipeline to connect through the second solution heat exchanger and the 3rd generator again, Second generator has refrigerant steam channel connect with compressor be adjusted to the second generator and have refrigerant steam channel and the 4th generator After connection, the 4th generator has cryogen liquid pipeline again through heater, generator, the 3rd generator and second throttle and vaporizer Connection, the 4th generator also has refrigerant steam channel to connect with compressor, and heater also has heated medium passage and ft connection, Form the 5th class thermal drivers compressing-absorbing type heat pump.
15. the 5th class thermal drivers compressing-absorbing type heat pumps, are at the 11st described arbitrary 5th class thermal drivers compressing-absorbing type In heat pump, increase the 4th generator, second throttle, the 3rd solution pump, the 4th solution heat exchanger and heater, by second Absorber has weak solution pipeline to be adjusted to the second absorber have dilute through solution pump and the second solution heat exchanger and the connection of the second generator Solution line is through solution pump and the second solution heat exchanger and the connection of the 4th generator, and the 4th generator has concentrated solution pipeline again through the Three solution pumps and the 4th solution heat exchanger and the second generator connect, and the second generator have concentrated solution pipeline through the second solution heat Exchanger and the connection of the 3rd generator are adjusted to the second generator has concentrated solution pipeline through the 4th solution heat exchanger and the second solution heat Exchanger and the connection of the 3rd generator, have the second generator refrigerant steam channel to connect with compressor and be adjusted to the second generator and have Refrigerant steam channel connect with the 4th generator after the 4th generator have again cryogen liquid pipeline through heater, generator, the 3rd Raw device connects with vaporizer with second throttle, and the 4th generator also has refrigerant steam channel to connect with compressor, and heater also has Heated medium passage and ft connection, form the 5th class thermal drivers compressing-absorbing type heat pump.
16. the 5th class thermal drivers compressing-absorbing type heat pumps, are in the arbitrary 5th class thermal drivers compression-suction described in 13-15 item In receipts formula heat pump, the 4th generator sets up high temperature thermal medium pipeline and ft connection, forms the 5th class thermal drivers compressing-absorbing type heat Pump.
17. the 5th class thermal drivers compressing-absorbing type heat pumps, are in the arbitrary 5th class thermal drivers compression-suction described in 13-16 item In receipts formula heat pump, cancel choke valve and second throttle, have cryogen liquid pipeline to connect with vaporizer through choke valve in the 3rd generator Being adjusted to the 3rd generator has cryogen liquid pipeline to connect with vaporizer, the 3rd generator is had cryogen liquid pipeline through second throttle with Vaporizer connection is adjusted to the 3rd generator has cryogen liquid pipeline to connect with vaporizer, forms the 5th class thermal drivers compressing-absorbing type heat Pump.
18. the 5th class thermal drivers compressing-absorbing type heat pumps, are at the described arbitrary 5th class thermal drivers compressing-absorbing type of 1-4 item In heat pump, increase the 3rd generator, the second solution pump, the 3rd solution heat exchanger and the second absorber, generator is had dense molten Liquid pipeline connects with generator through solution pump, solution heat exchanger and the second solution heat exchanger and is adjusted to generator and has concentrated solution pipe Road connects through solution pump, solution heat exchanger and the second solution heat exchanger and the second absorber, and the second absorber has weak solution again Second generator, through the second solution pump and the 3rd solution heat exchanger and the connection of the second generator, is had concentrated solution pipeline through the by pipeline Two solution heat exchangers connect with absorber and are adjusted to the second generator and have concentrated solution pipeline through the 3rd solution heat exchanger and the 3rd Raw device connection, the 3rd generator has concentrated solution to connect with absorber through the second solution heat exchanger again, and the 3rd generator also has cryogen Steam channel and the connection of the second absorber, the 3rd generator also has high temperature thermal medium passage and ft connection, and the second absorber also has Heated medium passage and ft connection, form the 5th class thermal drivers compressing-absorbing type heat pump.
19. the 5th class thermal drivers compressing-absorbing type heat pumps, are at the 18th described arbitrary 5th class thermal drivers compressing-absorbing type In heat pump, cancel choke valve, generator has cryogen liquid pipeline connect with vaporizer through choke valve and is adjusted to generator and has cryogen liquid Pipeline connects with vaporizer, forms the 5th class thermal drivers compressing-absorbing type heat pump.
20. the 5th class thermal drivers compressing-absorbing type heat pumps, are at the 18th described arbitrary 5th class thermal drivers compressing-absorbing type In heat pump, increasing the 4th generator, second throttle, the 3rd solution pump, the 4th solution heat exchanger and heater, second inhales Receiving device to set up weak solution pipeline and connect with the 4th generator through the 3rd solution pump and the 4th solution heat exchanger, the 4th generator is also Concentrated solution pipeline connects through the 4th solution heat exchanger and the 3rd generator, and the second generator is had refrigerant steam channel and compressor Connection is adjusted to the 4th generator after the second generator has refrigerant steam channel to connect with the 4th generator cryogen liquid pipeline warp again Heater, generator connect with vaporizer with second throttle, and the 4th generator also has refrigerant steam channel to connect with compressor, Heater also has heated medium passage and ft connection, forms the 5th class thermal drivers compressing-absorbing type heat pump.
21. the 5th class thermal drivers compressing-absorbing type heat pumps, are at the 18th described arbitrary 5th class thermal drivers compressing-absorbing type In heat pump, increase the 4th generator, second throttle, the 4th solution heat exchanger and heater, the second absorber is had dilute molten Liquid pipeline is adjusted to the second absorber has weak solution pipeline through the second solution pump and the 3rd solution heat exchanger and the connection of the second generator Connect through the second solution pump, the 3rd solution heat exchanger and the 4th solution heat exchanger and the second generator, the second generator is had Concentrated solution pipeline is adjusted to the second generator has concentrated solution pipeline molten through the 4th through the 3rd solution heat exchanger and the connection of the 3rd generator Liquid heat exchanger and the connection of the 4th generator, the 4th generator has concentrated solution pipeline again through the 3rd solution heat exchanger and the 3rd generation Device connects, and the second generator has refrigerant steam channel connect with compressor and is adjusted to the second generator and has refrigerant steam channel and the After four generator connections, the 4th generator has cryogen liquid pipeline to connect with vaporizer through heater, generator and second throttle again, 4th generator also has refrigerant steam channel to connect with compressor, and heater also has heated medium passage and ft connection, is formed 5th class thermal drivers compressing-absorbing type heat pump.
22. the 5th class thermal drivers compressing-absorbing type heat pumps, are at the 18th described arbitrary 5th class thermal drivers compressing-absorbing type In heat pump, increase the 4th generator, second throttle, the 3rd solution pump, the 4th solution heat exchanger and heater, by second Absorber has weak solution pipeline to be adjusted to the second absorber through the second solution pump and the 3rd solution heat exchanger and the connection of the second generator Having weak solution pipeline through the second solution pump and the 3rd solution heat exchanger and the connection of the 4th generator, the 4th generator has concentrated solution again Second generator, through the 3rd solution pump and the 4th solution heat exchanger and the connection of the second generator, is had concentrated solution pipeline through the by pipeline Three solution heat exchangers and the connection of the 3rd generator are adjusted to the second generator has concentrated solution pipeline through the 4th solution heat exchanger and the Three solution heat exchangers and the connection of the 3rd generator, have refrigerant steam channel to connect with compressor in the second generator and be adjusted to second After generator has refrigerant steam channel to connect with the 4th generator, the 4th generator has cryogen liquid pipeline again through heater, generator Connecting with vaporizer with second throttle, the 4th generator also has refrigerant steam channel to connect with compressor, and heater is also added Hot media channel and ft connection, form the 5th class thermal drivers compressing-absorbing type heat pump.
23. the 5th class thermal drivers compressing-absorbing type heat pumps, are in the arbitrary 5th class thermal drivers compression-suction described in 20-22 item In receipts formula heat pump, the 4th generator sets up high temperature thermal medium passage and ft connection, forms the 5th class thermal drivers compressing-absorbing type heat Pump.
24. the 5th class thermal drivers compressing-absorbing type heat pumps, are in the arbitrary 5th class thermal drivers compression-suction described in 20-23 item In receipts formula heat pump, cancel choke valve and second throttle, generator has cryogen liquid pipeline connect adjustment with vaporizer through choke valve There is cryogen liquid pipeline to connect with vaporizer for generator, generator has cryogen liquid pipeline connect tune with vaporizer through second throttle Whole have cryogen liquid pipeline to connect with vaporizer for generator, forms the 5th class thermal drivers compressing-absorbing type heat pump.
25. the 5th class thermal drivers compressing-absorbing type heat pumps, are at the 18th described arbitrary 5th class thermal drivers compressing-absorbing type In heat pump, increase the 4th generator, the 3rd solution pump, the 4th solution heat exchanger and the 3rd absorber, generator is had dense molten Liquid pipeline is adjusted to generator has dense molten through solution pump, solution heat exchanger and the second solution heat exchanger and the connection of the second absorber Liquid pipeline connects through solution heat exchanger and the 3rd absorber, and the 3rd absorber has weak solution pipeline again through solution pump and the second solution Heat exchanger and the connection of the second absorber, have concentrated solution pipeline to connect with absorber through the second solution heat exchanger in the 3rd generator Being adjusted to the 3rd generator has concentrated solution pipeline to connect through the second solution heat exchanger and the 4th generator, and the 4th generator has dense again Solution line connects with absorber through the 3rd solution pump and the 4th solution heat exchanger, absorber has weak solution pipeline through solution heat Exchanger connects with generator and is adjusted to absorber and has weak solution pipeline through the 4th solution heat exchanger and solution heat exchanger and generation Device connects, and generator has cryogen liquid pipeline connect with vaporizer through choke valve and is adjusted to generator and has cryogen liquid pipeline through the 4th Raw device connects with vaporizer with choke valve, and the 4th generator also has refrigerant steam channel to connect with the 3rd absorber, the 3rd absorber Also have coolant guiding channel and ft connection, form the 5th class thermal drivers compressing-absorbing type heat pump.
26. the 5th class thermal drivers compressing-absorbing type heat pumps, are at the 25th described arbitrary 5th class thermal drivers compressing-absorbing type In heat pump, cancel choke valve, the 4th generator has cryogen liquid pipeline connect with vaporizer through choke valve and is adjusted to the 4th generator There is cryogen liquid pipeline to connect with vaporizer, form the 5th class thermal drivers compressing-absorbing type heat pump.
27. the 5th class thermal drivers compressing-absorbing type heat pumps, mainly by generator, the second generator, absorber, compressor, Decompressor, condenser, the second condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, solution heat exchanger, second Solution heat exchanger, high-temperature heat exchanger and regenerator are formed；Generator has concentrated solution pipeline through solution pump, solution heat exchange Device and the second solution heat exchanger and the second generator connect, and the second generator also has concentrated solution pipeline through the second solution heat exchanger Connecting with absorber, absorber also has weak solution pipeline to connect with generator through solution heat exchanger, and generator also has refrigerant vapour Passage connects with condenser, and condenser also has cryogen liquid pipeline to connect with vaporizer through cryogen liquid pump, and the second generator also has cryogen Steam channel connects with compressor through regenerator, and compressor also has refrigerant steam channel to connect with decompressor through high-temperature heat exchanger, Decompressor also has refrigerant steam channel to connect through regenerator and the second condenser, and the second condenser also has cryogen liquid pipeline and generator After connection, generator has cryogen liquid pipeline to connect with vaporizer through choke valve again, and vaporizer also has refrigerant steam channel and absorber Connection, the second generator and high-temperature heat exchanger have high temperature thermal medium passage and ft connection, absorber and the second condensation the most respectively Device has heated medium passage and ft connection, generator and vaporizer to have low-temperature heat medium passage to connect with outside the most respectively the most respectively Logical, condenser also has coolant guiding channel and ft connection, and decompressor connects compressor and transmits power, forms the 5th class heat and drives Dynamic pressure contracting-absorption heat pump.
28. the 5th class thermal drivers compressing-absorbing type heat pumps, are at the 27th described 5th class thermal drivers compressing-absorbing type heat pump In, cancel choke valve, generator has cryogen liquid pipeline connect with vaporizer through choke valve and is adjusted to generator and has cryogen liquid pipeline Connect with vaporizer, form the 5th class thermal drivers compressing-absorbing type heat pump.
29. the 5th class thermal drivers compressing-absorbing type heat pumps, are in the described arbitrary 5th class thermal drivers compression of 1-5,27-28 item In-absorption heat pump, cancel or retain the low-temperature heat medium passage of generator and ft connection, increase the 3rd generator, second molten Liquid pump, the 3rd solution heat exchanger and the second absorber, generator is had concentrated solution pipeline through solution pump, solution heat exchanger and Second solution heat exchanger and the connection of the second generator are adjusted to generator has concentrated solution pipeline to absorb through solution heat exchanger and second Device connects, and the second absorber has weak solution pipeline to connect with the second generator through solution pump and the second solution heat exchanger again, by the Two generators have concentrated solution pipeline to connect with absorber through the second solution heat exchanger to be adjusted to two generators and have concentrated solution pipeline through Two solution heat exchangers and the connection of the 3rd generator, the 3rd generator has concentrated solution pipeline again through the second solution pump and the 3rd solution heat Exchanger connects with absorber, absorber has weak solution pipeline connect with generator through solution heat exchanger and is adjusted to absorber and has Weak solution pipeline connects with generator with solution heat exchanger through the 3rd solution heat exchanger, and the 3rd generator also has refrigerant vapour to lead to Road and the connection of the second absorber, the 3rd generator also has low-temperature heat medium passage and ft connection, and the second absorber also cools down Jie Matter passage and ft connection, form the 5th class thermal drivers compressing-absorbing type heat pump.
