CN106322821A - Fourth-class thermally driven compression-absorption heat pump - Google Patents

Fourth-class thermally driven compression-absorption heat pump Download PDF

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Publication number
CN106322821A
CN106322821A CN201610821029.5A CN201610821029A CN106322821A CN 106322821 A CN106322821 A CN 106322821A CN 201610821029 A CN201610821029 A CN 201610821029A CN 106322821 A CN106322821 A CN 106322821A
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China
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generator
solution
heat exchanger
pump
connect
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CN201610821029.5A
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CN106322821B (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

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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 fourth-class thermally driven compression-absorption heat pump, and belongs to the technical field of power, refrigeration and heat pumps. A generator, a second generator, an absorber, a solution pump, a solution heat exchanger and a second solution heat exchanger form a solution loop. The generator communicates with a condenser through a refrigerant steam channel. The second generator communicates with a second condenser through a refrigerant steam channel. The second condenser communicates with the generator, a throttling valve and an evaporator. The second condenser sequentially communicates with a high-temperature heat exchanger, an expansion machine and the absorber through a second refrigerant liquid pump. The condenser communicates with the evaporator through a refrigerant liquid pump. The evaporator communicates with the absorber through a refrigerant steam channel via a compressor. The generator and the high-temperature heat exchanger communicate with the outside through a high-temperature thermal medium channel. The absorber and the second condenser communicate with the outside through a heated medium channel. The evaporator communicates with the outside through a low-temperature thermal medium channel. The condenser communicates with the outside through a cooling medium channel. The expansion machine is connected with the compressor and transmits power, so that the fourth-class thermally driven compression-absorption heat pump is formed.

Description

4th 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 often need High temperature heat to be utilized realizes refrigeration, heat supply or is converted into power, it is also desirable to utilize power to carry out freezing or utilizing power And combine low temperature heat energy and carry out heat supply.During stating purpose in realization, many conditions will be faced and limit the energy Type, grade and quantity, the type of user's request, grade and quantity, the type of working media, the flow process of equipment, structure and Manufacturing cost, the safety that equipment runs, ambient temperature and the acceptable degree etc. of environment.
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 refrigeration；Affected by the character of working media (solution and refrigerant medium), the high-temperature hot load of excessive temperature or mistake low temperature Low Temperature Thermal load often cannot reasonably be applied in absorption heat pump flow process, cause its application and range of application to be subject to Bigger restriction.Compression heat pump technology has preferable motility in terms of thermodynamic property, but the core of compression heat pump Part is moving component, it is desirable to equipment runs higher safety, the noise etc. that reduction equipment to be managed runs；To this end, need Consider to reduce use and the quantity of big moving component (mainly compressor and decompressor).
In order to play the technical advantage of absorption heat pump and take into account power drive or externally provide power demand, the present invention carries The temperature difference going out to comprise cryogen liquid pump, high-temperature heat exchanger, decompressor and compressor composition utilizes link and to high temperature heat source and quilt Add the temperature difference between thermal medium effectively to utilize, and comprise cryogen liquid pump, high-temperature heat exchanger, decompressor, compressor and The temperature difference of two condenser compositions utilizes link and effectively utilizes the temperature difference between high temperature heat source and environment, with high-temperature hot load Temperature drop is as the driving temperature difference of absorption heat pump flow process step by step, has the 4th class thermal drivers compressing-absorbing type heat of comprehensive advantage Pump.
Summary of the invention:
Present invention is primarily intended to provide series the 4th class thermal drivers compressing-absorbing type heat pump, concrete summary of the invention divides Item is described below:
1. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by generator, the second generator, absorber, condenser, Second condenser, vaporizer, choke valve, cryogen liquid pump, the second cryogen liquid pump, solution pump, solution heat exchanger, the second solution heat Exchanger, high-temperature heat exchanger, decompressor and compressor are formed；Generator has concentrated solution pipeline to hand over through solution pump, solution heat Parallel operation and the second solution heat exchanger and the second generator connect, and the second generator also has concentrated solution pipeline to hand over through the second solution heat Parallel operation connects with absorber, and absorber also has weak solution pipeline to connect with generator through solution heat exchanger, and generator is the coldest Agent steam channel connects with condenser, and condenser also has cryogen liquid pipeline to connect with vaporizer through cryogen liquid pump, the second generator Also having refrigerant steam channel to connect with the second condenser, the second condenser also has cryogen liquid pipeline through generator and choke valve and steaming Sending out device connection, the second condenser also has cryogen liquid pipeline high-temperature hot after the second cryogen liquid pump connects with high-temperature heat exchanger to hand over Parallel operation has refrigerant steam channel to connect with decompressor again, and decompressor also has refrigerant steam channel to connect with absorber or condenser, Vaporizer also has refrigerant steam channel to connect with compressor, and compressor also has refrigerant steam channel to connect with absorber, second Raw device and high-temperature heat exchanger have high temperature thermal medium passage and ft connection, absorber and the second condenser to have the most respectively the most respectively Heated medium passage and ft connection, vaporizer also has low-temperature heat medium passage and ft connection, and condenser also cools down Jie Matter passage and ft connection, decompressor connects compressor and transmits power, forms the 4th class thermal drivers compressing-absorbing type heat pump； Wherein, or decompressor connects compressor, cryogen liquid pump, the second cryogen liquid pump and solution pump and transmits power.
2. the 4th class thermal drivers compressing-absorbing type heat pump, is at the 1st the 4th described class thermal drivers compressing-absorbing type In heat pump, increase the 3rd generator, the second absorber, the second solution pump and the 3rd solution heat exchanger, generator is had dense molten Liquid pipeline is adjusted to generator has dense through solution pump, solution heat exchanger and the second solution heat exchanger and the connection of the second generator Solution line connects through solution pump, solution heat exchanger and the second solution heat exchanger and the second absorber, and the second absorber is again There is weak solution pipeline through the second solution pump and the 3rd solution heat exchanger and the connection of the second generator, the second generator is had dense molten Liquid pipeline connects with absorber through the second solution heat exchanger and is adjusted to the second generator and has concentrated solution pipeline through the 3rd solution heat Exchanger and the connection of the 3rd generator, the 3rd generator has concentrated solution pipeline through the second solution heat exchanger with absorber even again Logical, the 3rd generator also has refrigerant steam channel to connect with the second absorber, the 3rd generator also have high temperature thermal medium passage and Ft connection, the second absorber also has heated medium passage and ft connection, forms the 4th class thermal drivers compressing-absorbing type heat Pump.
3. the 4th class thermal drivers compressing-absorbing type heat pump, be described in 1-2 item arbitrary 4th class thermal drivers compression- In absorption heat pump, cancel choke valve, have cryogen liquid pipeline to connect with vaporizer with choke valve through generator the second condenser Being adjusted to the second condenser has cryogen liquid pipeline to connect with vaporizer through generator, forms the 4th class thermal drivers compressing-absorbing type Heat pump.
4. the 4th class thermal drivers compressing-absorbing type heat pump, is the 1st described 4th class thermal drivers compressing-absorbing type heat In pump, increasing the 3rd generator, second throttle, the second solution pump, the 3rd solution heat exchanger and heater, generator is set up Concentrated solution pipeline connects through the second solution pump, solution heat exchanger and the 3rd solution heat exchanger and the 3rd generator, the 3rd Raw device also has concentrated solution pipeline to connect with absorber through the 3rd solution heat exchanger, the second generator is had refrigerant steam channel and Second condenser connection is adjusted to after the second generator has refrigerant steam channel to connect the 3rd generator with the 3rd generator again Having cryogen liquid pipeline to connect with vaporizer with second throttle through heater, generator, the 3rd generator also has refrigerant vapour to lead to Road and the connection of the second condenser, heater also has heated medium passage and ft connection, forms the 4th class thermal drivers compression-suction Receipts formula heat pump.
5. the 4th class thermal drivers compressing-absorbing type heat pump, is at the 1st the 4th described class thermal drivers compressing-absorbing type 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 through solution pump, solution heat exchanger and the second solution heat exchanger and the connection of the second generator Pipeline connects through solution pump, solution heat exchanger, the second solution heat exchanger and the 3rd solution heat exchanger and the second generator, Second generator has concentrated solution pipeline connect with absorber through the second solution heat exchanger be adjusted to the second generator and have dense molten Liquid pipeline connects through the 3rd solution heat exchanger and the 3rd generator, and the 3rd generator has concentrated solution pipeline again through the second solution heat Exchanger connects with absorber, the second generator has refrigerant steam channel connect with the second condenser and is adjusted to the second generator After having refrigerant steam channel to connect with the 3rd generator, the 3rd generator has cryogen liquid pipeline again through heater, generator and Two choke valves connect with vaporizer, and the 3rd generator also has refrigerant steam channel to connect with the second condenser, and heater also has quilt Heating medium passage and ft connection, form the 4th class thermal drivers compressing-absorbing type heat pump.