30. the 5th class thermal drivers compressing-absorbing type heat pumps, are in the arbitrary 5th class thermal drivers compression-suction described in 18-19 item In receipts formula heat pump, cancel or retain the low-temperature heat medium passage of generator and ft connection, increase the 4th generator, the 3rd solution Pump, the 4th solution heat exchanger and the 3rd absorber, have concentrated solution pipeline through solution pump, solution heat exchanger and by generator Two solution heat exchangers and the connection of the second absorber are adjusted to generator and have concentrated solution pipeline through solution heat exchanger and the 3rd absorber Connection, the 3rd absorber has weak solution pipeline to connect with the second absorber through solution pump and the second solution heat exchanger, by the 3rd again Generator has concentrated solution pipeline to connect with absorber through the second solution heat exchanger to be adjusted to the 3rd generator and have concentrated solution pipeline through Two solution heat exchangers and the connection of the 4th generator, the 4th generator has concentrated solution pipeline again through the 3rd solution pump and the 4th solution heat Exchanger connects with absorber, absorber has weak solution pipeline connect with generator through solution heat exchanger and is adjusted to absorber and has Weak solution pipeline connects with generator with solution heat exchanger through the 4th solution heat exchanger, and the 4th generator also has refrigerant vapour to lead to Road and the connection of the 3rd absorber, the 4th generator also has low-temperature heat medium passage and ft connection, and the 3rd absorber also cools down Jie Matter passage and ft connection, form the 5th class thermal drivers compressing-absorbing type heat pump.
31. the 5th class thermal drivers compressing-absorbing type heat pumps, are to compress at the arbitrary first kind thermal drivers described in 1-30 item-inhale In receipts formula heat pump, increasing working machine, decompressor connects working machine and provides power to working machine, and being formed to add externally provides power 5th class thermal drivers compressing-absorbing type heat pump of load.
32. the 5th class thermal drivers compressing-absorbing type heat pumps, are to compress at the arbitrary first kind thermal drivers described in 1-30 item-inhale In receipts formula heat pump, increasing engine, engine connects compressor and provides power to compressor, forms additional external power drive The 5th class thermal drivers compressing-absorbing type heat pump.
Accompanying drawing illustrates:
Fig. 1 is based on the 5th the 1st kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 2 is based on the 5th the 2nd kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 3 is based on the 5th the 3rd kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 4 is based on the 5th the 4th kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 5 is based on the 5th the 5th kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 6 is based on the 5th the 6th kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 7 is based on the 5th the 7th kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 8 is based on the 5th the 8th kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 9 is based on the 5th the 9th kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 10 is based on the 5th the 10th kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 11 is based on the 5th the 11st kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 12 is based on the 5th the 12nd kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 13 is based on the 5th the 13rd kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 14 is based on the 5th the 14th kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 15 is based on the 5th the 15th kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 16 is based on the 5th the 16th kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 17 is based on the 5th the 17th kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 18 is based on the 5th the 18th kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 19 is based on the 5th the 19th kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
In figure, 1-generator, 2-the second generator, 3-absorber, 4-compressor, 5-decompressor, 6-condenser, 7 -the second condenser, 8-vaporizer, 9-choke valve, 10-cryogen liquid pump, 11-solution pump, 12-solution heat exchanger, 13-the second solution heat exchanger, 14-high-temperature heat exchanger, 15-regenerator, 16-the second compressor, 17-the second high temperature Heat exchanger, 18-the second decompressor, 19-the 3rd generator, 20-second throttle, 21-the second solution pump, 22-the 3rd Solution heat exchanger, 23-heater, 24-the second absorber, 25-the 4th generator, 26-the 3rd solution pump, 27-the 4th Solution heat exchanger, 28-the 3rd absorber.
For ease of understanding, be given as described below:
As a example by the 5th class thermal drivers compressing-absorbing type heat pump shown in accompanying drawing 1, the choke valve 9 arranged in cryogen liquid pipeline, available Gravitational pressure drop substitutes；When coolant temperature is relatively low, the cryogen liquid temp flowing through generator 1 can be cooled within vaporizer 8 During evaporating temperature, it is not provided with choke valve 9, and power pressure reduction is used in generator 1 inner heat exchanger pipeline.
Detailed description of the invention:
First be noted that in the statement of structure and flow process, inessential in the case of do not repeat；To obvious stream Cheng Buzuo states.The present invention is described in detail below in conjunction with the accompanying drawings with example.
The 5th class thermal drivers compressing-absorbing type heat pump shown in Fig. 1 is achieved in that
(1), in structure, it is mainly by generator, the second generator, absorber, compressor, decompressor, condenser, second cold Condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, solution heat exchanger, the second solution heat exchanger and high-temperature hot are handed over Parallel operation is formed；Generator 1 has concentrated solution pipeline through solution pump 11, solution heat exchanger 12 and the second solution heat exchanger 13 Connecting with the second generator 2, the second generator 2 also concentrated solution pipeline connects with absorber 3 through the second solution heat exchanger 13, Absorber 3 also weak solution pipeline connects with generator 1 through solution heat exchanger 12, generator 1 also have refrigerant steam channel with Condenser 6 connects, and condenser 6 also cryogen liquid pipeline connects with vaporizer 8 through cryogen liquid pump 10, and the second generator 2 also has Refrigerant steam channel connects with compressor 4, and compressor 4 also has refrigerant steam channel through high-temperature heat exchanger 14 with decompressor 5 even Logical, decompressor 5 also refrigerant steam channel connects with the second condenser 7, and the second condenser 7 also has cryogen liquid pipeline and generation After device 1 connection, generator 1 has cryogen liquid pipeline to connect with vaporizer 8 through choke valve 9 again, and vaporizer 8 also has refrigerant vapour Passage connects with absorber 3, and the second generator 2 and high-temperature heat exchanger 14 have high temperature thermal medium passage and ft connection the most respectively, Absorber 3 and the second condenser 7 have heated medium passage and ft connection, generator 1 and vaporizer 8 also to distinguish the most respectively Having low-temperature heat medium passage and ft connection, condenser 6 to also have coolant guiding channel and ft connection, decompressor 5 connects compression Machine 4 also transmits power.
(2), in flow process, the concentrated solution of generator 1 is entered through solution pump 11, solution heat exchanger 12 and the second solution heat exchanger 13 Entering the second generator 2, high temperature thermal medium flows through the second generator 2, heating enters its interior solution and discharges refrigerant vapour and to compression Machine 4 provides, and the concentrated solution of the second generator 2 enters absorber 3 through the second solution heat exchanger 13, absorbs refrigerant vapour and put Heat is in heated medium, and the weak solution of absorber 3 enters generator 1, cryogen liquid and low-temperature heat medium through solution heat exchanger 12 Flow separately through generator 1, heating enters its interior solution release refrigerant vapour and provides to condenser 6, the cryogen of condenser 6 Steam heat release becomes cryogen liquid in cooling medium, and the cryogen liquid of condenser 6 enters vaporizer 8 through cryogen liquid pump 10 pressurization；Cryogen steams Steam flow heats up through compressor 4 boosting, flows through high-temperature heat exchanger 14 and absorbs heat, and enters decompressor 5 blood pressure lowering work done afterwards；Expand The refrigerant vapour of machine 5 discharge enters the second condenser 7, heat release becomes cryogen liquid, the cryogen of the second condenser 7 in heated medium Liquid stream enters vaporizer 8 through choke valve 9 throttling after generator 1 heat release again；Low-temperature heat medium flow through vaporizer 8, heat into Entering its interior cryogen liquid and become refrigerant vapour, the refrigerant vapour that vaporizer 8 produces is supplied to absorber 3；The merit of decompressor 5 output It is supplied to compressor 4 be used as power, forms the 5th class thermal drivers compressing-absorbing type heat pump.
The 5th class thermal drivers compressing-absorbing type heat pump shown in Fig. 2 is achieved in that
(1), in structure, it is mainly by generator, the second generator, absorber, compressor, decompressor, condenser, second cold Condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, solution heat exchanger, the second solution heat exchanger, high-temperature hot are handed over Parallel operation and regenerator are formed；Generator 1 has concentrated solution pipeline through solution pump 11, solution heat exchanger 12 and the second solution heat Exchanger 13 connects with the second generator 2, and the second generator 2 also has concentrated solution pipeline through the second solution heat exchanger 13 and suction Receiving device 3 to connect, absorber 3 also weak solution pipeline connects with generator 1 through solution heat exchanger 12, and generator 1 is the coldest Agent steam channel connects with condenser 6, and condenser 6 also cryogen liquid pipeline connects with vaporizer 8 through cryogen liquid pump 10, and second Generator 2 also refrigerant steam channel connects with compressor 4, and compressor 4 also has refrigerant steam channel through regenerator 15 and high temperature Heat exchanger 14 connects with decompressor 5, and decompressor 5 also refrigerant steam channel connects with the second condenser 7 through regenerator 15, Second condenser 7 after also cryogen liquid pipeline connects with generator 1 generator 1 have again cryogen liquid pipeline through choke valve 9 with steam Sending out device 8 to connect, vaporizer 8 also refrigerant steam channel connects with absorber 3, the second generator 2 and high-temperature heat exchanger 14 Also having high temperature thermal medium passage and ft connection, absorber 3 and the second condenser 7 have heated medium passage the most respectively with outside Connection, generator 1 and vaporizer 8 have low-temperature heat medium passage and ft connection, condenser 6 to also have cooling medium to lead to the most respectively Road and ft connection, decompressor 5 connects compressor 4 and transmits power.
(2), in flow process, the concentrated solution of generator 1 is entered through solution pump 11, solution heat exchanger 12 and the second solution heat exchanger 13 Entering the second generator 2, high temperature thermal medium flows through the second generator 2, heating enters its interior solution and discharges refrigerant vapour and to compression Machine 4 provides, and the concentrated solution of the second generator 2 enters absorber 3 through the second solution heat exchanger 13, absorbs refrigerant vapour and put Heat is in heated medium, and the weak solution of absorber 3 enters generator 1, cryogen liquid and low-temperature heat medium through solution heat exchanger 12 Flow separately through generator 1, heating enters its interior solution release refrigerant vapour and provides to condenser 6, the cryogen of condenser 6 Steam heat release becomes cryogen liquid in cooling medium, and the cryogen liquid of condenser 6 enters vaporizer 8 through cryogen liquid pump 10 pressurization；Cryogen steams Steam flow heats up through compressor 4 boosting, flows through regenerator 15 and high-temperature heat exchanger 14 successively and progressively absorbs heat, entering swollen afterwards Swollen machine 5 blood pressure lowering work done；The refrigerant vapour of decompressor 5 discharge enters the second condenser 7, heat release after flowing through regenerator 15 heat release Become cryogen liquid in heated medium, the cryogen liquid stream of the second condenser 7 after generator 1 heat release again through choke valve 9 throttle into Enter vaporizer 8；Low-temperature heat medium flows through vaporizer 8, heating enters its interior cryogen liquid and becomes refrigerant vapour, and vaporizer 8 produces Refrigerant vapour is supplied to absorber 3；The merit of decompressor 5 output is supplied to compressor 4 and is used as power, and forms the 5th class thermal drivers pressure Contracting-absorption heat pump.
The 5th class thermal drivers compressing-absorbing type heat pump shown in Fig. 3 is achieved in that
(1), in structure, it is mainly by generator, the second generator, absorber, compressor, decompressor, condenser, second cold Condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, solution heat exchanger, the second solution heat exchanger, high-temperature hot are handed over Parallel operation, the second compressor and the second high-temperature heat exchanger are formed；Generator 1 has concentrated solution pipeline through solution pump 11, solution heat Exchanger 12 connects with the second generator 2 with the second solution heat exchanger 13, and the second generator 2 also has concentrated solution pipeline through the Two solution heat exchangers 13 connect with absorber 3, and absorber 3 also has weak solution pipeline through solution heat exchanger 12 and generator 1 connection, generator 1 also refrigerant steam channel connects with condenser 6, and condenser 6 also has cryogen liquid pipeline through cryogen liquid pump 10 connect with vaporizer 8, and the second generator 2 also refrigerant steam channel connects with compressor 4, and compressor 4 also has cryogen to steam Vapour passage connects with the second compressor 16 through high-temperature heat exchanger 14, and the second compressor 16 also has refrigerant steam channel high through second Temperature heat exchanger 17 connects with decompressor 5, and decompressor 5 also refrigerant steam channel connects with the second condenser 7, the second condensation Device 7 after also cryogen liquid pipeline connects with generator 1 generator 1 have cryogen liquid pipeline through choke valve 9 with vaporizer 8 even again Logical, vaporizer 8 also refrigerant steam channel connects with absorber 3, and the second generator 2, high-temperature heat exchanger 14 and second are high Temperature heat exchanger 17 has high temperature thermal medium passage and ft connection, absorber 3 and the second condenser 7 to have the most respectively to be added the most respectively Hot media channel and ft connection, generator 1 and vaporizer 8 have low-temperature heat medium passage and ft connection, condenser the most respectively 6 also have coolant guiding channel and ft connection, and decompressor 5 connects compressor 4 and the second compressor 16 and transmits power.
(2), in flow process, the concentrated solution of generator 1 is entered through solution pump 11, solution heat exchanger 12 and the second solution heat exchanger 13 Entering the second generator 2, high temperature thermal medium flows through the second generator 2, heating enters its interior solution and discharges refrigerant vapour and to compression Machine 4 provides, and the concentrated solution of the second generator 2 enters absorber 3 through the second solution heat exchanger 13, absorbs refrigerant vapour and put Heat is in heated medium, and the weak solution of absorber 3 enters generator 1, cryogen liquid and low-temperature heat medium through solution heat exchanger 12 Flow separately through generator 1, heating enters its interior solution release refrigerant vapour and provides to condenser 6, the cryogen of condenser 6 Steam heat release becomes cryogen liquid in cooling medium, and the cryogen liquid of condenser 6 enters vaporizer 8 through cryogen liquid pump 10 pressurization；Cryogen steams Steam flow heats up through compressor 4 boosting, flows through high-temperature heat exchanger 14 and absorbs heat, and enters the second compressor 16 boosting afterwards and heats up； The refrigerant vapour of the second compressor 16 discharge flows through the second high-temperature heat exchanger 17 and absorbs heat, and enters decompressor 5 blood pressure lowering afterwards and makees Merit；The refrigerant vapour of decompressor 5 discharge enters the second condenser 7, heat release becomes cryogen liquid, the second condenser 7 in heated medium Cryogen liquid stream after generator 1 heat release again through choke valve 9 throttling enter vaporizer 8；Low-temperature heat medium flow through vaporizer 8, Heating enters its interior cryogen liquid and becomes refrigerant vapour, and the refrigerant vapour that vaporizer 8 produces is supplied to absorber 3；Decompressor 5 is defeated The merit gone out is supplied to compressor 4 and the second compressor 16 is used as power, and forms the 5th class thermal drivers compressing-absorbing type heat pump.
The 5th class thermal drivers compressing-absorbing type heat pump shown in Fig. 4 is achieved in that
(1), in structure, it is mainly by generator, the second generator, absorber, compressor, decompressor, condenser, second cold Condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, solution heat exchanger, the second solution heat exchanger, high-temperature hot are handed over Parallel operation, the second high-temperature heat exchanger and the second decompressor are formed；Generator 1 has concentrated solution pipeline through solution pump 11, solution heat Exchanger 12 connects with the second generator 2 with the second solution heat exchanger 13, and the second generator 2 also has concentrated solution pipeline through the Two solution heat exchangers 13 connect with absorber 3, and absorber 3 also has weak solution pipeline through solution heat exchanger 12 and generator 1 connection, generator 1 also refrigerant steam channel connects with condenser 6, and condenser 6 also has cryogen liquid pipeline through cryogen liquid pump 10 connect with vaporizer 8, and the second generator 2 also refrigerant steam channel connects with compressor 4, and compressor 4 also has cryogen to steam Vapour passage connects with the second decompressor 18 through high-temperature heat exchanger 14, and the second decompressor 18 also has refrigerant steam channel high through second Temperature heat exchanger 17 connects with decompressor 5, and decompressor 5 also refrigerant steam channel connects with the second condenser 7, the second condensation Device 7 after also cryogen liquid pipeline connects with generator 1 generator 1 have cryogen liquid pipeline through choke valve 9 with vaporizer 8 even again Logical, vaporizer 8 also refrigerant steam channel connects with absorber 3, and the second generator 2, high-temperature heat exchanger 14 and second are high Temperature heat exchanger 17 has high temperature thermal medium passage and ft connection, absorber 3 and the second condenser 7 to have the most respectively to be added the most respectively Hot media channel and ft connection, generator 1 and vaporizer 8 have low-temperature heat medium passage and ft connection, condenser the most respectively 6 also have coolant guiding channel and ft connection, and decompressor 5 and the second decompressor 18 connect compressor 4 and transmit power.
(2), in flow process, the concentrated solution of generator 1 is entered through solution pump 11, solution heat exchanger 12 and the second solution heat exchanger 13 Entering the second generator 2, high temperature thermal medium flows through the second generator 2, heating enters its interior solution and discharges refrigerant vapour and to compression Machine 4 provides, and the concentrated solution of the second generator 2 enters absorber 3 through the second solution heat exchanger 13, absorbs refrigerant vapour and put Heat is in heated medium, and the weak solution of absorber 3 enters generator 1, cryogen liquid and low-temperature heat medium through solution heat exchanger 12 Flow separately through generator 1, heating enters its interior solution release refrigerant vapour and provides to condenser 6, the cryogen of condenser 6 Steam heat release becomes cryogen liquid in cooling medium, and the cryogen liquid of condenser 6 enters vaporizer 8 through cryogen liquid pump 10 pressurization；Cryogen steams Steam flow heats up through compressor 4 boosting, flows through high-temperature heat exchanger 14 and absorbs heat, entering the second decompressor 18 blood pressure lowering work done afterwards； The refrigerant vapour of the second decompressor 18 discharge flows through the second high-temperature heat exchanger 17 and absorbs heat, and enters decompressor 5 blood pressure lowering afterwards and makees Merit；The refrigerant vapour of decompressor 5 discharge enters the second condenser 7, heat release becomes cryogen liquid, the second condenser 7 in heated medium Cryogen liquid stream after generator 1 heat release again through choke valve 9 throttling enter vaporizer 8；Low-temperature heat medium flow through vaporizer 8, Heating enters its interior cryogen liquid and becomes refrigerant vapour, and the refrigerant vapour that vaporizer 8 produces is supplied to absorber 3；Decompressor 5 He The merit of the second decompressor 18 output is supplied to compressor 4 and is used as power, and forms the 5th class thermal drivers compressing-absorbing type heat pump.
The 5th class thermal drivers compressing-absorbing type heat pump shown in Fig. 5 is achieved in that
(1) in structure, in the 5th class thermal drivers compressing-absorbing type heat pump shown in Fig. 1, increase the 3rd generator, second throttle, Second solution pump, the 3rd solution heat exchanger and heater, generator 1 sets up concentrated solution pipeline through the second solution pump 21, solution Heat exchanger 12 connects with the 3rd generator 19 with the 3rd solution heat exchanger 22, and the 3rd generator 19 also has concentrated solution pipeline Connect with absorber 3 through the 3rd solution heat exchanger 22, have refrigerant steam channel to connect tune with compressor 4 in second generator 2 Whole is that after the second generator 2 has refrigerant steam channel to connect with the 3rd generator 19, the 3rd generator 19 has cryogen liquid pipeline again Connecting with vaporizer 8 with second throttle 20 through heater 23, generator 1, the 3rd generator 19 also has refrigerant steam channel Connecting with compressor 4, heater 23 also has heated medium passage and ft connection.
(2), in flow process, the refrigerant vapour that the second generator 2 produces is supplied to the 3rd generator 19 and makees to drive thermal medium, generator 1 Part concentrated solution enter the 3rd generator 19 through the second solution pump 21, solution heat exchanger 12 and the 3rd solution heat exchanger 22, Refrigerant vapour flows through the 3rd generator 19, heating enters its interior solution release refrigerant vapour and provides to compressor 4, the 3rd The concentrated solution of raw device 19 enters absorber 3 through the 3rd solution heat exchanger 22；Flow through the refrigerant vapour heat release of the 3rd generator 19 Become after cryogen liquid and flow through heater 23 and generator 1 and progressively heat release successively, after enter steaming through second throttle 20 throttling Send out device 8, form the 5th class thermal drivers compressing-absorbing type heat pump.
The 5th class thermal drivers compressing-absorbing type heat pump shown in Fig. 6 is achieved in that
(1) in structure, in the 5th class thermal drivers compressing-absorbing type heat pump shown in Fig. 1, increase the 3rd generator, second throttle, 3rd solution heat exchanger and heater, has concentrated solution pipeline through solution pump 11, solution heat exchanger 12 and by generator 1 Two solution heat exchangers 13 connect with the second generator 2 be adjusted to generator 1 have concentrated solution pipeline through solution pump 11, solution heat Exchanger the 12, second solution heat exchanger 13 connects with the second generator 2 with the 3rd solution heat exchanger 22, occurs second Device 2 has concentrated solution pipeline to connect with absorber 3 through the second solution heat exchanger 13 to be adjusted to the second generator 2 and have concentrated solution pipeline Connecting with the 3rd generator 19 through the 3rd solution heat exchanger 22, the 3rd generator 19 has concentrated solution pipeline again through the second solution heat Exchanger 13 connects with absorber 3, has refrigerant steam channel to connect with compressor 4 in second generator 2 and is adjusted to the second generation Device 2 have refrigerant steam channel to connect with the 3rd generator 19 after the 3rd generator 19 have again cryogen liquid pipeline through heater 23, Generator 1 connects with vaporizer 8 with second throttle 20, and the 3rd generator 19 also has refrigerant steam channel with compressor 4 even Logical, heater 23 also has heated medium passage and ft connection.
(2), in flow process, the refrigerant vapour that the second generator 2 produces is supplied to the 3rd generator 19 and makees to drive thermal medium, generator 1 Concentrated solution enter through solution pump 11, solution heat exchanger the 12, second solution heat exchanger 13 and the 3rd solution heat exchanger 22 Second generator 2, the concentrated solution of the second generator 2 enters the 3rd generator 19, refrigerant vapour through the 3rd solution heat exchanger 22 Flow through the 3rd generator 19, heating enters its interior solution release refrigerant vapour and provides to compressor 4, the 3rd generator 19 Concentrated solution enter absorber 3 through the second solution heat exchanger 13；The refrigerant vapour heat release flowing through the 3rd generator 19 becomes cryogen Flow through heater 23 and generator 1 progressively heat release after liquid successively, after through second throttle 20 throttling enter vaporizer 8, Form the 5th class thermal drivers compressing-absorbing type heat pump.
The 5th class thermal drivers compressing-absorbing type heat pump shown in Fig. 7 is achieved in that
(1) in structure, in the 5th class thermal drivers compressing-absorbing type heat pump shown in Fig. 1, increase the 3rd generator, second throttle, Second solution pump, the 3rd solution heat exchanger and heater, have concentrated solution pipeline to hand over through solution pump 11, solution heat by generator 1 Parallel operation 12 and the second solution heat exchanger 13 connect with the second generator 2 and are adjusted to generator 1 and have concentrated solution pipeline through solution pump 11, solution heat exchanger 12 connects with the 3rd generator 19 with the second solution heat exchanger 13, and the 3rd generator 19 has dense again Solution line connects with the second generator 2 with the 3rd solution heat exchanger 22 through the second solution pump 21, is had by the second generator 2 Concentrated solution pipeline connects with absorber 3 through the second solution heat exchanger 13 and is adjusted to the second generator 2 and has concentrated solution pipeline through the 3rd Solution heat exchanger 22 connects with absorber 3 with the second solution heat exchanger 13, and the second generator 2 is had refrigerant steam channel Connect with compressor 4 and be adjusted to the 3rd generator after the second generator 2 has refrigerant steam channel to connect with the 3rd generator 19 19 have cryogen liquid pipeline to connect with vaporizer 8 with second throttle 20 through heater 23, generator 1 again, the 3rd generator 19 Also having refrigerant steam channel to connect with compressor 4, heater 23 also has heated medium passage and ft connection.
(2), in flow process, the refrigerant vapour that the second generator 2 produces is supplied to the 3rd generator 19 and makees to drive thermal medium, generator 1 Concentrated solution enter the 3rd generator 19 through solution pump 11, solution heat exchanger 12 and the second solution heat exchanger 13, cryogen steams Steam flow enters its interior solution release refrigerant vapour through the 3rd generator 19, heating and provides to compressor 4, the 3rd generator 19 Concentrated solution enter the second generator 2 through the second solution pump 21 and the 3rd solution heat exchanger 22, the second generator 2 dense molten Liquid enters absorber 3 through the 3rd solution heat exchanger 22 and the second solution heat exchanger 13；Flow through the cryogen of the 3rd generator 19 Steam heat release flows through heater 23 and generator 1 progressively heat release successively after becoming cryogen liquid, after save through second throttle 20 Stream enters vaporizer 8, forms the 5th class thermal drivers compressing-absorbing type heat pump.