6. the 4th class thermal drivers compressing-absorbing type heat pump, is at the 1st the 4th described class thermal drivers compressing-absorbing type In heat pump, increase the 3rd generator, second throttle, the second solution pump, the 3rd solution heat exchanger and heater, by generator There is concentrated solution pipeline to connect through solution pump, solution heat exchanger and the second solution heat exchanger and the second generator and be adjusted to generation Device has concentrated solution pipeline to connect through solution pump, solution heat exchanger and the second solution heat exchanger and the 3rd generator, the 3rd Raw device has concentrated solution pipeline to connect with the second generator, by the second generator through the second solution pump and the 3rd solution heat exchanger again Have 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 through the 3rd Solution heat exchanger and the second solution heat exchanger connect with absorber, have refrigerant steam channel cold with second in second generator Condenser connection is adjusted to the 3rd generator after the second generator has refrigerant steam channel to connect with the 3rd generator cryogen again Liquid pipeline connects with vaporizer with second throttle through heater, generator, and the 3rd generator also has refrigerant steam channel and the Two condenser connections, heater also has heated medium passage and ft connection, forms the 4th class thermal drivers compressing-absorbing type heat Pump.
7. the 4th class thermal drivers compressing-absorbing type heat pump, is at the 2nd the 4th described 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 absorbs Device sets up weak solution pipeline through the 3rd solution pump and the 4th solution heat exchanger and the connection of the 4th generator, and the 4th generator also has Concentrated solution pipeline connects through the 4th solution heat exchanger and the 3rd generator, and the second generator is had refrigerant steam channel and second Condenser connection is adjusted to the 4th generator after the second generator has refrigerant steam channel to connect with the 4th generator to be had cold again Agent liquid pipeline connects with vaporizer with second throttle through heater, generator, the 4th generator also have refrigerant steam channel with Second condenser connection, heater also has heated medium passage and ft connection, forms the 4th class thermal drivers compressing-absorbing type Heat pump.
8. the 4th class thermal drivers compressing-absorbing type heat pump, is at the 2nd the 4th described 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 through the second solution pump and the 3rd solution heat exchanger and the connection of the second generator Pipeline connects, by second through the second solution pump, the 3rd solution heat exchanger and the 4th solution heat exchanger and the second generator Raw device has concentrated solution pipeline to be adjusted to the second generator have concentrated solution pipe through the 3rd solution heat exchanger and the connection of the 3rd generator Lu Jing tetra-solution heat exchanger and the connection of the 4th generator, the 4th generator has concentrated solution pipeline again through the 3rd solution heat exchange Device and the connection of the 3rd generator, have the second generator refrigerant steam channel to connect with the second condenser and be adjusted to the second generator After having refrigerant steam channel to connect with the 4th generator, the 4th generator has cryogen liquid pipeline again through heater, generator and Two choke valves connect with vaporizer, and the 4th generator also has refrigerant steam channel to connect with the second condenser, and heater also has quilt Heating medium passage and ft connection, form the 4th class thermal drivers compressing-absorbing type heat pump.
9. the 4th class thermal drivers compressing-absorbing type heat pump, is at the 2nd the 4th described 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, inhale second Receive device to have weak solution pipeline to connect with the second generator through the second solution pump and the 3rd solution heat exchanger to be adjusted to the second absorption Device has weak solution pipeline through the second solution pump and the 3rd solution heat exchanger and the connection of the 4th generator, and the 4th generator has dense 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 pipe by solution line Lu Jing tri-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 3rd solution heat exchanger and the 3rd generator connect, and the second generator has refrigerant steam channel and the second condensation Device connection is adjusted to the 4th generator after the second generator has refrigerant steam channel to connect with the 4th generator cryogen liquid again Pipeline connects with vaporizer with second throttle through heater, generator, and the 4th generator also has refrigerant steam channel and second Condenser connects, and heater also has heated medium passage and ft connection, forms the 4th class thermal drivers compressing-absorbing type heat Pump.
10. the 4th class thermal drivers compressing-absorbing type heat pump, be described in 4-6 item arbitrary 4th class thermal drivers compression- Absorption heat pump, the 3rd generator is set up high temperature thermal medium passage and ft connection, is formed the 4th class thermal drivers compressing-absorbing type Heat pump.
11. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the described arbitrary 4th class thermal drivers compression-suction of 7-9 item Receipts formula heat pump, the 4th generator is set up high temperature thermal medium passage and ft connection, is formed the 4th class thermal drivers compressing-absorbing type heat Pump.
12. the 4th class thermal drivers compressing-absorbing type heat pumps, be 4-11 item described arbitrary 4th class thermal drivers compression- Absorption heat pump, cancels choke valve and second throttle, and generator has cryogen liquid pipeline connect tune with vaporizer through choke valve Whole have cryogen liquid pipeline to connect with vaporizer for generator, and generator has cryogen liquid pipeline through second throttle with vaporizer even Logical it be adjusted to generator and have cryogen liquid pipeline to connect with vaporizer, formation the 4th class thermal drivers compressing-absorbing type heat pump.
13. the 4th class thermal drivers compressing-absorbing type heat pumps, are at the 1st the 4th described class thermal drivers compressing-absorbing type In heat pump, increase the 3rd generator, the second absorber, the second solution pump and the 3rd solution heat exchanger, generator is had dense molten Liquid pipeline is adjusted to generator has dense through solution pump, solution heat exchanger and the second solution heat exchanger and the connection of the second generator Solution line connects through solution heat exchanger and the second absorber, and the second absorber has weak solution pipeline again through solution pump and second Solution heat exchanger and the connection of the second generator, have concentrated solution pipeline through the second solution heat exchanger and absorption by the second generator Device connection is adjusted to the second generator has concentrated solution pipeline to connect through the second solution heat exchanger and the 3rd generator, and the 3rd occurs Device has concentrated solution pipeline to connect with absorber through the second solution pump and the 3rd solution heat exchanger again, and absorber has weak solution pipe Road connects with generator through solution heat exchanger and is adjusted to absorber and has weak solution pipeline through the 3rd solution heat exchanger and solution Heat exchanger connects with generator, and the second condenser has cryogen liquid pipeline connect adjustment with vaporizer through generator and choke valve Being that the second condenser has cryogen liquid pipeline to connect with vaporizer with choke valve through generator, the 3rd generator, the 3rd generator is also Having refrigerant steam channel to connect with the second absorber, the second absorber also has coolant guiding channel and ft connection, forms the 4th Class thermal drivers compressing-absorbing type heat pump.
14. the 4th class thermal drivers compressing-absorbing type heat pumps, are the 13rd described the 4th class thermal drivers compression-absorption In formula heat pump, cancel choke valve, the 3rd generator has cryogen liquid pipeline connect with vaporizer through choke valve and is adjusted to the 3rd Raw device has cryogen liquid pipeline to connect with vaporizer, forms the 4th class thermal drivers compressing-absorbing type heat pump.
15. the 4th class thermal drivers compressing-absorbing type heat pumps, are the 13rd described the 4th class thermal drivers compression-absorption In formula 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 There is concentrated solution pipeline to connect through the 4th solution heat exchanger and the 3rd generator, the second generator is had refrigerant steam channel and the Two condenser connections are adjusted to the 4th generator after the second generator has refrigerant steam channel to connect with the 4th generator to be had again Cryogen liquid pipeline connects with vaporizer with second throttle through heater, generator, the 3rd generator, and the 4th generator is the coldest Agent steam channel and the connection of the second condenser, heater also has heated medium passage and ft connection, forms the 4th class heat and drives Dynamic pressure contracting-absorption heat pump.
16. the 4th class thermal drivers compressing-absorbing type heat pumps, are the 13rd described the 4th class thermal drivers compression-absorption In formula heat pump, increase the 4th generator, second throttle, the 4th solution heat exchanger and heater, the second absorber is had dilute Solution line is adjusted to the second absorber has weak solution pipe through solution pump and the second solution heat exchanger and the connection of the second generator Road connects through solution pump, the second solution heat exchanger and the 4th solution heat exchanger and the second generator, is had by the second generator Concentrated solution pipeline connects through the second solution heat exchanger and the 3rd generator and is adjusted to the second generator and has concentrated solution pipeline through the Four solution heat exchangers and the connection of the 4th generator, the 4th generator has concentrated solution pipeline again through the second solution heat exchanger and the Three generators connections, have the second generator refrigerant steam channel to connect with the second condenser and are adjusted to the second generator and have cryogen After steam channel and the connection of the 4th generator, the 4th generator has cryogen liquid pipeline again through heater, generator, the 3rd generation Device connects with vaporizer with second throttle, and the 4th generator also has refrigerant steam channel to connect with the second condenser, heater Also have heated medium passage and ft connection, form the 4th class thermal drivers compressing-absorbing type heat pump.
17. the 4th class thermal drivers compressing-absorbing type heat pumps, are the 13rd described the 4th class thermal drivers compression-absorption In formula 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 solution pump and the second solution heat exchanger and the connection of the second generator Having weak solution pipeline through solution pump and the second solution heat exchanger and the connection of the 4th generator, the 4th generator has concentrated solution pipe again Lu Jing tri-solution pump and the 4th solution heat exchanger and the connection of the second generator, have concentrated solution pipeline through the by the second generator Two solution heat exchangers and the connection of the 3rd generator are adjusted to the second generator and have concentrated solution pipeline through the 4th solution heat exchanger Connect with the second solution heat exchanger and the 3rd generator, have refrigerant steam channel to connect with the second condenser in the second generator It is adjusted to the 4th generator after the second generator has refrigerant steam channel to connect with the 4th generator and has 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 Second condenser connection, heater also has heated medium passage and ft connection, forms the 4th class thermal drivers compressing-absorbing type Heat pump.
18. the 4th class thermal drivers compressing-absorbing type heat pumps, be 15-17 item described arbitrary 4th class thermal drivers compression- Absorption heat pump, the 4th generator is set up high temperature thermal medium passage and ft connection, is formed the 4th class thermal drivers compressing-absorbing type Heat pump.
19. the 4th class thermal drivers compressing-absorbing type heat pumps, be 15-18 item described arbitrary 4th class thermal drivers compression- In absorption heat pump, cancel choke valve and second throttle, the 3rd generator is had cryogen liquid pipeline through choke valve and vaporizer Connection is adjusted to the 3rd generator has cryogen liquid pipeline to connect with vaporizer, and the 3rd generator is had cryogen liquid pipeline through second section Stream valve connects with vaporizer and is adjusted to the 3rd generator and has cryogen liquid pipeline to connect with vaporizer, formation the 4th class thermal drivers pressure Contracting-absorption heat pump.
20. the 4th class thermal drivers compressing-absorbing type heat pumps, are the 2nd described arbitrary 4th class thermal drivers compression-absorption In formula heat pump, increase the 4th generator, the 3rd absorber, the 3rd solution pump and the 4th solution heat exchanger, generator is had dense Solution line is adjusted to generator has through solution pump, solution heat exchanger and the second solution heat exchanger and the connection of the second absorber Concentrated solution pipeline connects through solution heat exchanger and the 3rd absorber, and the 3rd absorber has weak solution pipeline again through solution pump and the Two solution heat exchangers and the connection of the second absorber, have concentrated solution pipeline through the second solution heat exchanger and suction by the 3rd generator Receipts device connection is adjusted to the 3rd generator has concentrated solution pipeline to connect through the second solution heat exchanger and the 4th generator, the 4th Raw device has concentrated solution pipeline to connect with absorber through the 3rd solution pump and the 4th solution heat exchanger again, and absorber is had weak solution Pipeline connects with generator through solution heat exchanger and is adjusted to absorber and has weak solution pipeline through the 4th solution heat exchanger and molten Liquid heat exchanger connects with generator, and the second condenser has cryogen liquid pipeline connect tune with vaporizer through generator and choke valve Whole is that the second condenser has cryogen liquid pipeline to connect with vaporizer with choke valve through generator, the 4th generator, the 4th generator Also having refrigerant steam channel to connect with the 3rd absorber, the 3rd absorber also has coolant guiding channel and ft connection, formation the Four class thermal drivers compressing-absorbing type heat pumps.
21. the 4th class thermal drivers compressing-absorbing type heat pumps, be the 20th described arbitrary 4th class thermal drivers compression- In absorption heat pump, cancel choke valve, the 4th generator has cryogen liquid pipeline connect with vaporizer through choke valve and is adjusted to the Four generators have cryogen liquid pipeline to connect with vaporizer, form the 4th class thermal drivers compressing-absorbing type heat pump.
22. the 4th class thermal drivers compressing-absorbing type heat pumps, are at the 1st the 4th described class thermal drivers compressing-absorbing type In heat pump, increase the 3rd generator, the second absorber, the second solution pump and the 3rd solution heat exchanger, the second generator is had Refrigerant steam channel connects with the second condenser and is adjusted to the second generator and has refrigerant steam channel to connect with the second absorber, and Two absorbers also have weak solution pipeline through the second solution pump and the 3rd solution heat exchanger and the connection of the 3rd generator, and the 3rd occurs Device also has concentrated solution pipeline to connect through the 3rd solution heat exchanger and the second absorber, and the 3rd generator also has refrigerant steam channel Connecting with the second condenser, the 3rd generator also has high temperature thermal medium passage and ft connection, and the second absorber also has heated Medium channel and ft connection, form the 4th class thermal drivers compressing-absorbing type heat pump.
23. the 4th class thermal drivers compressing-absorbing type heat pumps, are at the 22nd described 4th 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 4th class thermal drivers compressing-absorbing type heat pump.
24. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the arbitrary 4th class thermal drivers pressure described in 1-23 item In contracting-absorption heat pump, decompressor has refrigerant steam channel connect with absorber or condenser and is adjusted to decompressor and has cryogen Steam channel and the connection of the second condenser, form the 4th class thermal drivers compressing-absorbing type heat pump.
25. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the arbitrary 4th class thermal drivers pressure described in 1-24 item In contracting-absorption heat pump, increasing engine, engine connects compressor and transmits power to compressor, forms additional external and moves Power-actuated 4th class thermal drivers compressing-absorbing type heat pump.
26. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the arbitrary 4th class thermal drivers pressure described in 1-24 item In contracting-absorption heat pump, increasing working machine, decompressor connects working machine and transmits power to working machine, and formation is additional externally to be carried The 4th class thermal drivers compressing-absorbing type heat pump for living load.
Accompanying drawing illustrates:
Fig. 1 is based on the 4th the 1st kind of principled thermal system of class thermal drivers compressing-absorbing type heat pump provided by the present invention Figure.
Fig. 2 is based on the 4th the 2nd kind of principled thermal system of class thermal drivers compressing-absorbing type heat pump provided by the present invention Figure.
Fig. 3 is based on the 4th the 3rd kind of principled thermal system of class thermal drivers compressing-absorbing type heat pump provided by the present invention Figure.
Fig. 4 is based on the 4th the 4th kind of principled thermal system of class thermal drivers compressing-absorbing type heat pump provided by the present invention Figure.
Fig. 5 is based on the 4th the 5th kind of principled thermal system of class thermal drivers compressing-absorbing type heat pump provided by the present invention Figure.
Fig. 6 is based on the 4th the 6th kind of principled thermal system of class thermal drivers compressing-absorbing type heat pump provided by the present invention Figure.
Fig. 7 is based on the 4th the 7th kind of principled thermal system of class thermal drivers compressing-absorbing type heat pump provided by the present invention Figure.
Fig. 8 is based on the 4th the 8th kind of principled thermal system of class thermal drivers compressing-absorbing type heat pump provided by the present invention Figure.
Fig. 9 is based on the 4th the 9th kind of principled thermal system of class thermal drivers compressing-absorbing type heat pump provided by the present invention Figure.
Figure 10 is based on the 4th class thermal drivers compressing-absorbing type heat pump provided by the present invention 10th kind principle heating power system System figure.
Figure 11 is based on the 4th class thermal drivers compressing-absorbing type heat pump provided by the present invention 11st kind principle heating power system System figure.
Figure 12 is based on the 4th class thermal drivers compressing-absorbing type heat pump provided by the present invention 12nd kind principle heating power system System figure.
Figure 13 is based on the 4th class thermal drivers compressing-absorbing type heat pump provided by the present invention 13rd kind principle heating power system System figure.
Figure 14 is based on the 4th class thermal drivers compressing-absorbing type heat pump provided by the present invention 14th kind principle heating power system System figure.
Figure 15 is based on the 4th class thermal drivers compressing-absorbing type heat pump provided by the present invention 15th kind principle heating power system System figure.
In figure, 1-generator, 2-the second generator, 3-absorber, 4-condenser, 5-the second condenser, 6-vaporizer, 7- Choke valve, 8-cryogen liquid pump, 9-the second cryogen liquid pump, 10-solution pump, 11-solution heat exchanger, 12-the second solution heat exchange Device, 13-high-temperature heat exchanger, 14-decompressor, 15-compressor, 16-the 3rd generator, 17-the second absorber, 18-second is molten Liquid pump, 19-the 3rd solution heat exchanger, 20-second throttle, 21-heater, 22-the 4th generator, 23-the 3rd solution pump, 24-the 4th solution heat exchanger, 25-the 3rd absorber.