The 5th class thermal drivers compressing-absorbing type heat pump shown in Fig. 8 is achieved in that
(1) in structure, in the 5th class thermal drivers compressing-absorbing type heat pump shown in Fig. 1, increase the 3rd generator, the second solution pump, 3rd solution heat exchanger and the second absorber, have concentrated solution pipeline through solution pump 11, solution heat exchanger 12 by generator 1 Connect with the second generator 2 with the second solution heat exchanger 13 and be adjusted to generator 1 and have concentrated solution pipeline through solution heat exchanger 12 connect with the second absorber 24, and the second absorber 24 has weak solution pipeline again through solution pump 11 and the second solution heat exchanger 13 connect with the second generator 2, the second generator 2 have concentrated solution pipeline through the second solution heat exchanger 13 and absorber 3 Connection is adjusted to the second generator 2 has concentrated solution pipeline to connect with the 3rd generator 19 through the second solution heat exchanger 13, and the 3rd Generator 19 has concentrated solution pipeline to connect with absorber 3 with the 3rd solution heat exchanger 22 through the second solution pump 21 again, will absorb Device 3 has weak solution pipeline to connect with generator 1 through solution heat exchanger 12 to be adjusted to absorber 3 and have weak solution pipeline molten through the 3rd Liquid heat exchanger 22 connects with generator 1 with solution heat exchanger 12, generator 1 is had cryogen liquid pipeline through choke valve 9 with Vaporizer 8 connection is adjusted to generator 1 has cryogen liquid pipeline to connect with vaporizer 8 with choke valve 9 through the 3rd generator 19, the Three generator 19 also refrigerant steam channel connect with the second absorber 24, and the second absorber 24 also has coolant guiding channel with outer Portion connects.
(2), in flow process, the concentrated solution of generator 1 enters the second absorber 24 through solution heat exchanger 12, absorbs refrigerant vapour also Heat release enters the second generation in cooling medium, the weak solution of the second absorber 24 through solution pump 11 and the second solution heat exchanger 13 Device 2, the concentrated solution of the second generator 2 enters the 3rd generator 19, heat absorption release refrigerant vapour through the second solution heat exchanger 13 And provide to the second absorber 24, the concentrated solution of the 3rd generator 19 is through the second solution pump 21 and the 3rd solution heat exchanger 22 Entering absorber 3, the weak solution of absorber 3 enters generator 1 through the 3rd solution heat exchanger 22 and solution heat exchanger 12； The cryogen liquid of the second condenser 7 flows through generator 1 and the 3rd generator 19 progressively heat release successively, throttles through choke valve 9 afterwards Enter vaporizer 8, form the 5th class thermal drivers compressing-absorbing type heat pump.
The 5th class thermal drivers compressing-absorbing type heat pump shown in Fig. 9 is achieved in that
(1) in structure, in the 5th class thermal drivers compressing-absorbing type heat pump shown in Fig. 8, increase the 4th generator, second throttle, 3rd solution pump, the 4th solution heat exchanger and heater, the second absorber 24 sets up weak solution pipeline through the 3rd solution pump 26 Connecting with the 4th generator 25 with the 4th solution heat exchanger 27, the 4th generator 25 also has concentrated solution pipeline through the 4th solution heat Exchanger 27 connects with the 3rd generator 19, the second generator 2 has refrigerant steam channel connect with compressor 4 and is adjusted to After two generators 2 have refrigerant steam channel to connect with the 4th generator 25, the 4th generator 25 has cryogen liquid pipeline again through heat supply Device 23, generator the 1, the 3rd generator 19 connect with vaporizer 8 with second throttle 20, and the 4th generator 25 also has cryogen Steam channel connects with compressor 4, and heater 23 also has heated medium passage and ft connection.
(2), in flow process, the second generator produces the refrigerant vapour of 2 and is supplied to the 4th generator 25 work driving thermal medium, and second absorbs The part weak solution of device 24 enters the 4th generator 25 through the 3rd solution pump 26 and the 4th solution heat exchanger 27, refrigerant vapour Flow through the 4th generator 25, heating enters its interior solution release refrigerant vapour and provides to compressor 4, the 4th generator 25 Concentrated solution enter the 3rd generator 19 through the 4th solution heat exchanger 27；The refrigerant vapour heat release flowing through the 4th generator 25 becomes Flow through heater 23, generator 1 and the 3rd generator 19 progressively heat release after cryogen liquid successively, after through second throttle 20 throttlings enter vaporizer 8, form the 5th class thermal drivers compressing-absorbing type heat pump.
The 5th class thermal drivers compressing-absorbing type heat pump shown in Figure 10 is achieved in that
(1) in structure, in the 5th class thermal drivers compressing-absorbing type heat pump shown in Fig. 8, increase the 4th generator, second throttle, 4th solution heat exchanger and heater, has weak solution pipeline through solution pump 11 and the second solution heat exchange by the second absorber 24 Device 13 connects with the second generator 2 and is adjusted to the second absorber 24 and has weak solution pipeline through the 11, the second solution heat exchange of solution pump Device 13 connects with the second generator 2 with the 4th solution heat exchanger 27, has concentrated solution pipeline molten through second in second generator 2 Liquid heat exchanger 13 connects with the 3rd generator 19 and is adjusted to the second generator 2 and has concentrated solution pipeline through the 4th solution heat exchanger 27 connect with the 4th generator 25, and the 4th generator 25 has concentrated solution pipeline again through the second solution heat exchanger 13 and the 3rd Raw device 19 connects, and the second generator 2 has refrigerant steam channel connect with compressor 4 and is adjusted to the second generator 2 and has cryogen to steam After vapour passage and the connection of the 4th generator 25 the 4th generator 25 have again cryogen liquid pipeline through heater 23, generator 1, the Three generators 19 connect with vaporizer 8 with second throttle 20, and the 4th generator 25 also has refrigerant steam channel and compressor 4 Connection, heater 23 also has heated medium passage and ft connection.
(2), in flow process, the second generator produces the refrigerant vapour of 2 and is supplied to the 4th generator 25 work driving thermal medium, and second absorbs The weak solution of device 24 enters the second generator 2 through solution pump the 11, second solution heat exchanger 13 and the 4th solution heat exchanger 27, The concentrated solution of the second generator 2 enters the 4th generator 25 through the 4th solution heat exchanger 27, and refrigerant vapour flows through the 4th generation Device 25, heating enter its interior solution release refrigerant vapour and also provide to compressor 4, and the concentrated solution of the 4th generator 25 is through the Two solution heat exchangers 13 enter the 3rd generator 19；Flow through after the refrigerant vapour heat release of the 4th generator 25 becomes cryogen liquid and depend on Secondary flow through heater 23, generator 1 and the 3rd generator 19 progressively heat release, after enter through second throttle 20 throttling and to steam Send out device 8, form the 5th class thermal drivers compressing-absorbing type heat pump.
The 5th class thermal drivers compressing-absorbing type heat pump shown in Figure 11 is achieved in that
(1) in structure, in the 5th class thermal drivers compressing-absorbing type heat pump shown in Fig. 8, increase the 4th generator, second throttle, 3rd solution pump, the 4th solution heat exchanger and heater, have weak solution pipeline through solution pump 11 and by the second absorber 24 Two solution heat exchangers 13 connect with the second generator 2 and are adjusted to the second absorber 24 and have weak solution pipeline through solution pump 11 and Two solution heat exchangers 13 connect with the 4th generator 25, and the 4th generator 25 has concentrated solution pipeline again through the 3rd solution pump 26 Connect with the second generator 2 with the 4th solution heat exchanger 27, have concentrated solution pipeline to hand over through the second solution heat in the second generator 2 Parallel operation 13 connects with the 3rd generator 19 and is adjusted to the second generator 2 and has concentrated solution pipeline through the 4th solution heat exchanger 27 and Two solution heat exchangers 13 connect with the 3rd generator 19, have refrigerant steam channel to connect with compressor 4 in second generator 2 It is adjusted to the 4th generator 25 after the second generator 2 has refrigerant steam channel to connect with the 4th generator 25 and has cryogen liquid pipe again Road connects with vaporizer 8 with second throttle 20 through heater 23, generator the 1, the 3rd generator 19, the 4th generator 25 Also having refrigerant steam channel to connect with compressor 4, heater 23 also has heated medium passage and ft connection.
(2), in flow process, the second generator produces the refrigerant vapour of 2 and is supplied to the 4th generator 25 work driving thermal medium, and second absorbs The weak solution of device 24 enters the 4th generator 25 through solution pump 11 and the second solution heat exchanger 13, and refrigerant vapour flows through the 4th Generator 25, heating enter its interior solution release refrigerant vapour and provide to compressor 4, the concentrated solution of the 4th generator 25 Entering the second generator 2 through the 3rd solution pump 26 and the 4th solution heat exchanger 27, the concentrated solution of the second generator 2 is through the 4th Solution heat exchanger 27 and the second solution heat exchanger 13 enter the 3rd generator 19；The cryogen flowing through the 4th generator 25 steams Vapour heat release flows through heater 23, generator 1 and the 3rd generator 19 progressively heat release successively after becoming cryogen liquid, after through Two choke valve 20 throttlings enter vaporizer 8, form the 5th class thermal drivers compressing-absorbing type heat pump.
The 5th class thermal drivers compressing-absorbing type heat pump shown in Figure 12 is achieved in that
(1) in structure, in the 5th class thermal drivers compressing-absorbing type heat pump shown in Fig. 1, increase the 3rd generator, the second solution pump, 3rd solution heat exchanger and the second absorber, have concentrated solution pipeline through solution pump 11, solution heat exchanger 12 by generator 1 Connect with generator 2 with the second solution heat exchanger 13 and be adjusted to generator 1 and have concentrated solution pipeline through solution pump 11, solution heat Exchanger 12 connects with the second absorber 24 with the second solution heat exchanger 13, and the second absorber 24 has weak solution pipeline warp again Second solution pump 21 connects with the second generator 2 with the 3rd solution heat exchanger 22, and the second generator 2 is had concentrated solution pipeline Connect with absorber 3 through the second solution heat exchanger 13 and be adjusted to the second generator 2 and have concentrated solution pipeline through the 3rd solution heat exchange Device 22 connects with the 3rd generator 19, and the 3rd generator 19 has concentrated solution again through the second solution heat exchanger 13 and absorber 3 Connection, the 3rd generator 19 also refrigerant steam channel connects with the second absorber 24, and the 3rd generator 19 also has high-temperature hot to be situated between Matter passage and ft connection, the second absorber 24 also has heated medium passage and ft connection.
(2), in flow process, the concentrated solution of generator 1 is entered through solution pump 11, solution heat exchanger 12 and the 3rd solution heat exchanger 22 Entering the second absorber 24, absorb refrigerant vapour heat release in heated medium, the weak solution of the second absorber 24 is through the second solution Pump 21 and the second solution heat exchanger 13 enter the second generator 2, and the concentrated solution of the second generator 2 is through the second solution heat exchange Device 13 enters the 3rd generator 19, and high temperature thermal medium flows through the 3rd generator 19, heating enters its interior solution release cryogen and steams Vapour also provides to the second absorber 24, and the concentrated solution of the 3rd generator 19 enters absorber 3 through the 3rd solution heat exchanger 22, Form the 5th class thermal drivers compressing-absorbing type heat pump.
The 5th class thermal drivers compressing-absorbing type heat pump shown in Figure 13 is achieved in that
(1) in structure, in the 5th class thermal drivers compressing-absorbing type heat pump shown in Figure 12, the 4th generator, the second throttling are increased Valve, the 3rd solution pump, the 4th solution heat exchanger and heater, the second absorber 24 sets up weak solution pipeline through the 3rd solution pump 26 connect with the 4th generator 25 with the 4th solution heat exchanger 27, and the 4th generator 25 also has concentrated solution pipeline molten through the 4th Liquid heat exchanger 27 connects with the 3rd generator 19, has refrigerant steam channel to connect adjustment with compressor 4 in second generator 2 It is that after the second generator 2 has refrigerant steam channel to connect with the 4th generator 25, the 4th generator 25 has cryogen liquid pipeline warp again Heater 23, generator 1 connect with vaporizer 8 with second throttle 20, the 4th generator 25 also have refrigerant steam channel with Compressor 4 connects, and heater 23 also has heated medium passage and ft connection.
(2), in flow process, the refrigerant vapour that the second generator 2 produces is supplied to the 4th generator 25 and makees to drive thermal medium, and second absorbs The part weak solution of device 24 enters the 4th generator 25 through the 3rd solution pump 26 and the 4th solution heat exchanger 27, refrigerant vapour Flow through the 4th generator 25, heating enters its interior solution release refrigerant vapour and provides to compressor 4, the 4th generator 25 Concentrated solution enter the 3rd generator 19 through the 4th solution heat exchanger 27；The refrigerant vapour heat release flowing through the 4th generator 25 becomes Flow through heater 23 and generator 1 progressively heat release after cryogen liquid successively, after through second throttle 20 throttling enter evaporation Device 8, forms the 5th class thermal drivers compressing-absorbing type heat pump.