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 obviously Flow process do not state.The present invention is described in detail below in conjunction with the accompanying drawings with example.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 1 is achieved in that
(1) in structure, it mainly by generator, the second generator, absorber, condenser, the second condenser, vaporizer, Choke valve, cryogen liquid pump, the second cryogen liquid pump, solution pump, solution heat exchanger, the second solution heat exchanger, high-temperature hot exchange Device, decompressor and compressor are formed；Generator 1 has concentrated solution pipeline molten through solution pump 10, solution heat exchanger 11 and second Liquid heat exchanger 12 connects with the second generator 2, the second generator 2 also have concentrated solution pipeline through the second solution heat exchanger 12 with Absorber 3 connects, and absorber 3 also weak solution pipeline connects with generator 1 through solution heat exchanger 11, and generator 1 is the coldest Agent steam channel connects with condenser 4, and condenser 4 also cryogen liquid pipeline connects with vaporizer 6 through cryogen liquid pump 8, second Raw device 2 also refrigerant steam channel connects with the second condenser 5, and the second condenser 5 also has cryogen liquid pipeline through generator 1 and joint Stream valve 7 connects with vaporizer 6, and the second condenser 5 also has cryogen liquid pipeline through the second cryogen liquid pump 9 with high-temperature heat exchanger 13 even After Tong, high-temperature heat exchanger 13 has refrigerant steam channel to connect with decompressor 14 again, decompressor 14 also have refrigerant steam channel with Absorber 3 connects, and vaporizer 6 also refrigerant steam channel connects with compressor 15, compressor 15 also have refrigerant steam channel with Absorber 3 connects, and the second generator 2 and high-temperature heat exchanger 13 have high temperature thermal medium passage and ft connection the most respectively, absorbs Device 3 and the second condenser 5 have heated medium passage and ft connection the most respectively, vaporizer 6 also have low-temperature heat medium passage with Ft connection, condenser 4 also has coolant guiding channel and ft connection, and decompressor 14 connects compressor 15 and transmits power.
(2), in flow process, the concentrated solution of generator 1 is through solution pump 10, solution heat exchanger 11 and the second solution heat exchanger 12 enter the second generator 2, and high temperature thermal medium flows through the second generator 2, heating enters its interior solution release refrigerant vapour also Thering is provided to the second condenser 5, the concentrated solution of the second generator 2 enters absorber 3 through the second solution heat exchanger 12, absorbs cryogen Steam heat release enter generator 1, cryogen liquid stream warp in heated medium, the weak solution of absorber 3 through solution heat exchanger 11 Generator 1, heating enter its interior solution release refrigerant vapour and provide to condenser 4；The refrigerant vapour heat release of condenser 4 in Cooling medium becomes cryogen liquid, and the cryogen liquid of condenser 4 enters vaporizer 6 through cryogen liquid pump 8 pressurization；The cryogen of the second condenser 5 Steam heat release becomes cryogen liquid, the cryogen liquid of the second condenser 5 to be divided into the two-way first via in heated medium to flow through generator 1 Enter vaporizer 6 through choke valve 7 reducing pressure by regulating flow again after heat release, after second tunnel the second cryogen liquid pump 9 pressurization, flow through high temperature Heat exchanger 13 absorbs heat into refrigerant vapour and provides to decompressor 14, and refrigerant vapour enters after flowing through decompressor 14 blood pressure lowering work done Absorber 3, the merit of decompressor 14 output is supplied to compressor 15 and is used as power；Low-temperature heat medium flows through vaporizer 6, heating enters it Interior cryogen liquid becomes refrigerant vapour, the refrigerant vapour of vaporizer 6 release to flow through entrance absorber after compressor 15 boosting heats up 1, form the 4th class thermal drivers compressing-absorbing type heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 2 is achieved in that
In the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 1, decompressor 14 there are refrigerant steam channel and suction Receipts device 3 connection is adjusted to decompressor 14 has refrigerant steam channel to connect with condenser 4, forms the 4th class thermal drivers compression-absorption Formula heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 3 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 1, increase the 3rd generator, second Absorber, the second solution pump and the 3rd solution heat exchanger, have concentrated solution pipeline to hand over through solution pump 10, solution heat by generator 1 Parallel operation 11 and the second solution heat exchanger 12 connect with the second generator 2 and are adjusted to generator 1 and have concentrated solution pipeline through solution pump 10, solution heat exchanger 11 connects with the second absorber 17 with the second solution heat exchanger 12, and the second absorber 17 has dilute molten again Liquid pipeline connects with the second generator 2 with the 3rd solution heat exchanger 19 through the second solution pump 18, has dense molten by the second generator 2 Liquid pipeline connects with absorber 3 through the second solution heat exchanger 12 and is adjusted to the second generator 2 and has concentrated solution pipeline molten through the 3rd Liquid heat exchanger 19 connects with the 3rd generator 16, and the 3rd generator 16 has concentrated solution pipeline again through the second solution heat exchanger 12 Connecting with absorber 3, the 3rd generator 16 also refrigerant steam channel connects with the second absorber 17, and the 3rd generator 16 also has High temperature thermal medium passage and ft connection, the second absorber 17 also has heated medium passage and ft connection.
(2), in flow process, the concentrated solution of generator 1 is through solution pump 10, solution heat exchanger 11 and the second solution heat exchanger 12 entrance the second absorbers 17, absorption refrigerant vapour heat release are in heated medium, and the weak solution of the second absorber 17 is through second Solution pump 18 and the 3rd solution heat exchanger 19 enter the second generator 2, and the concentrated solution of the second generator 2 is handed over through the 3rd solution heat Parallel operation 19 enters the 3rd generator 16, and high temperature thermal medium flows through the 3rd generator 16, heating enters its interior solution release cryogen Steam also provides to the second absorber 17, and the concentrated solution of the 3rd generator 16 enters absorber 3 through the second solution heat exchanger 12, Form the 4th class thermal drivers compressing-absorbing type heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 4 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 1, increase the 3rd generator, second Choke valve, the second solution pump, the 3rd solution heat exchanger and heater, generator 1 sets up concentrated solution pipeline through the second solution pump 18, solution heat exchanger 11 connects with the 3rd generator 16 with the 3rd solution heat exchanger 19, and the 3rd generator 16 also has dense molten Liquid pipeline connects with absorber 3 through the 3rd solution heat exchanger 19, and the second generator 2 has refrigerant steam channel and the second condensation Device 5 connection is adjusted to the 3rd generator 16 after the second generator 2 has refrigerant steam channel to connect with the 3rd generator 16 to be had again Cryogen liquid pipeline connects with vaporizer 6 with second throttle 20 through heater 21, generator 1, and the 3rd generator 16 also has cryogen Steam channel and the second condenser 5 connect, and heater 21 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 16 and makees to drive thermal medium, sends out The part concentrated solution of raw device 1 enters the 3rd through the second solution pump 18, solution heat exchanger 11 and the 3rd solution heat exchanger 19 Raw device 16, refrigerant vapour flows through the 3rd generator 16, heating enters its interior solution and discharges refrigerant vapour and to the second condenser 5 Thering is provided, the concentrated solution of the 3rd generator 16 is through the 3rd solution heat exchanger 19 absorber 3；The cryogen flowing through the 3rd generator 16 steams Vapour heat release becomes cryogen liquid, cryogen liquid stream through heater 21 and generator 1 progressively heat release, after through second throttle 20 throttle into Enter vaporizer 6, form the 4th class thermal drivers compressing-absorbing type heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 5 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 1, increase the 3rd generator, second Choke valve, the 3rd solution heat exchanger and heater, have concentrated solution pipeline through solution pump 10, solution heat exchanger by generator 1 11 connect with the second generator 2 with the second solution heat exchanger 12 and to be adjusted to generator 1 and have concentrated solution pipeline through solution pump 10, molten Liquid heat exchanger the 11, second solution heat exchanger 12 connects with the second generator 2 with the 3rd solution heat exchanger 19, by second Raw device 2 has concentrated solution pipeline to connect with absorber 3 through the second solution heat exchanger 12 to be adjusted to the second generator 2 and have concentrated solution pipe Lu Jing tri-solution heat exchanger 19 connects with the 3rd generator 16, and the 3rd generator 16 has concentrated solution pipeline again through the second solution Heat exchanger 12 connects with absorber 3, the second generator 2 has refrigerant steam channel connect with the second condenser 5 and is adjusted to After two generators 2 have refrigerant steam channel to connect with the 3rd generator 16, the 3rd generator 16 has cryogen liquid pipeline again through heat supply Device 21, generator 1 connect with vaporizer 6 with second throttle 20, and the 3rd generator 16 also has refrigerant steam channel cold with second Condenser 5 connects, and heater 21 also has heated medium passage and ft connection, the 3rd generator 16 to also have high temperature thermal medium passage With ft connection.