The 5th class thermal drivers compressing-absorbing type heat pump shown in Figure 14 is achieved in that
(1) in structure, in the 5th class thermal drivers compressing-absorbing type heat pump shown in Figure 12, the 4th generator, the second throttling are increased Valve, the 4th solution heat exchanger and heater, have weak solution pipeline molten through the second solution pump 21 and the 3rd by the second absorber 24 Liquid heat exchanger 22 connect with the second generator 2 be adjusted to the second absorber 24 have weak solution pipeline through the second solution pump 21, Three solution heat exchangers 22 connect with the second generator 2 with the 4th solution heat exchanger 27, and the second generator 2 is had concentrated solution Pipeline connects with the 3rd generator 19 through the 3rd solution heat exchanger 22 and is adjusted to the second generator 2 and has concentrated solution pipeline through the 4th Solution heat exchanger 27 connects with the 4th generator 25, and the 4th generator 25 has concentrated solution pipeline again through the 3rd solution heat exchanger 22 connect with the 3rd generator 19, have refrigerant steam channel to connect with compressor 4 in second generator 2 and are adjusted to the second generation Device 2 have refrigerant steam channel to connect with the 4th generator 25 after the 4th generator 25 have again cryogen liquid pipeline through heater 23, Generator 1 connects with vaporizer 8 with second throttle 20, and the 4th generator 25 also has refrigerant steam channel with compressor 4 even Logical, the 4th generator 25 also has high temperature thermal medium passage and ft connection, heater 23 to also have heated medium passage with outside Connection.
(2), in flow process, the refrigerant vapour that high temperature thermal medium and the second generator 2 produce provides to the 4th generator 25 and drives thermic load, The weak solution of the second absorber 24 is entered through the second solution pump the 21, the 3rd solution heat exchanger 22 and the 4th solution heat exchanger 27 Entering the second generator 2, the concentrated solution of the second generator 2 enters the 4th generator 25 through the 4th solution heat exchanger 27, and cryogen steams Vapour and high temperature thermal medium flow separately through the 4th generator 25, heating enters its interior solution release refrigerant vapour and carries to compressor 4 Confession, the concentrated solution of the 4th generator 25 enters the 3rd generator 19 through the 3rd solution heat exchanger 22；Flow through the 4th generator 25 Refrigerant vapour heat release become cryogen liquid after flow through heater 23 and generator 1 progressively heat release successively, after through second throttle 20 throttlings enter vaporizer 8, form the 5th class thermal drivers compressing-absorbing type heat pump.
The 5th class thermal drivers compressing-absorbing type heat pump shown in Figure 15 is achieved in that
(1) in structure, in the 5th class thermal drivers compressing-absorbing type heat pump shown in Figure 12, the 4th generator, the second throttling are increased Valve, the 3rd solution pump, the 4th solution heat exchanger and heater, have weak solution pipeline through the second solution pump by the second absorber 24 21 connect with the second generator 2 with the 3rd solution heat exchanger 22 and to be adjusted to the second absorber 24 and have weak solution pipeline molten through second Liquid pump 21 connects with the 4th generator 25 with the 3rd solution heat exchanger 22, and the 4th generator 25 has concentrated solution pipeline again through Three solution pumps 26 connect with the second generator 2 with the 4th solution heat exchanger 27, and the second generator 2 is had concentrated solution pipeline warp 3rd solution heat exchanger 22 connect with the 3rd generator 19 be adjusted to the second generator 2 have concentrated solution pipeline through the 4th solution heat Exchanger 27 connects with the 3rd generator 19 with the 3rd solution heat exchanger 22, the second generator 2 is had refrigerant steam channel with Compressor 4 connection is adjusted to the 4th generator 25 after the second generator 2 has refrigerant steam channel to connect with the 4th generator 25 Having cryogen liquid pipeline to connect with vaporizer 8 with second throttle 20 through heater 23, generator 1 again, the 4th generator 25 is also Having refrigerant steam channel to connect with compressor 4, heater 23 also has heated medium passage and ft connection.
(2), in flow process, the refrigerant vapour that the second generator 2 produces is supplied to the 4th generator 25 and makees to drive thermal medium, and second absorbs The weak solution of device 24 enters the 4th generator 25 through the second solution pump 21 and the 3rd solution heat exchanger 22, and refrigerant vapour flows through 4th generator 25, heating enter its interior solution release refrigerant vapour and also provide to compressor 4, the 4th generator 25 dense Solution enters the second generator 2 through the 3rd solution pump 26 and the 4th solution heat exchanger 27, the concentrated solution warp of the second generator 2 4th solution heat exchanger 27 and the second solution heat exchanger 13 enter the 3rd generator 19；Flow through the cold of the 4th generator 25 Agent steam heat release flows through heater 23 and generator 1 progressively heat release successively after becoming cryogen liquid, after through second throttle 20 Throttling enters vaporizer 8, forms the 5th class thermal drivers compressing-absorbing type heat pump.
The 5th class thermal drivers compressing-absorbing type heat pump shown in Figure 16 is achieved in that
(1) in structure, in the 5th class thermal drivers compressing-absorbing type heat pump shown in Figure 12, the 4th generator, the 3rd solution are increased Pump, the 4th solution heat exchanger and the 3rd absorber, have concentrated solution pipeline through solution pump 11, solution heat exchanger by generator 1 12 connect with the second absorber 24 with the second solution heat exchanger 13 and to be adjusted to generator 1 and have concentrated solution pipeline through solution heat exchange Device 12 connects with the 3rd absorber 28, and the 3rd absorber 28 has weak solution pipeline again through solution pump 11 and the second solution heat exchange Device 13 connects with the second absorber 24, the 3rd generator 19 has concentrated solution pipeline through the second solution heat exchanger 13 and absorption Device 3 connection is adjusted to the 3rd generator 19 has concentrated solution pipeline to connect with the 4th generator 25 through the second solution heat exchanger 13, 4th generator 25 has concentrated solution pipeline to connect with absorber 3 with the 4th solution heat exchanger 27 through the 3rd solution pump 26 again, will Absorber 3 has weak solution pipeline to connect with generator 1 through solution heat exchanger 12 to be adjusted to absorber 3 and have weak solution pipeline through Four solution heat exchangers 27 connect with generator 1 with solution heat exchanger 12, and generator 1 is had cryogen liquid pipeline through choke valve 9 connect with vaporizer 8 and to be adjusted to generator 1 and have cryogen liquid pipeline to connect with vaporizer 8 through the 4th generator 25 and choke valve 9, 4th generator 25 also refrigerant steam channel connects with the 3rd absorber 28, the 3rd absorber 28 also have coolant guiding channel with Ft connection.
(2), in flow process, the concentrated solution of generator 1 enters the 3rd absorber 28 through solution heat exchanger 12, absorbs refrigerant vapour also Heat release enters the second absorption in cooling medium, the weak solution of the 3rd absorber 28 through solution pump 11 and the second solution heat exchanger 13 Device 24；The concentrated solution of the 3rd generator 19 enters the 4th generator 25 through the second solution heat exchanger 13, heat absorption release cryogen steams Vapour also provides to the 3rd absorber 28, and the concentrated solution of the 4th generator 25 is through the 3rd solution pump 26 and the 4th solution heat exchanger 27 enter absorber 3, and the weak solution of absorber 3 enters generator through the 4th solution heat exchanger 27 and solution heat exchanger 12 1；The cryogen liquid of the second condenser 7 flows through generator 1 and the 4th generator 25 progressively heat release successively, afterwards through choke valve 9 Throttling enters vaporizer 8, forms the 5th class thermal drivers compressing-absorbing type heat pump.
The 5th class absorption heat pump shown in Figure 17 is achieved in that
(1), in structure, it is mainly by generator, the second generator, absorber, compressor, decompressor, condenser, second cold Condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, solution heat exchanger, the second solution heat exchanger, high-temperature hot are handed over Parallel operation and regenerator are formed；Generator 1 has concentrated solution pipeline through solution pump 11, solution heat exchanger 12 and the second solution heat Exchanger 13 connects with the second generator 2, and the second generator 2 also has concentrated solution pipeline through the second solution heat exchanger 13 and suction Receiving device 3 to connect, absorber 3 also weak solution pipeline connects with generator 1 through solution heat exchanger 12, and generator 1 is the coldest Agent steam channel connects with condenser 6, and condenser 6 also cryogen liquid pipeline connects with vaporizer 8 through cryogen liquid pump 10, and second Generator 2 also refrigerant steam channel connects with compressor 4 through regenerator 15, and compressor 4 also has refrigerant steam channel through high temperature Heat exchanger 14 connects with decompressor 5, and decompressor 5 also refrigerant steam channel connects with the second condenser 7 through regenerator 15, Second condenser 7 after also cryogen liquid pipeline connects with generator 1 generator 1 have again cryogen liquid pipeline through choke valve 9 with steam Sending out device 8 to connect, vaporizer 8 also refrigerant steam channel connects with absorber 3, the second generator 2 and high-temperature heat exchanger 14 Have the most respectively high temperature thermal medium passage and ft connection, absorber 3 and the second condenser 7 have the most respectively heated medium passage with Ft connection, generator 1 and vaporizer 8 have low-temperature heat medium passage and ft connection, condenser 6 also to cool down Jie the most respectively Matter passage and ft connection, decompressor 5 connects compressor 4 and transmits power.
(2), in flow process, the concentrated solution of generator 1 is entered through solution pump 11, solution heat exchanger 12 and the second solution heat exchanger 13 Entering the second generator 2, high temperature thermal medium flows through the second generator 2, heating enters its interior solution and discharges refrigerant vapour and to compression Machine 4 provides, and the concentrated solution of the second generator 2 enters absorber 3 through the second solution heat exchanger 13, absorbs refrigerant vapour and put Heat is in heated medium, and the weak solution of absorber 3 enters generator 1, cryogen liquid and low-temperature heat medium through solution heat exchanger 12 Flow separately through generator 1, heating enters its interior solution release refrigerant vapour and provides to condenser 6, the cryogen of condenser 6 Steam heat release becomes cryogen liquid in cooling medium, and the cryogen liquid of condenser 6 enters vaporizer 8 through cryogen liquid pump 10 pressurization；Cryogen steams Steam flow is through regenerator 15 and absorbs heat, and enters compressor 4 boosting afterwards and heats up；The refrigerant vapour of compressor 4 discharge flows through high-temperature hot Exchanger 14 also absorbs heat, and enters decompressor 5 blood pressure lowering work done afterwards；The refrigerant vapour of decompressor 5 discharge flows through regenerator 15 and puts Enter the second condenser 7 after heat, heat release becomes cryogen liquid in heated medium, and the cryogen liquid stream of the second condenser 7 is through generator 1 Vaporizer 8 is entered through choke valve 9 throttling again after heat release；Low-temperature heat medium flows through vaporizer 8, heating enters its interior cryogen liquid Becoming refrigerant vapour, the refrigerant vapour that vaporizer 8 produces is supplied to absorber 3；The merit of decompressor 5 output is supplied to compressor 4 It is used as power, forms the 5th class thermal drivers compressing-absorbing type heat pump.
The 5th class thermal drivers compressing-absorbing type heat pump shown in Figure 18 is achieved in that
(1) in structure, in the 5th class thermal drivers compressing-absorbing type heat pump shown in Fig. 1, cancellation generator 1 is low with ft connection Warm passage, increases the 3rd generator, the second solution pump, the 3rd solution heat exchanger and the second absorber, by generator 1 has concentrated solution pipeline to connect with the second generator 2 with the second solution heat exchanger 13 through solution pump 11, solution heat exchanger 12 Being adjusted to generator 1 has concentrated solution pipeline to connect with the second absorber 24 through solution heat exchanger 12, and the second absorber 24 has again Weak solution pipeline connects with the second generator 2 with the second solution heat exchanger 13 through solution pump 11, has dense by the second generator 2 Solution line connects with absorber 3 through the second solution heat exchanger 13 and is adjusted to two generators 2 and has concentrated solution pipeline through the second solution Heat exchanger 13 connects with the 3rd generator 19, and the 3rd generator 19 has concentrated solution pipeline again through the second solution pump 21 and the 3rd Solution heat exchanger 22 connects with absorber 3, absorber 3 has weak solution pipeline through solution heat exchanger 12 and generator 1 Connection is adjusted to absorber 3 has weak solution pipeline to connect with generator 1 through the 3rd solution heat exchanger 22 and solution heat exchanger 12 Logical, the 3rd generator 19 also refrigerant steam channel connects with the second absorber 24, and the 3rd generator 19 also has low-temperature heat medium Passage and ft connection, the second absorber 24 also has coolant guiding channel and ft connection.
(2), in flow process, the concentrated solution of generator 1 enters the second absorber 24 through solution heat exchanger 12, absorbs refrigerant vapour also Heat release enters the second generation in cooling medium, the weak solution of the second absorber 24 through solution pump 11 and the second solution heat exchanger 13 Device 2, the concentrated solution of the second generator 2 enters the 3rd generator 19 through the second solution heat exchanger 13, and low-temperature heat medium flows through Three generators 19, heating enter its interior solution release refrigerant vapour and provide to the second absorber 24, the 3rd generator 19 Concentrated solution enters absorber 3 through the second solution pump 21 and the 3rd solution heat exchanger 22, and the weak solution of absorber 3 is molten through the 3rd Liquid heat exchanger 22 and solution heat exchanger 12 enter generator 1, form the 5th class thermal drivers compressing-absorbing type heat pump.
The 5th class thermal drivers compressing-absorbing type heat pump shown in Figure 19 is achieved in that
(1) in structure, in the 5th class thermal drivers compressing-absorbing type heat pump shown in Figure 12, cancel or retain generator 1 with outside The low-temperature heat medium passage of connection, increases the 4th generator, the 3rd solution pump, the 4th solution heat exchanger and the 3rd absorber, Generator 1 have concentrated solution pipeline absorb through solution pump 11, solution heat exchanger 12 and the second solution heat exchanger 13 and second Device 24 connection is adjusted to generator 1 has concentrated solution pipeline to connect with the 3rd absorber 28 through solution heat exchanger 12, and the 3rd absorbs Device 28 has weak solution pipeline to connect with the second absorber 24 with the second solution heat exchanger 13 through solution pump 11 again, by the 3rd Raw device 19 has concentrated solution pipeline to connect with absorber 3 through the second solution heat exchanger 13 to be adjusted to the 3rd generator 19 and have concentrated solution Pipeline connects with the 4th generator 25 through the second solution heat exchanger 13, and the 4th generator 25 has concentrated solution pipeline molten through the 3rd again Liquid pump 26 connects with absorber 3 with the 4th solution heat exchanger 27, and absorber 3 is had weak solution pipeline through solution heat exchanger 12 connect with generator 1 and to be adjusted to absorber 3 and have weak solution pipeline through the 4th solution heat exchanger 27 and solution heat exchanger 12 Connecting with generator 1, the 4th generator 25 also refrigerant steam channel connects with the 3rd absorber 28, and the 4th generator 25 is also Low-temperature heat medium passage and ft connection, the 3rd absorber 28 is had to also have coolant guiding channel and ft connection.
(2), in flow process, the concentrated solution of generator 1 enters the 3rd absorber 28 through solution heat exchanger 12, absorbs refrigerant vapour also Heat release enters the second absorption in cooling medium, the weak solution of the 3rd absorber 28 through solution pump 11 and the second solution heat exchanger 13 Device 24；The concentrated solution of the 3rd generator 19 enters the 4th generator 25 through the second solution heat exchanger 13, and low-temperature heat medium flows through 4th generator 25, heating enter its interior solution release refrigerant vapour and provide to the 3rd absorber 28, the 4th generator 25 Concentrated solution enter absorber 3 through the 3rd solution pump 26 and the 4th solution heat exchanger 27, the weak solution of absorber 3 is through the 4th Solution heat exchanger 27 and solution heat exchanger 12 enter generator 1, form the 5th class thermal drivers compressing-absorbing type heat pump.
The 5th class thermal drivers compressing-absorbing type heat pump that effect that the technology of the present invention can realize is proposed by the invention, have as Lower effect and advantage:
(1) propose new approaches, new ideas and new technique that the temperature difference utilizes, sending out further of compressing-absorbing type heat pump techniques will be promoted Exhibition and application.
(2) heat energy (temperature difference) drives, it is achieved heat supply/refrigeration, or externally provides power while of optional.
(3) flow process is reasonable, and performance index is variable and thermodynamic parameter change is corresponding, it is possible to realize heat energy (temperature difference) fully and Efficiently utilize.
(4) if desired, realizing heat supply by external impetus, mode is flexible, and adaptability is good.
(5) it is capable of effective utilization of high temperature heat, compensate for the deficiency of absorption heat pump technology, it is to avoid drive thermal medium parameter With conflicting between solution property.
(6) rely primarily on latent heat and realize acquisition and the release of thermic load, overcome the deficiency of gas compression formula heat pump techniques.
(7) multiple concrete technical scheme is provided, it is possible to tackle numerous different actual state, have the wider scope of application.
(8) extend heat pump techniques, enrich the type of thermal drivers compressing-absorbing type heat pump, be conducive to being better achieved the height of heat energy Effect utilizes.

Claims (32)

1. the 5th class thermal drivers compressing-absorbing type heat pump, mainly by generator, the second generator, absorber, compressor, swollen Swollen machine, condenser, the second condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, solution heat exchanger, second molten Liquid heat exchanger and high-temperature heat exchanger are formed；Generator (1) has concentrated solution pipeline through solution pump (11), solution heat exchange Device (12) connects with the second generator (2) with the second solution heat exchanger (13), and the second generator (2) also has concentrated solution Pipeline connects with absorber (3) through the second solution heat exchanger (13), and absorber (3) also has weak solution pipeline through solution heat Exchanger (12) connects with generator (1), and generator (1) also has refrigerant steam channel to connect with condenser (6), condensation Device (6) also has cryogen liquid pipeline to connect with vaporizer (8) through cryogen liquid pump (10), and the second generator (2) also has cryogen to steam Vapour passage connects with compressor (4), and compressor (4) also has refrigerant steam channel through high-temperature heat exchanger (14) and decompressor (5) connection, decompressor (5) also has refrigerant steam channel to connect with the second condenser (7), and the second condenser (7) also has After cryogen liquid pipeline connects with generator (1), generator (1) has cryogen liquid pipeline again through choke valve (9) and vaporizer (8) Connection, vaporizer (8) also has refrigerant steam channel to connect with absorber (3), the second generator (2) and high-temperature heat exchanger (14) having high temperature thermal medium passage and ft connection the most respectively, absorber (3) and the second condenser (7) have the most respectively and are added Hot media channel and ft connection, generator (1) and vaporizer (8) have low-temperature heat medium passage and ft connection the most respectively, Condenser (6) also has coolant guiding channel and ft connection, and decompressor (5) connects compressor (4) and transmits power, is formed 5th class thermal drivers compressing-absorbing type heat pump.
2. the 5th class thermal drivers compressing-absorbing type heat pump, mainly by generator, the second generator, absorber, compressor, swollen Swollen machine, condenser, the second condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, solution heat exchanger, second molten Liquid heat exchanger, high-temperature heat exchanger and regenerator are formed；Generator (1) has concentrated solution pipeline through solution pump (11), molten Liquid heat exchanger (12) connects with the second generator (2) with the second solution heat exchanger (13), and the second generator (2) is also Having concentrated solution pipeline to connect with absorber (3) through the second solution heat exchanger (13), absorber (3) also has weak solution pipeline Connecting with generator (1) through solution heat exchanger (12), generator (1) also has refrigerant steam channel with condenser (6) even Logical, condenser (6) also has cryogen liquid pipeline to connect with vaporizer (8) through cryogen liquid pump (10), and the second generator (2) is also Having refrigerant steam channel to connect with compressor (4), compressor (4) also has refrigerant steam channel through regenerator (15) and high temperature Heat exchanger (14) connects with decompressor (5), and decompressor (5) also has refrigerant steam channel through regenerator (15) and second Condenser (7) connect, the second condenser (7) also have cryogen liquid pipeline connect with generator (1) after generator (1) again Having cryogen liquid pipeline to connect with vaporizer (8) through choke valve (9), vaporizer (8) also has refrigerant steam channel and absorber (3) Connection, the second generator (2) and high-temperature heat exchanger (14) also have high temperature thermal medium passage and ft connection, absorber (3) Heated medium passage and ft connection, generator (1) and vaporizer (8) is had also to distinguish the most respectively with the second condenser (7) Having low-temperature heat medium passage and ft connection, condenser (6) also has coolant guiding channel and ft connection, and decompressor (5) is even Connect compressor (4) and transmit power, forming the 5th class thermal drivers compressing-absorbing type heat pump.
3. the 5th class thermal drivers compressing-absorbing type heat pump, mainly by generator, the second generator, absorber, compressor, swollen Swollen machine, condenser, the second condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, solution heat exchanger, second molten Liquid heat exchanger, high-temperature heat exchanger, the second compressor and the second high-temperature heat exchanger are formed；Generator (1) has concentrated solution Pipeline is through solution pump (11), solution heat exchanger (12) and the second solution heat exchanger (13) with the second generator (2) even Logical, the second generator (2) also has concentrated solution pipeline to connect with absorber (3) through the second solution heat exchanger (13), absorbs Device (3) also has weak solution pipeline to connect with generator (1) through solution heat exchanger (12), and generator (1) also has cryogen to steam Vapour passage connects with condenser (6), and condenser (6) also has cryogen liquid pipeline through cryogen liquid pump (10) with vaporizer (8) even Logical, the second generator (2) also has refrigerant steam channel to connect with compressor (4), and compressor (4) also has refrigerant steam channel Connecting with the second compressor (16) through high-temperature heat exchanger (14), the second compressor (16) also has refrigerant steam channel through the Two high-temperature heat exchangers (17) connect with decompressor (5), and decompressor (5) also has refrigerant steam channel and the second condenser (7) Connection, after the second condenser (7) also has cryogen liquid pipeline to connect with generator (1), generator (1) has cryogen liquid pipeline again Connecting with vaporizer (8) through choke valve (9), vaporizer (8) also has refrigerant steam channel to connect with absorber (3), the Two generators (2), high-temperature heat exchanger (14) and the second high-temperature heat exchanger (17) have the most respectively high temperature thermal medium passage with Ft connection, absorber (3) and the second condenser (7) have heated medium passage and ft connection, generator (1) the most respectively Having low-temperature heat medium passage and ft connection the most respectively with vaporizer (8), condenser (6) also has coolant guiding channel with outside Connection, decompressor (5) connects compressor (4) and the second compressor (16) and transmits power, forms the 5th class thermal drivers pressure Contracting-absorption heat pump.
4. the 5th class thermal drivers compressing-absorbing type heat pump, mainly by generator, the second generator, absorber, compressor, swollen Swollen machine, condenser, the second condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, solution heat exchanger, second molten Liquid heat exchanger, high-temperature heat exchanger, the second high-temperature heat exchanger and the second decompressor are formed；Generator (1) has concentrated solution Pipeline is through solution pump (11), solution heat exchanger (12) and the second solution heat exchanger (13) with the second generator (2) even Logical, the second generator (2) also has concentrated solution pipeline to connect with absorber (3) through the second solution heat exchanger (13), absorbs Device (3) also has weak solution pipeline to connect with generator (1) through solution heat exchanger (12), and generator (1) also has cryogen to steam Vapour passage connects with condenser (6), and condenser (6) also has cryogen liquid pipeline through cryogen liquid pump (10) with vaporizer (8) even Logical, the second generator (2) also has refrigerant steam channel to connect with compressor (4), and compressor (4) also has refrigerant steam channel Connecting with the second decompressor (18) through high-temperature heat exchanger (14), the second decompressor (18) also has refrigerant steam channel through the Two high-temperature heat exchangers (17) connect with decompressor (5), and decompressor (5) also has refrigerant steam channel and the second condenser (7) Connection, after the second condenser (7) also has cryogen liquid pipeline to connect with generator (1), generator (1) has cryogen liquid pipeline again Connecting with vaporizer (8) through choke valve (9), vaporizer (8) also has refrigerant steam channel to connect with absorber (3), the Two generators (2), high-temperature heat exchanger (14) and the second high-temperature heat exchanger (17) have the most respectively high temperature thermal medium passage with Ft connection, absorber (3) and the second condenser (7) have heated medium passage and ft connection, generator (1) the most respectively Having low-temperature heat medium passage and ft connection the most respectively with vaporizer (8), condenser (6) also has coolant guiding channel with outside Connection, decompressor (5) and the second decompressor (18) connect compressor (4) and transmit power, form the 5th class thermal drivers pressure Contracting-absorption heat pump.
5. the 5th class thermal drivers compressing-absorbing type heat pump, is in the 5th class thermal drivers compression-suction arbitrary described in claim 1-4 In receipts formula heat pump, cancel choke valve, have cryogen liquid pipeline to connect tune through choke valve (9) with vaporizer (8) in generator (1) Whole have cryogen liquid pipeline to connect with vaporizer (8) for generator (1), forms the 5th class thermal drivers compressing-absorbing type heat pump.
6. the 5th class thermal drivers compressing-absorbing type heat pump, is in the 5th class thermal drivers compression-suction arbitrary described in claim 1-4 In receipts formula heat pump, increase the 3rd generator, second throttle, the second solution pump, the 3rd solution heat exchanger and heater, send out Raw device (1) sets up concentrated solution pipeline through the second solution pump (21), solution heat exchanger (12) and the 3rd solution heat exchanger (22) Connect with the 3rd generator (19), the 3rd generator (19) also have concentrated solution pipeline through the 3rd solution heat exchanger (22) with Absorber (3) connects, and the second generator (2) has refrigerant steam channel connect with compressor (4) and is adjusted to the second generator (2) after having refrigerant steam channel to connect with the 3rd generator (19), the 3rd generator (19) has cryogen liquid pipeline again through heat supply Device (23), generator (1) connect with vaporizer (8) with second throttle (20), and the 3rd generator (19) also has cryogen Steam channel connects with compressor (4), and heater (23) also has heated medium passage and ft connection, forms the 5th class heat Drive compression-absorption heat pump.