(2), in flow process, the refrigerant vapour that high temperature thermal medium and the second generator 2 produce is supplied to the 3rd generator 16 and drives Dynamic thermal medium, the concentrated solution of generator 1 is molten through solution pump 10, solution heat exchanger the 11, second solution heat exchanger 12 and the 3rd Liquid heat exchanger 19 enters the second generator 2, and the concentrated solution of the second generator 2 enters the 3rd through the 3rd solution heat exchanger 19 Raw device 16, high temperature thermal medium and refrigerant vapour stream enter its interior solution release cryogen steam through the 3rd generator 16, heating respectively Vapour also provides to the second condenser 5, and the concentrated solution of the 3rd generator 16 enters absorber 3 through the second solution heat exchanger 12；Stream Become cryogen liquid through the refrigerant vapour heat release of the 3rd generator 16, cryogen liquid stream through heater 21 and generator 1 progressively heat release, it Enter vaporizer 6 by second throttle 20 throttling, form the 4th class thermal drivers compressing-absorbing type heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 6 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 1, increase the 3rd generator, second Choke valve, the second solution pump, the 3rd solution heat exchanger and heater, have concentrated solution pipeline through solution pump 10, molten by generator 1 Liquid heat exchanger 11 and the second solution heat exchanger 12 connect with the second generator 2 and are adjusted to generator 1 and have concentrated solution pipeline warp Solution pump 10, solution heat exchanger 11 connect with the 3rd generator 16 with the second solution heat exchanger 12, and the 3rd generator 16 is again Concentrated solution pipeline is had to connect with the second generator 2 with the 3rd solution heat exchanger 19 through the second solution pump 18, by the second generator 2 Have concentrated solution pipeline to connect with absorber 3 through the second solution heat exchanger 12 to be adjusted to the second generator 2 and have concentrated solution pipeline warp 3rd solution heat exchanger 19 connects with absorber 3 with the second solution heat exchanger 12, has refrigerant vapour to lead in the second generator 2 Road and the connection of the second condenser 5 are adjusted to after the second generator 2 has refrigerant steam channel to connect with the 3rd generator 16 the 3rd Generator 16 has cryogen liquid pipeline to connect with vaporizer 6 with second throttle 20 through heater 21, generator 1 again, and the 3rd occurs Device 16 also refrigerant steam channel connects with the second condenser 5, and heater 21 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 16 and makees to drive thermal medium, sends out The concentrated solution of raw device 1 enters the 3rd generator 16 through solution pump 10, solution heat exchanger 11 and the second solution heat exchanger 12, cold Agent steam flows through the 3rd generator 16, heating enters its interior solution release refrigerant vapour and provides to the second condenser 5, the 3rd The concentrated solution of generator 16 enters the second generator 2, the second generator 2 through the second solution pump 18 and the 3rd solution heat exchanger 19 Concentrated solution enter absorber 3 through the 3rd solution heat exchanger 19 and the second solution heat exchanger 12；Flow through the 3rd generator 16 Refrigerant vapour heat release become cryogen liquid, cryogen liquid stream through heater 21 and generator 1 progressively heat release, after through second throttle 20 throttlings enter vaporizer 6, form the 4th class thermal drivers compressing-absorbing type heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 7 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 3, increase the 4th generator, second Choke valve, the 3rd solution pump, the 4th solution heat exchanger and heater, it is molten through the 3rd that the second absorber 17 sets up weak solution pipeline Liquid pump 23 connects with the 4th generator 22 with the 4th solution heat exchanger 24, and the 4th generator 22 also has concentrated solution pipeline through the 4th Solution heat exchanger 24 connects with the 3rd generator 16, has refrigerant steam channel to connect with the second condenser 5 in second generator 2 It is adjusted to the 4th generator 22 after the second generator 2 has refrigerant steam channel to connect with the 4th generator 22 and has cryogen liquid pipe again Road connects with vaporizer 6 with second throttle 20 through heater 21, generator 1, and the 4th generator 22 also has refrigerant steam channel Connecting with the second condenser 5, heater 21 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 22 and makees to drive thermal medium, the The part weak solution of two absorbers 17 enters the 4th generator 22 through the 3rd solution pump 23 and the 4th solution heat exchanger 24, cryogen Steam flows through the 4th generator 22, heating enters its interior solution release refrigerant vapour and provides to the second condenser 5, the 4th The concentrated solution of raw device 22 enters the 3rd generator 16 through the 4th solution heat exchanger 24；Flow through the refrigerant vapour of the 4th generator 22 Heat release becomes cryogen liquid, cryogen liquid stream through heater 21 and generator 1 progressively heat release, after enter through second throttle 20 throttling Vaporizer 6, forms the 4th class thermal drivers compressing-absorbing type heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 8 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 3, increase the 4th generator, second Choke valve, the 4th solution heat exchanger and heater, have weak solution pipeline through the second solution pump 18 and by the second absorber 17 Three solution heat exchangers 19 connect with the second generator 2 and are adjusted to the second absorber 17 and have weak solution pipeline through the second solution pump 18, the 3rd solution heat exchanger 19 connects with the second generator 2 with the 4th solution heat exchanger 24, has dense by the second generator 2 Solution line connects with the 3rd generator 16 through the 3rd solution heat exchanger 19 and is adjusted to the second generator 2 and has concentrated solution pipeline warp 4th solution heat exchanger 24 connects with the 4th generator 22, and the 4th generator 22 has concentrated solution pipeline to hand over through the 3rd solution heat again Parallel operation 19 connects with the 3rd generator 16, the second generator 2 has refrigerant steam channel connect with the second condenser 5 and is adjusted to After two generators 2 have refrigerant steam channel to connect with the 4th generator 22, the 4th generator 22 has cryogen liquid pipeline again through heat supply Device 21, generator 1 connect with vaporizer 6 with second throttle 20, and the 4th generator 22 also has refrigerant steam channel cold with second Condenser 5 connects, and heater 21 also has heated medium passage and ft connection, the 4th generator 22 to also have high temperature thermal medium passage With ft connection.
(2), in flow process, the refrigerant vapour that high temperature thermal medium and the second generator 2 produce is supplied to the 4th generator 22 and drives Dynamic thermal medium, the weak solution of the second absorber 17 is handed over through the second solution pump the 18, the 3rd solution heat exchanger 19 and the 4th solution heat Parallel operation 24 enters the second generator 2, and the concentrated solution of the second generator 2 enters the 4th generator through the 4th solution heat exchanger 24 22, refrigerant vapour and high temperature thermal medium flow separately through the 4th generator 22, heating enters its interior solution release refrigerant vapour also Thering is provided to the second condenser 5, the concentrated solution of the 4th generator 22 enters the 3rd generator 16 through the 3rd solution heat exchanger 19；Stream Cryogen liquid, cryogen liquid is become to flow through heater 21 and generator 1 successively and progressively put through the refrigerant vapour heat release of the 4th generator 22 Heat, after through second throttle 20 throttling enter vaporizer 6, formed the 4th class thermal drivers compressing-absorbing type heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 9 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 3, choke valve is cancelled, by generator 1 There is cryogen liquid pipeline to connect with vaporizer 6 through choke valve 7 to be adjusted to generator 1 and have cryogen liquid pipeline to connect with vaporizer 6, increase 4th generator, the 3rd solution pump, the 4th solution heat exchanger and heater, have weak solution pipeline through by the second absorber 17 Two solution pumps 18 and the 3rd solution heat exchanger 19 connect with the second generator 2 and are adjusted to the second absorber 17 and have weak solution pipeline Connecting with the 4th generator 22 with the 3rd solution heat exchanger 19 through the second solution pump 18, the 4th generator 22 has concentrated solution pipe again Lu Jing tri-solution pump 23 connects with the second generator 2 with the 4th solution heat exchanger 24, and the second generator 2 is had concentrated solution pipe Lu Jing tri-solution heat exchanger 19 connects with the 3rd generator 16 and is adjusted to the second generator 2 and has concentrated solution pipeline molten through the 4th Liquid heat exchanger 24 connects with the 3rd generator 16 with the 3rd solution heat exchanger 19, has refrigerant vapour to lead in the second generator 2 Road and the connection of the second condenser 5 are adjusted to after the second generator 2 has refrigerant steam channel to connect with the 4th generator 22 the 4th Generator 22 has cryogen liquid pipeline to connect with vaporizer 6 with generator 1 through heater 21 again, and the 4th generator 22 also has cryogen to steam Vapour passage and the second condenser 5 connect, and heater 21 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 22 and makees to drive thermal medium, the The weak solution of two absorbers 17 enters the 4th generator 22, refrigerant vapour through the second solution pump 18 and the 3rd solution heat exchanger 19 Flow through the 4th generator 22, heating enters its interior solution release refrigerant vapour and provides to the second condenser 5, the 4th generator The concentrated solution of 22 enters the second generator 2 through the 3rd solution pump 23 and the 4th solution heat exchanger 24, the second generator 2 dense molten Liquid enters the 3rd generator 16 through the 4th solution heat exchanger 24 and the 3rd solution heat exchanger 19；Flow through the 4th generator 22 Refrigerant vapour heat release becomes cryogen liquid, cryogen liquid to flow through heater 21 and generator 1 progressively heat release successively, enters vaporizer afterwards 6, form the 4th class thermal drivers compressing-absorbing type heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Figure 10 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 1, increase the 3rd generator, second Absorber, the second solution pump and the 3rd solution heat exchanger, have concentrated solution pipeline to hand over through solution pump 10, solution heat by generator 1 Parallel operation 11 and the second solution heat exchanger 12 connect with the second generator 2 and are adjusted to generator 1 and have concentrated solution pipeline through solution heat Exchanger 11 connects with the second absorber 17, and the second absorber 17 has weak solution pipeline to hand over through solution pump 10 and the second solution heat again Parallel operation 12 connects with the second generator 2, and the second generator 2 is had concentrated solution pipeline through the second solution heat exchanger 12 and absorber 3 connections are adjusted to the second generator 2 has concentrated solution pipeline to connect with the 3rd generator 16 through the second solution heat exchanger 12, and the 3rd Generator 16 has concentrated solution pipeline to connect with absorber 3 with the 3rd solution heat exchanger 19 through the second solution pump 18 again, will absorb Device 3 has weak solution pipeline to connect with generator 1 through solution heat exchanger 11 to be adjusted to absorber 3 and have weak solution pipeline molten through the 3rd Liquid heat exchanger 19 connects with generator 1 with solution heat exchanger 11, and the second condenser 5 is had cryogen liquid pipeline through generator 1 Connect with vaporizer 6 with choke valve 7 and be adjusted to the second condenser 5 and have cryogen liquid pipeline through generator the 1, the 3rd generator 16 and joint Stream valve 7 connects with vaporizer 6, and the 3rd generator 16 also refrigerant steam channel connects with the second absorber 17, the second absorber 17 also have coolant guiding channel and ft connection.