7. the 5th class thermal drivers compressing-absorbing type heat pump, is in the 5th class thermal drivers compression-suction arbitrary described in claim 1-4 In receipts formula heat pump, increase the 3rd generator, second throttle, the 3rd solution heat exchanger and heater, generator (1) is had Concentrated solution pipeline is through solution pump (11), solution heat exchanger (12) and the second solution heat exchanger (13) and the second generator (2) Connection is adjusted to generator (1) has concentrated solution pipeline through solution pump (11), solution heat exchanger (12), the second solution heat exchange Device (13) connects with the second generator (2) with the 3rd solution heat exchanger (22), and the second generator (2) is had concentrated solution Pipeline connects with absorber (3) through the second solution heat exchanger (13) and is adjusted to the second generator (2) and has concentrated solution pipeline warp 3rd solution heat exchanger (22) connects with the 3rd generator (19), and the 3rd generator (19) has concentrated solution pipeline again through Two solution heat exchangers (13) connect with absorber (3), and the second generator (2) has refrigerant steam channel and compressor (4) Connection is adjusted to the 3rd generator (19) after the second generator (2) has refrigerant steam channel to connect with the 3rd generator (19) Cryogen liquid pipeline is had to connect with vaporizer (8) with second throttle (20) through heater (23), generator (1) again, the 3rd Generator (19) also has refrigerant steam channel to connect with compressor (4), and heater (23) also has heated medium passage with outer Portion connects, and forms the 5th class thermal drivers compressing-absorbing type heat pump.
8. the 5th class thermal drivers compressing-absorbing type heat pump, is in the 5th class thermal drivers compression-suction arbitrary described in claim 1-4 In receipts formula heat pump, increase the 3rd generator, second throttle, the second solution pump, the 3rd solution heat exchanger and heater, will Generator (1) has concentrated solution pipeline through solution pump (11), solution heat exchanger (12) and the second solution heat exchanger (13) Connect with the second generator (2) and be adjusted to generator (1) and have concentrated solution pipeline through solution pump (11), solution heat exchanger (12) Connecting with the 3rd generator (19) with the second solution heat exchanger (13), the 3rd generator (19) has concentrated solution pipeline warp again Second solution pump (21) connects with the second generator (2) with the 3rd solution heat exchanger (22), by the second generator (2) Have concentrated solution pipeline to connect with absorber (3) through the second solution heat exchanger (13) to be adjusted to the second generator (2) and have dense molten Liquid pipeline connects with absorber (3) with the second solution heat exchanger (13) through the 3rd solution heat exchanger (22), by second Raw device (2) has refrigerant steam channel to connect with compressor (4) to be adjusted to the second generator (2) and have refrigerant steam channel and the 3rd After generator (19) connection, the 3rd generator (19) has cryogen liquid pipeline again through heater (23), generator (1) and the Two choke valves (20) connect with vaporizer (8), and the 3rd generator (19) also has refrigerant steam channel with compressor (4) even Logical, heater (23) also has heated medium passage and ft connection, forms the 5th class thermal drivers compressing-absorbing type heat pump.
9. the 5th class thermal drivers compressing-absorbing type heat pump, is in the 5th class thermal drivers compression-absorption arbitrary described in claim 6-8 In formula heat pump, the 3rd generator (19) sets up high temperature thermal medium pipeline and ft connection, forms the 5th class thermal drivers compression-absorption Formula heat pump.
10. the 5th class thermal drivers compressing-absorbing type heat pump, is in the 5th class thermal drivers compression-suction arbitrary described in claim 6-9 In receipts formula heat pump, cancel choke valve and second throttle, generator (1) is had cryogen liquid pipeline through choke valve (9) and evaporation Device (8) connection is adjusted to generator (1) has cryogen liquid pipeline to connect with vaporizer (8), and generator (1) is had cryogen liquid Pipeline connects with vaporizer (8) through second throttle (21) and is adjusted to generator (1) and has cryogen liquid pipeline and vaporizer (8) Connection, forms the 5th class thermal drivers compressing-absorbing type heat pump.
11. the 5th class thermal drivers compressing-absorbing type heat pumps, are in the 5th class thermal drivers compression-suction arbitrary described in claim 1-4 In receipts formula heat pump, increase the 3rd generator, the second solution pump, the 3rd solution heat exchanger and the second absorber, by generator (1) There is concentrated solution pipeline through solution pump (11), solution heat exchanger (12) and the second solution heat exchanger (13) and the second generator (2) connection is adjusted to generator (1) has concentrated solution pipeline to connect with the second absorber (24) through solution heat exchanger (12), Second absorber (24) has weak solution pipeline again through solution pump (11) and the second solution heat exchanger (13) and the second generator (2) connection, has concentrated solution pipeline to connect with absorber (3) through the second solution heat exchanger (13) in the second generator (2) Being adjusted to the second generator (2) has concentrated solution pipeline to connect with the 3rd generator (19) through the second solution heat exchanger (13), 3rd generator (19) has concentrated solution pipeline again through the second solution pump (21) and the 3rd solution heat exchanger (22) and absorber (3) connection, has absorber (3) weak solution pipeline to connect with generator (1) through solution heat exchanger (12) and is adjusted to suction Receiving device (3) has weak solution pipeline to connect with generator (1) through the 3rd solution heat exchanger (22) and solution heat exchanger (12) Logical, generator (1) has cryogen liquid pipeline connect with vaporizer (8) through choke valve (9) and is adjusted to generator (1) and has cold Agent liquid pipeline connects with vaporizer (8) with choke valve (9) through the 3rd generator (19), and the 3rd generator (19) is the coldest Agent steam channel and the second absorber (24) connection, the second absorber (24) also has coolant guiding channel and ft connection, shape Become the 5th class thermal drivers compressing-absorbing type heat pump.
12. the 5th class thermal drivers compressing-absorbing type heat pumps, are in the 5th class thermal drivers compression-suction arbitrary described in claim 11 In receipts formula heat pump, cancel choke valve, the 3rd generator (19) is had cryogen liquid pipeline through choke valve (9) and vaporizer (8) Connection is adjusted to the 3rd generator (19) has cryogen liquid pipeline to connect with vaporizer (8), forms the 5th class thermal drivers compression-suction Receipts formula heat pump.
13. the 5th class thermal drivers compressing-absorbing type heat pumps, are in the 5th class thermal drivers compression-suction arbitrary described in claim 11 In receipts formula heat pump, increase the 4th generator, second throttle, the 3rd solution pump, the 4th solution heat exchanger and heater, the Two absorbers (24) are set up weak solution pipeline and are occurred with the 4th through the 3rd solution pump (26) and the 4th solution heat exchanger (27) Device (25) connects, and the 4th generator (25) also has concentrated solution pipeline through the 4th solution heat exchanger (27) and the 3rd generator (19) connection, has the second generator (2) refrigerant steam channel to connect with compressor (4) and is adjusted to the second generator (2) After having refrigerant steam channel to connect with the 4th generator (25) the 4th generator (25) have again cryogen liquid pipeline through heater (23), Generator (1), the 3rd generator (19) connect with vaporizer (8) with second throttle (20), the 4th generator (25) Also having refrigerant steam channel to connect with compressor (4), heater (23) also has heated medium passage and ft connection, is formed 5th class thermal drivers compressing-absorbing type heat pump.
14. the 5th class thermal drivers compressing-absorbing type heat pumps, are in the 5th class thermal drivers compression-suction arbitrary described in claim 11 In receipts formula heat pump, increase the 4th generator, second throttle, the 4th solution heat exchanger and heater, by the second absorber (24) There is weak solution pipeline to connect with the second generator (2) through solution pump (11) and the second solution heat exchanger (13) and be adjusted to second Absorber (24) has weak solution pipeline through solution pump (11), the second solution heat exchanger (13) and the 4th solution heat exchanger (27) Connect with the second generator (2), the second generator (2) is had concentrated solution pipeline through the second solution heat exchanger (13) and the Three generators (19) connection is adjusted to the second generator (2) has concentrated solution pipeline through the 4th solution heat exchanger (27) and the 4th Generator (25) connect, the 4th generator (25) have again concentrated solution pipeline through the second solution heat exchanger (13) with the 3rd Raw device (19) connection, has the second generator (2) refrigerant steam channel to connect with compressor (4) and is adjusted to the second generator (2) after having refrigerant steam channel to connect with the 4th generator (25), the 4th generator (25) has cryogen liquid pipeline again through heat supply Device (23), generator (1), the 3rd generator (19) connect with vaporizer (8) with second throttle (20), the 4th Raw device (25) also has refrigerant steam channel to connect with compressor (4), and heater (23) also has heated medium passage with outside Connection, forms the 5th class thermal drivers compressing-absorbing type heat pump.
15. the 5th class thermal drivers compressing-absorbing type heat pumps, are in the 5th class thermal drivers compression-suction arbitrary described in claim 11 In receipts formula heat pump, increase the 4th generator, second throttle, the 3rd solution pump, the 4th solution heat exchanger and heater, will Second absorber (24) has weak solution pipeline through solution pump (11) and the second solution heat exchanger (13) and the second generator (2) Connection is adjusted to the second absorber (24) has weak solution pipeline through solution pump (11) and the second solution heat exchanger (13) and the Four generators (25) connect, and the 4th generator (25) has concentrated solution pipeline again through the 3rd solution pump (26) and the 4th solution heat Exchanger (27) connects with the second generator (2), and the second generator (2) is had concentrated solution pipeline through the second solution heat exchange Device (13) connects with the 3rd generator (19) and is adjusted to the second generator (2) and has concentrated solution pipeline through the 4th solution heat exchanger (27) with the second solution heat exchanger (13) connects with the 3rd generator (19), and the second generator (2) is had refrigerant vapour Passage connects with compressor (4) and is adjusted to the second generator (2) and has refrigerant steam channel to connect it with the 4th generator (25) Rear 4th generator (25) has cryogen liquid pipeline again through heater (23), generator (1), the 3rd generator (19) and second Choke valve (20) connects with vaporizer (8), and the 4th generator (25) also has refrigerant steam channel to connect with compressor (4), Heater (23) also has heated medium passage and ft connection, forms the 5th class thermal drivers compressing-absorbing type heat pump.
16. the 5th class thermal drivers compressing-absorbing type heat pumps, are in the arbitrary 5th class thermal drivers pressure described in claim 13-15 In contracting-absorption heat pump, the 4th generator (25) sets up high temperature thermal medium pipeline and ft connection, forms the 5th class thermal drivers pressure Contracting-absorption heat pump.
17. the 5th class thermal drivers compressing-absorbing type heat pumps, are in the arbitrary 5th class thermal drivers pressure described in claim 13-16 In contracting-absorption heat pump, cancel choke valve and second throttle, the 3rd generator (19) is had cryogen liquid pipeline through choke valve (9) Connect with vaporizer (8) and be adjusted to the 3rd generator (19) and have cryogen liquid pipeline to connect with vaporizer (8), occur the 3rd Device (19) has cryogen liquid pipeline to connect with vaporizer (8) through second throttle (20) to be adjusted to the 3rd generator (19) and have cold Agent liquid pipeline connects with vaporizer (8), forms the 5th class thermal drivers compressing-absorbing type heat pump.
18. the 5th class thermal drivers compressing-absorbing type heat pumps, are in the 5th class thermal drivers compression-suction arbitrary described in claim 1-4 In receipts formula heat pump, increase the 3rd generator, the second solution pump, the 3rd solution heat exchanger and the second absorber, by generator (1) There is concentrated solution pipeline through solution pump (11), solution heat exchanger (12) and the second solution heat exchanger (13) and generator (2) Connection is adjusted to generator (1) has concentrated solution pipeline to hand over through solution pump (11), solution heat exchanger (12) and the second solution heat Parallel operation (13) connects with the second absorber (24), and the second absorber (24) has weak solution pipeline again through the second solution pump (21) Connect with the second generator (2) with the 3rd solution heat exchanger (22), the second generator (2) is had concentrated solution pipeline through Two solution heat exchangers (13) connect with absorber (3) and are adjusted to the second generator (2) and have concentrated solution pipeline through the 3rd solution Heat exchanger (22) connects with the 3rd generator (19), and the 3rd generator (19) has concentrated solution again through the second solution heat exchange Device (13) connects with absorber (3), and the 3rd generator (19) also has refrigerant steam channel to connect with the second absorber (24), 3rd generator (19) also has high temperature thermal medium passage and ft connection, and the second absorber (24) also has heated medium passage With ft connection, form the 5th class thermal drivers compressing-absorbing type heat pump.
19. the 5th class thermal drivers compressing-absorbing type heat pumps, are in the 5th class thermal drivers compression-suction arbitrary described in claim 18 In receipts formula heat pump, cancel choke valve, have cryogen liquid pipeline to connect tune through choke valve (9) with vaporizer (8) in generator (1) Whole have cryogen liquid pipeline to connect with vaporizer (8) for generator (1), forms the 5th class thermal drivers compressing-absorbing type heat pump.
20. the 5th class thermal drivers compressing-absorbing type heat pumps, are in the 5th class thermal drivers compression-suction arbitrary described in claim 18 In receipts formula heat pump, increase the 4th generator, second throttle, the 3rd solution pump, the 4th solution heat exchanger and heater, the Two absorbers (24) set up weak solution pipeline through the 3rd solution pump (26) and the 4th solution heat exchanger (27) and the 4th generator (25) connection, the 4th generator (25) also has concentrated solution pipeline through the 4th solution heat exchanger (27) and the 3rd generator (19) Connection, has the second generator (2) refrigerant steam channel to connect with compressor (4) and is adjusted to the second generator (2) and has cryogen After steam channel and the connection of the 4th generator (25), the 4th generator (25) has cryogen liquid pipeline through heater (23) again, sends out Raw device (1) connects with vaporizer (8) with second throttle (20), and the 4th generator (25) also has refrigerant steam channel and pressure Contracting machine (4) connects, and heater (23) also has heated medium passage and ft connection, forms the 5th class thermal drivers compression-suction Receipts formula heat pump.
21. the 5th class thermal drivers compressing-absorbing type heat pumps, are in the 5th class thermal drivers compression-suction arbitrary described in claim 18 In receipts formula heat pump, increase the 4th generator, second throttle, the 4th solution heat exchanger and heater, by the second absorber (24) Have weak solution pipeline to connect with the second generator (2) through the second solution pump (21) and the 3rd solution heat exchanger (22) to be adjusted to Second absorber (24) has weak solution pipeline through the second solution pump (21), the 3rd solution heat exchanger (22) and the 4th solution heat Exchanger (27) connects with the second generator (2), and the second generator (2) is had concentrated solution pipeline through the 3rd solution heat exchange Device (22) connects with the 3rd generator (19) and is adjusted to the second generator (2) and has concentrated solution pipeline through the 4th solution heat exchanger (27) connecting with the 4th generator (25), the 4th generator (25) has concentrated solution pipeline again through the 3rd solution heat exchanger (22) Connect with the 3rd generator (19), the second generator (2) has refrigerant steam channel connect with compressor (4) and is adjusted to After two generators (2) have refrigerant steam channel to connect with the 4th generator (25), the 4th generator (25) has cryogen liquid pipe again Road connects with vaporizer (8) with second throttle (20) through heater (23), generator (1), the 4th generator (25) Also having refrigerant steam channel to connect with compressor (4), heater (23) also has heated medium passage and ft connection, is formed 5th class thermal drivers compressing-absorbing type heat pump.
22. the 5th class thermal drivers compressing-absorbing type heat pumps, are in the 5th class thermal drivers compression-suction arbitrary described in claim 18 In receipts formula heat pump, increase the 4th generator, second throttle, the 3rd solution pump, the 4th solution heat exchanger and heater, will Second absorber (24) has weak solution pipeline to occur with second through the second solution pump (21) and the 3rd solution heat exchanger (22) Device (2) connection is adjusted to the second absorber (24) has weak solution pipeline through the second solution pump (21) and the 3rd solution heat exchanger (22) connect with the 4th generator (25), the 4th generator (25) have concentrated solution pipeline through the 3rd solution pump (26) again and 4th solution heat exchanger (27) connects with the second generator (2), and the second generator (2) is had concentrated solution pipeline through the 3rd Solution heat exchanger (22) connects with the 3rd generator (19) and is adjusted to the second generator (2) and has concentrated solution pipeline molten through the 4th Liquid heat exchanger (27) connects with the 3rd generator (19) with the 3rd solution heat exchanger (22), by the second generator (2) Have refrigerant steam channel to connect with compressor (4) to be adjusted to the second generator (2) and have refrigerant steam channel and the 4th generator (25) After connection, the 4th generator (25) has cryogen liquid pipeline again through heater (23), generator (1) and second throttle (20) Connecting with vaporizer (8), the 4th generator (25) also has refrigerant steam channel to connect with compressor (4), heater (23) Also have heated medium passage and ft connection, form the 5th class thermal drivers compressing-absorbing type heat pump.
23. the 5th class thermal drivers compressing-absorbing type heat pumps, are in the arbitrary 5th class thermal drivers pressure described in claim 20-22 In contracting-absorption heat pump, the 4th generator (25) sets up high temperature thermal medium passage and ft connection, forms the 5th class thermal drivers pressure Contracting-absorption heat pump.
24. the 5th class thermal drivers compressing-absorbing type heat pumps, are in the arbitrary 5th class thermal drivers pressure described in claim 20-23 In contracting-absorption heat pump, cancel choke valve and second throttle, generator (1) is had cryogen liquid pipeline through choke valve (9) with Vaporizer (8) connection is adjusted to generator (1) has cryogen liquid pipeline to connect with vaporizer (8), has cold by generator (1) Agent liquid pipeline connects with vaporizer (8) through second throttle (20) and is adjusted to generator (1) and has cryogen liquid pipeline and vaporizer (8) connection, forms the 5th class thermal drivers compressing-absorbing type heat pump.
25. the 5th class thermal drivers compressing-absorbing type heat pumps, are in the 5th class thermal drivers compression-suction arbitrary described in claim 18 In receipts formula heat pump, increase the 4th generator, the 3rd solution pump, the 4th solution heat exchanger and the 3rd absorber, by generator (1) There is concentrated solution pipeline through solution pump (11), solution heat exchanger (12) and the second solution heat exchanger (13) and the second absorber (24) connection is adjusted to generator (1) has concentrated solution pipeline to connect with the 3rd absorber (28) through solution heat exchanger (12), 3rd absorber (28) has weak solution pipeline again through solution pump (11) and the second solution heat exchanger (13) and the second absorber (24) connection, has concentrated solution pipeline through the second solution heat exchanger (13) with absorber (3) even by the 3rd generator (19) Logical the 3rd generator (19) that is adjusted to has concentrated solution pipeline through the second solution heat exchanger (13) with the 4th generator (25) even Logical, the 4th generator (25) has concentrated solution pipeline through the 3rd solution pump (26) and the 4th solution heat exchanger (27) and to inhale again Receive device (3) connection, have weak solution pipeline to connect adjustment through solution heat exchanger (12) with generator (1) absorber (3) Weak solution pipeline is had through the 4th solution heat exchanger (27) and solution heat exchanger (12) and generator (1) for absorber (3) Connection, has generator (1) cryogen liquid pipeline to connect with vaporizer (8) through choke valve (9) and is adjusted to generator (1) and has Cryogen liquid pipeline connects with vaporizer (8) with choke valve (9) through the 4th generator (25), and the 4th generator (25) also has Refrigerant steam channel connects with the 3rd absorber (28), and the 3rd absorber (28) also has coolant guiding channel and ft connection, Form the 5th class thermal drivers compressing-absorbing type heat pump.
26. the 5th class thermal drivers compressing-absorbing type heat pumps, are in the 5th class thermal drivers compression-suction arbitrary described in claim 25 In receipts formula heat pump, cancel choke valve, the 4th generator (25) is had cryogen liquid pipeline through choke valve (9) and vaporizer (8) Connection is adjusted to the 4th generator (25) has cryogen liquid pipeline to connect with vaporizer (8), forms the 5th class thermal drivers compression-suction Receipts formula heat pump.
27. the 5th class thermal drivers compressing-absorbing type heat pumps, mainly by generator, the second generator, absorber, compressor, Decompressor, condenser, the second condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, solution heat exchanger, second Solution heat exchanger, high-temperature heat exchanger and regenerator are formed；Generator (1) have concentrated solution pipeline through solution pump (11), Solution heat exchanger (12) connects with the second generator (2) with the second solution heat exchanger (13), the second generator (2) Also having concentrated solution pipeline to connect with absorber (3) through the second solution heat exchanger (13), absorber (3) also has weak solution pipe Road connects with generator (1) through solution heat exchanger (12), and generator (1) also has refrigerant steam channel and condenser (6) Connection, condenser (6) also has cryogen liquid pipeline to connect with vaporizer (8) through cryogen liquid pump (10), the second generator (2) Also having refrigerant steam channel to connect with compressor (4) through regenerator (15), compressor (4) also has refrigerant steam channel through height Temperature heat exchanger (14) connects with decompressor (5), and decompressor (5) also has refrigerant steam channel through regenerator (15) and the Two condensers (7) connect, the second condenser (7) also have cryogen liquid pipeline connect with generator (1) after generator (1) Having cryogen liquid pipeline to connect with vaporizer (8) through choke valve (9) again, vaporizer (8) also has refrigerant steam channel and absorber (3) connecting, the second generator (2) and high-temperature heat exchanger (14) have high temperature thermal medium passage and ft connection the most respectively, Absorber (3) and the second condenser (7) have heated medium passage and ft connection, generator (1) and vaporizer the most respectively (8) having low-temperature heat medium passage and ft connection the most respectively, condenser (6) also has coolant guiding channel and ft connection, swollen Swollen machine (5) connects compressor (4) and transmits power, forms the 5th class thermal drivers compressing-absorbing type heat pump.
28. the 5th class thermal drivers compressing-absorbing type heat pumps, are at the 5th class thermal drivers compressing-absorbing type described in claim 27 In heat pump, cancel choke valve, generator (1) has cryogen liquid pipeline connect with vaporizer (8) through choke valve (9) and is adjusted to Generator (1) has cryogen liquid pipeline to connect with vaporizer (8), forms the 5th class thermal drivers compressing-absorbing type heat pump.
29. the 5th class thermal drivers compressing-absorbing type heat pumps, are at the 5th class thermal drivers arbitrary described in claim 1-5,27-28 In compressing-absorbing type heat pump, cancel or retain the low-temperature heat medium passage of generator (1) and ft connection, increase by the 3rd generation Device, the second solution pump, the 3rd solution heat exchanger and the second absorber, generator (1) is had concentrated solution pipeline through solution pump (11), Solution heat exchanger (12) and the second solution heat exchanger (13) connect with the second generator (2) and are adjusted to generator (1) Having concentrated solution pipeline to connect with the second absorber (24) through solution heat exchanger (12), the second absorber (24) has dilute molten again Liquid pipeline connects with the second generator (2) with the second solution heat exchanger (13) through solution pump (11), by the second generator (2) Have concentrated solution pipeline to connect with absorber (3) through the second solution heat exchanger (13) to be adjusted to two generators (2) and have concentrated solution Pipeline connects with the 3rd generator (19) through the second solution heat exchanger (13), and the 3rd generator (19) has concentrated solution pipe again Road the second solution pump (21) connects with absorber (3) with the 3rd solution heat exchanger (22), has dilute by absorber (3) Solution line connects with generator (1) through solution heat exchanger (12) and is adjusted to absorber (3) and has weak solution pipeline through the 3rd Solution heat exchanger (22) connects with generator (1) with solution heat exchanger (12), and the 3rd generator (19) also has cryogen Steam channel and the second absorber (24) connection, the 3rd generator (19) also has low-temperature heat medium passage and ft connection, the Two absorbers (24) also have coolant guiding channel and ft connection, form the 5th class thermal drivers compressing-absorbing type heat pump.
30. the 5th class thermal drivers compressing-absorbing type heat pumps, are in the arbitrary 5th class thermal drivers pressure described in claim 18-19 In contracting-absorption heat pump, cancel or retain the low-temperature heat medium passage of generator (1) and ft connection, increase the 4th generator, 3rd solution pump, the 4th solution heat exchanger and the 3rd absorber, generator (1) is had concentrated solution pipeline through solution pump (11), Solution heat exchanger (12) and the second solution heat exchanger (13) connect with the second absorber (24) and are adjusted to generator (1) Having concentrated solution pipeline to connect with the 3rd absorber (28) through solution heat exchanger (12), the 3rd absorber (28) has dilute molten again Liquid pipeline connects with the second absorber (24) with the second solution heat exchanger (13) through solution pump (11), by the 3rd generator (19) there is concentrated solution pipeline to connect with absorber (3) through the second solution heat exchanger (13) and be adjusted to the 3rd generator (19) Having concentrated solution pipeline to connect with the 4th generator (25) through the second solution heat exchanger (13), the 4th generator (25) has again Concentrated solution pipeline connects with absorber (3) with the 4th solution heat exchanger (27) through the 3rd solution pump (26), by absorber (3) Have weak solution pipeline to connect with generator (1) through solution heat exchanger (12) to be adjusted to absorber (3) and have weak solution pipeline warp 4th solution heat exchanger (27) connects with generator (1) with solution heat exchanger (12), and the 4th generator (25) also has Refrigerant steam channel connects with the 3rd absorber (28), and the 4th generator (25) also has low-temperature heat medium passage and ft connection, 3rd absorber (28) also has coolant guiding channel and ft connection, forms the 5th class thermal drivers compressing-absorbing type heat pump.
31. the 5th class thermal drivers compressing-absorbing type heat pumps, are in the arbitrary first kind thermal drivers pressure described in claim 1-30 In contracting-absorption heat pump, increasing working machine, decompressor (5) connects working machine and provides power to working machine, and it is additional right to be formed 5th class thermal drivers compressing-absorbing type heat pump of outer offer living load.
32. the 5th class thermal drivers compressing-absorbing type heat pumps, are in the arbitrary first kind thermal drivers pressure described in claim 1-30 In contracting-absorption heat pump, increasing engine, engine connects compressor (4) and provides power to compressor (4), is formed attached Add the 5th class thermal drivers compressing-absorbing type heat pump that external impetus drives.
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