(2), in flow process, the concentrated solution of generator 1 enters the second absorber 17 through solution heat exchanger 11, absorbs cryogen steaming Vapour heat release enter second in cooling medium, the weak solution of the second absorber 17 through solution pump 10 and the second solution heat exchanger 12 Generator 2；The concentrated solution of the second generator 2 enters the 3rd generator 16, heat absorption release cryogen through the second solution heat exchanger 12 Steam also provides to the second absorber 17, and the concentrated solution of the 3rd generator 16 is through the second solution pump 18 and the 3rd solution heat exchanger 19 enter absorber 3, and the weak solution of absorber 3 enters generator 1 through the 3rd solution heat exchanger 19 and solution heat exchanger 11； The part cryogen liquid of the second condenser 5 flows through generator 1 and the 3rd generator 16 progressively heat release, successively afterwards through choke valve 7 Reducing pressure by regulating flow enters vaporizer 6, forms the 4th class thermal drivers compressing-absorbing type heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Figure 11 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Figure 10, choke valve is cancelled, by the 3rd Raw device 16 has cryogen liquid pipeline to connect with vaporizer 6 through choke valve 7 to be adjusted to the 3rd generator 16 and have cryogen liquid pipeline and evaporation Device 6 connects, and increases the 4th generator, the 3rd solution pump, the 4th solution heat exchanger and heater, and the second absorber 17 is set up dilute Solution line connects with the 4th generator 22 with the 4th solution heat exchanger 24 through the 3rd solution pump 23, and the 4th generator 22 also has Concentrated solution pipeline connects with the 3rd generator 16 through the 4th solution heat exchanger 24, and the second generator 2 is had refrigerant steam channel Connect with the second condenser 5 and be adjusted to after the second generator 2 has refrigerant steam channel to connect with the 4th generator 22 the 4th Raw device 22 has cryogen liquid pipeline to connect with vaporizer 6 with the 3rd generator 16 through heater 21, generator 1 again, the 4th generator 22 also refrigerant steam channel connect with the second condenser 5, heater 21 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 22 and makees to drive thermal medium, the The part weak solution of two absorbers 17 enters the 4th generator 22 through the 3rd solution pump 23 and the 4th solution heat exchanger 24, cryogen Steam flows through the 4th generator 22, heating enters its interior solution release refrigerant vapour and provides to the second condenser 5, the 4th The concentrated solution of raw device 22 enters the 3rd generator 16 through the 4th solution heat exchanger 24；Flow through the refrigerant vapour of the 4th generator 22 Heat release becomes cryogen liquid, cryogen liquid to flow through heater 21, generator 1 and the 3rd generator 16 progressively heat release successively, enters afterwards Vaporizer 6, forms the 4th class thermal drivers compressing-absorbing type heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Figure 12 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Figure 10, choke valve is cancelled, by the 3rd Raw device 16 has cryogen liquid pipeline to connect with vaporizer 6 through choke valve 7 to be adjusted to the 3rd generator 16 and have cryogen liquid pipeline and evaporation Device 6 connects, and increases the 4th generator, the 4th solution heat exchanger and heater, the second absorber 17 is had weak solution pipeline warp Solution pump 10 and the second solution heat exchanger 12 connect with the second generator 2 and are adjusted to the second absorber 17 and have weak solution pipeline warp Solution pump the 10, second solution heat exchanger 12 connects with the second generator 2 with the 4th solution heat exchanger 24, by the second generator 2 have concentrated solution pipeline to connect with the 3rd generator 16 through the second solution heat exchanger 12 is adjusted to the second generator 2 and has concentrated solution Pipeline connects with the 4th generator 22 through the 4th solution heat exchanger 24, and the 4th generator 22 has concentrated solution pipeline molten through second again Liquid heat exchanger 12 connects with the 3rd generator 16, has refrigerant steam channel to connect tune with the second condenser 5 in second generator 2 Whole is that after the second generator 2 has refrigerant steam channel to connect with the 4th generator 22, the 4th generator 22 has cryogen liquid pipeline again Connect with vaporizer 6 with the 3rd generator 16 through heater 21, generator 1, the 4th generator 22 also have refrigerant steam channel with Second condenser 5 connects, and heater 21 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 22 and makees to drive thermal medium, the The weak solution of two absorbers 17 enters second through solution pump the 10, second solution heat exchanger 12 and the 4th solution heat exchanger 24 Raw device 2, the concentrated solution of the second generator 2 enters the 4th generator 22 through the 4th solution heat exchanger 24, and refrigerant vapour flows through the Four generators 22, heating enter its interior solution release refrigerant vapour and also provide to the second condenser 5, the 4th generator 22 dense Solution enters the 3rd generator 16 through the second solution heat exchanger 12；The refrigerant vapour heat release flowing through the 4th generator 22 becomes cryogen Liquid, cryogen liquid flows through heater 21, generator 1 and the 3rd generator 16 progressively heat release successively, enters vaporizer 6, shape afterwards Become the 4th class thermal drivers compressing-absorbing type heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Figure 13 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Figure 10, choke valve is cancelled, by the 3rd Raw device 16 has cryogen liquid pipeline to connect with vaporizer 6 through choke valve 7 to be adjusted to the 3rd generator 16 and have cryogen liquid pipeline and evaporation Device 6 connects, and increases the 4th generator, the 3rd solution pump, the 4th solution heat exchanger and heater, has dilute by the second absorber 17 Solution line connects with the second generator 2 through solution pump 10 and the second solution heat exchanger 12 and is adjusted to the second absorber 17 and has dilute Solution line connects with the 4th generator 22 with the second solution heat exchanger 12 through solution pump 10, and the 4th generator 22 has dense molten again Liquid pipeline connects with the second generator 2 with the 4th solution heat exchanger 24 through the 3rd solution pump 23, has dense molten by the second generator 2 Liquid pipeline connects with the 3rd generator 16 through the second solution heat exchanger 12 and is adjusted to the second generator 2 and has concentrated solution pipeline through Four solution heat exchangers 24 connect with the 3rd generator 16 with the second solution heat exchanger 12, have cryogen to steam in the second generator 2 Vapour passage and the connection of the second condenser 5 are adjusted to after the second generator 2 has refrigerant steam channel to connect with the 4th generator 22 4th generator 22 has cryogen liquid pipeline to connect with vaporizer 6 with the 3rd generator 16 through heater 21, generator 1 again, and the 4th Generator 22 also refrigerant steam channel connects with the second condenser 5, and heater 21 also heated medium passage connects with outside Logical.
(2), in flow process, the refrigerant vapour that the second generator 2 produces is supplied to the 4th generator 22 and makees to drive thermal medium, the The weak solution of two absorbers 17 enters the 4th generator 22 through solution pump 10 and the second solution heat exchanger 12, and refrigerant vapour flows through 4th generator 22, heating enter its interior solution release refrigerant vapour and provide to the second condenser 5, the 4th generator 22 Concentrated solution enters the second generator 2 through the 3rd solution pump 23 and the 4th solution heat exchanger 24, the concentrated solution warp of the second generator 2 4th solution heat exchanger 24 and the second solution heat exchanger 12 enter the 3rd generator 16；Flow through the cryogen of the 4th generator 22 Steam heat release becomes cryogen liquid, cryogen liquid to flow through heater 21, generator 1 and the 3rd generator 16 progressively heat release successively, afterwards Enter vaporizer 6, form the 4th class thermal drivers compressing-absorbing type heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Figure 14 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 3, increase the 4th generator, the 3rd Absorber, the 3rd solution pump and the 4th solution heat exchanger, have concentrated solution pipeline to hand over through solution pump 10, solution heat by generator 1 Parallel operation 11 and the second solution heat exchanger 12 connect with the second absorber 17 and are adjusted to generator 1 and have concentrated solution pipeline through solution heat Exchanger 11 connects with the 3rd absorber 25, and the 3rd absorber 25 has weak solution pipeline to hand over through solution pump 10 and the second solution heat again Parallel operation 12 connects with the second absorber 17, the 3rd generator 16 has concentrated solution pipeline through the second solution heat exchanger 12 and absorption Device 3 connection is adjusted to the 3rd generator 16 has concentrated solution pipeline to connect with the 4th generator 22 through the second solution heat exchanger 12, 4th generator 22 has concentrated solution pipeline to connect with absorber 3 with the 4th solution heat exchanger 24 through the 3rd solution pump 23 again, will Absorber 3 has weak solution pipeline to connect with generator 1 through solution heat exchanger 11 to be adjusted to absorber 3 and have weak solution pipeline through Four solution heat exchangers 24 connect with generator 1 with solution heat exchanger 11, the second condenser 5 have cryogen liquid pipeline through occurring Device 1 and choke valve 7 connect with vaporizer 6 and are adjusted to the second condenser 5 and have cryogen liquid pipeline through generator the 1, the 4th generator 22 Connecting with vaporizer 6 with choke valve 7, the 4th generator 22 also refrigerant steam channel connects with the 3rd absorber 25, and the 3rd inhales Receive device 25 and also have coolant guiding channel and ft connection.
(2), in flow process, the concentrated solution of generator 1 enters the 3rd absorber 25 through solution heat exchanger 11, absorbs cryogen steaming Vapour heat release enter second in cooling medium, the weak solution of the 3rd absorber 25 through solution pump 10 and the second solution heat exchanger 12 Absorber 17；The concentrated solution of the 3rd generator 16 enters the 4th generator 22 through the second solution heat exchanger 12, heat absorption discharges cold Agent steam also provides to the 3rd absorber 25, and the concentrated solution of the 4th generator 22 is through the 3rd solution pump 23 and the 4th solution heat exchange Device 24 enters absorber 3, and the weak solution of absorber 3 enters generator through the 4th solution heat exchanger 24 and solution heat exchanger 11 1；The part cryogen liquid of the second condenser 5 flows through generator 1 and the 4th generator 22 progressively heat release successively, flows through throttling afterwards Valve 7 reducing pressure by regulating flow enters vaporizer 6, forms the 4th class thermal drivers compressing-absorbing type heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Figure 15 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 1, increase the 3rd generator, second Absorber, the second solution pump and the 3rd solution heat exchanger, have refrigerant steam channel and the second condenser 5 by the second generator 2 Connection is adjusted to the second generator 2 has refrigerant steam channel to connect with the second absorber 17, and the second absorber 17 also has weak solution Pipeline connects with the 3rd generator 16 with the 3rd solution heat exchanger 19 through the second solution pump 18, and the 3rd generator 16 also has dense molten Liquid pipeline connects with the second absorber 17 through the 3rd solution heat exchanger 19, and the 3rd generator 16 also has refrigerant steam channel and the Two condensers 5 connect, and the 3rd generator 16 also has high temperature thermal medium passage and ft connection, and the second absorber 17 also has heated Medium channel and ft connection.
(2), in flow process, the refrigerant vapour that the second generator 2 produces enters the second absorber 17, the second absorber 17 dilute Solution enters the 3rd generator 16 through the second solution pump 18 and the 3rd solution heat exchanger 19, and high temperature thermal medium flows through the 3rd generation Device 16, heating enter its interior solution release refrigerant vapour and provide to the second condenser 5, the concentrated solution warp of the 3rd generator 16 3rd solution heat exchanger 19 enters the second absorber 17, absorbs refrigerant vapour heat release in heated medium, formation the 4th class Thermal drivers compressing-absorbing type heat pump.
The 4th class thermal drivers compressing-absorbing type heat that effect that the technology of the present invention can realize is proposed by the invention Pump, has the effect that and advantage:
(1) new approaches and new technique that the temperature difference utilizes are proposed.
(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 corresponding with thermodynamic parameter change, it is possible to realize heat energy (temperature difference) Fully and efficiently utilize.
(4) if desired, realizing heat supply/refrigeration by external impetus, mode is flexible, and adaptability is good.
(5) refrigerant medium and solution there is wider subject range.
(6) effective utilization of high temperature heat is realized, it is to avoid conflicting between high temperature thermal medium parameter and solution property, make up The deficiency of absorption heat pump technology.
(7) effective utilization of low temperature heat energy is realized, it is to avoid conflicting between low-temperature heat medium parameter and solution property, make up The deficiency of absorption heat pump technology.
(8) compare thermal drivers compression heat pump, use absorption heat pump flow process to complete refrigerant vapour boosting, reduce motion portion Part, improves device security, reduces environmentally undesirable impact.
(9) multiple concrete technical scheme is provided, it is possible to tackle numerous different actual state, have the wider scope of application.
(10) extend heat pump techniques, enrich the type of compressing-absorbing type heat pump, be conducive to that heat energy is better achieved high Effect utilizes.

Claims (26)

1. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by generator, the second generator, absorber, condenser, second Condenser, vaporizer, choke valve, cryogen liquid pump, the second cryogen liquid pump, solution pump, solution heat exchanger, the second solution heat exchange Device, high-temperature heat exchanger, decompressor and compressor are formed；Generator (1) has concentrated solution pipeline through solution pump (10), solution heat Exchanger (11) connects with the second generator (2) with the second solution heat exchanger (12), and the second generator (2) also has concentrated solution pipe Road the second solution heat exchanger (12) connects with absorber (3), and absorber (3) also has weak solution pipeline through solution heat exchanger (11) connecting with generator (1), generator (1) also has refrigerant steam channel to connect with condenser (4), and condenser (4) is the coldest Agent liquid pipeline connects with vaporizer (6) through cryogen liquid pump (8), and the second generator (2) also has refrigerant steam channel and the second condensation Device (5) connects, and the second condenser (5) also has cryogen liquid pipeline to connect with vaporizer (6) with choke valve (7) through generator (1), the Two condensers (5) also have cryogen liquid pipeline high-temperature hot after the second cryogen liquid pump (9) connects with high-temperature heat exchanger (13) to hand over Parallel operation (13) has refrigerant steam channel to connect with decompressor (14) again, and decompressor (14) also has refrigerant steam channel and absorber (3) or condenser (4) connection, vaporizer (6) also have refrigerant steam channel connect with compressor (15), compressor (15) is the coldest Agent steam channel connects with absorber (3), and the second generator (2) and high-temperature heat exchanger (13) have high temperature thermal medium to lead to the most respectively Road and ft connection, absorber (3) and the second condenser (5) have heated medium passage and ft connection, vaporizer the most respectively (6) also having low-temperature heat medium passage and ft connection, condenser (4) also has coolant guiding channel and ft connection, decompressor (14) connect compressor (15) and transmit power, forming the 4th class thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor (14) connect compressor (15), cryogen liquid pump (8), the second cryogen liquid pump (9) and solution pump (10) and transmit power.
2. the 4th class thermal drivers compressing-absorbing type heat pump, is at the 4th class thermal drivers compressing-absorbing type described in claim 1 In heat pump, increase the 3rd generator, the second absorber, the second solution pump and the 3rd solution heat exchanger, generator (1) is had dense Solution line is through solution pump (10), solution heat exchanger (11) and the second solution heat exchanger (12) with the second generator (2) even Logical it be adjusted to generator (1) and have concentrated solution pipeline through solution pump (10), solution heat exchanger (11) and the second solution heat exchanger (12) connecting with the second absorber (17), the second absorber (17) has weak solution pipeline molten through the second solution pump (18) and the 3rd again Liquid heat exchanger (19) connects with the second generator (2), and the second generator (2) is had concentrated solution pipeline through the second solution heat exchange Device (12) connect with absorber (3) be adjusted to the second generator (2) have concentrated solution pipeline through the 3rd solution heat exchanger (19) with 3rd generator (16) connection, the 3rd generator (16) has concentrated solution pipeline again through the second solution heat exchanger (12) and absorber (3) connection, the 3rd generator (16) also has refrigerant steam channel to connect with the second absorber (17), and the 3rd generator (16) also has High temperature thermal medium passage and ft connection, the second absorber (17) also has heated medium passage and ft connection, forms the 4th Class thermal drivers compressing-absorbing type heat pump.
3. the 4th class thermal drivers compressing-absorbing type heat pump, be described in claim 1-2 arbitrary 4th class thermal drivers compression- In absorption heat pump, cancel choke valve, the second condenser (5) has cryogen liquid pipeline through generator (1) and choke valve (7) and steam Send out device (6) connection to be adjusted to the second condenser (5) and have cryogen liquid pipeline to connect with vaporizer (6) through generator (1), formation the 4th Class thermal drivers compressing-absorbing type heat pump.
4. the 4th class thermal drivers compressing-absorbing type heat pump, is at the 4th class thermal drivers compressing-absorbing type described in claim 1 In heat pump, increase the 3rd generator, second throttle, the second solution pump, the 3rd solution heat exchanger and heater, generator (1) concentrated solution pipeline is set up through the second solution pump (18), solution heat exchanger (11) and the 3rd solution heat exchanger (19) and the Three generators (16) connect, and the 3rd generator (16) also has concentrated solution pipeline through the 3rd solution heat exchanger (19) and absorber (3) connection, has the second generator (2) refrigerant steam channel to connect with the second condenser (5) and is adjusted to the second generator (2) and has Refrigerant steam channel connect with the 3rd generator (16) after the 3rd generator (16) have again cryogen liquid pipeline through heater (21), Generator (1) connects with vaporizer (6) with second throttle (20), and the 3rd generator (16) also has refrigerant steam channel and second Condenser (5) connects, and heater (21) also has heated medium passage and ft connection, forms the 4th class thermal drivers compression-suction Receipts formula heat pump.
5. the 4th class thermal drivers compressing-absorbing type heat pump, is at the 4th class thermal drivers compressing-absorbing type described in claim 1 In heat pump, increase the 3rd generator, second throttle, the 3rd solution heat exchanger and heater, generator (1) is had concentrated solution Pipeline connects tune with the second solution heat exchanger (12) with the second generator (2) through solution pump (10), solution heat exchanger (11) Whole for generator (1) have concentrated solution pipeline through solution pump (10), solution heat exchanger (11), the second solution heat exchanger (12) and 3rd solution heat exchanger (19) connects with the second generator (2), and the second generator (2) is had concentrated solution pipeline through the second solution Heat exchanger (12) connects with absorber (3) and is adjusted to the second generator (2) and has concentrated solution pipeline through the 3rd solution heat exchanger (19) connect with the 3rd generator (16), the 3rd generator (16) have again concentrated solution pipeline through the second solution heat exchanger (12) with Absorber (3) connects, and the second generator (2) has refrigerant steam channel connect with the second condenser (5) and is adjusted to the second generation After device (2) has refrigerant steam channel to connect with the 3rd generator (16), the 3rd generator (16) has cryogen liquid pipeline again through heat supply Device (21), generator (1) connect with vaporizer (6) with second throttle (20), and the 3rd generator (16) also has refrigerant vapour to lead to Road and the second condenser (5) connection, heater (21) also has heated medium passage and ft connection, forms the 4th class thermal drivers Compressing-absorbing type heat pump.
6. the 4th class thermal drivers compressing-absorbing type heat pump, is at the 4th class thermal drivers compressing-absorbing type described in claim 1 In heat pump, increase the 3rd generator, second throttle, the second solution pump, the 3rd solution heat exchanger and heater, by generator (1) concentrated solution pipeline is had to occur with second through solution pump (10), solution heat exchanger (11) and the second solution heat exchanger (12) Device (2) connection is adjusted to generator (1) has concentrated solution pipeline through solution pump (10), solution heat exchanger (11) and the second solution heat Exchanger (12) connects with the 3rd generator (16), the 3rd generator (16) have concentrated solution pipeline through the second solution pump (18) again and 3rd solution heat exchanger (19) connects with the second generator (2), and the second generator (2) is had concentrated solution pipeline through the second solution Heat exchanger (12) connects with absorber (3) and is adjusted to the second generator (2) and has concentrated solution pipeline through the 3rd solution heat exchanger (19) with the second solution heat exchanger (12) connects with absorber (3), and the second generator (2) is had refrigerant steam channel and second Condenser (5) connection is adjusted to after the second generator (2) has refrigerant steam channel to connect with the 3rd generator (16) the 3rd Raw device (16) has cryogen liquid pipeline to connect with vaporizer (6) with second throttle (20) through heater (21), generator (1) again, 3rd generator (16) also has refrigerant steam channel to connect with the second condenser (5), and heater (21) also has heated medium to lead to Road and ft connection, form the 4th class thermal drivers compressing-absorbing type heat pump.
7. the 4th class thermal drivers compressing-absorbing type heat pump, is at the 4th class thermal drivers compressing-absorbing type described in claim 2 In heat pump, increasing the 4th generator, second throttle, the 3rd solution pump, the 4th solution heat exchanger and heater, second absorbs Device (17) is set up weak solution pipeline and is connected with the 4th generator (22) through the 3rd solution pump (23) and the 4th solution heat exchanger (24) Logical, the 4th generator (22) also has concentrated solution pipeline to connect with the 3rd generator (16) through the 4th solution heat exchanger (24), will Second generator (2) have refrigerant steam channel connect with the second condenser (5) be adjusted to the second generator (2) have refrigerant vapour lead to After road and the connection of the 4th generator (22), the 4th generator (22) has cryogen liquid pipeline again through heater (21), generator (1) Connecting with vaporizer (6) with second throttle (20), the 4th generator (22) also has refrigerant steam channel and the second condenser (5) Connection, heater (21) also has heated medium passage and ft connection, forms the 4th class thermal drivers compressing-absorbing type heat pump.
8. the 4th class thermal drivers compressing-absorbing type heat pump, is at the 4th class thermal drivers compressing-absorbing type described in claim 2 In heat pump, increase the 4th generator, second throttle, the 4th solution heat exchanger and heater, the second absorber (17) is had Weak solution pipeline connects with the second generator (2) through the second solution pump (18) and the 3rd solution heat exchanger (19) and is adjusted to second Absorber (17) has weak solution pipeline through the second solution pump (18), the 3rd solution heat exchanger (19) and the 4th solution heat exchanger (24) connect with the second generator (2), the second generator (2) is had concentrated solution pipeline through the 3rd solution heat exchanger (19) and the Three generators (16) connection be adjusted to the second generator (2) have concentrated solution pipeline through the 4th solution heat exchanger (24) with the 4th Raw device (22) connection, the 4th generator (22) has concentrated solution pipeline again through the 3rd solution heat exchanger (19) and the 3rd generator (16) connection, has the second generator (2) refrigerant steam channel to connect with the second condenser (5) and is adjusted to the second generator (2) After having refrigerant steam channel to connect with the 4th generator (22), the 4th generator (22) has cryogen liquid pipeline again through heater (21), generator (1) connect with vaporizer (6) with second throttle (20), the 4th generator (22) also have refrigerant steam channel Connecting with the second condenser (5), heater (21) also has heated medium passage and ft connection, forms the 4th class thermal drivers pressure Contracting-absorption heat pump.
9. the 4th class thermal drivers compressing-absorbing type heat pump, is at the 4th class thermal drivers compressing-absorbing type described in claim 2 In heat pump, increase the 4th generator, second throttle, the 3rd solution pump, the 4th solution heat exchanger and heater, inhale second Receiving device (17) has weak solution pipeline to connect with the second generator (2) with the 3rd solution heat exchanger (19) through the second solution pump (18) It is adjusted to the second absorber (17) and has weak solution pipeline through the second solution pump (18) and the 3rd solution heat exchanger (19) and the 4th Generator (22) connects, and the 4th generator (22) has concentrated solution pipeline again through the 3rd solution pump (23) and the 4th solution heat exchanger (24) connect with the second generator (2), the second generator (2) is had concentrated solution pipeline through the 3rd solution heat exchanger (19) and the Three generators (16) connection is adjusted to the second generator (2) has concentrated solution pipeline molten through the 4th solution heat exchanger (24) and the 3rd Liquid heat exchanger (19) connects with the 3rd generator (16), and the second generator (2) has refrigerant steam channel and the second condenser (5) connection is adjusted to the 4th generator after the second generator (2) has refrigerant steam channel to connect with the 4th generator (22) (22) cryogen liquid pipeline is had to connect with vaporizer (6) with second throttle (20) through heater (21), generator (1) again, the 4th Generator (22) also has refrigerant steam channel connect with the second condenser (5), heater (21) also heated medium passage and Ft connection, forms the 4th class thermal drivers compressing-absorbing type heat pump.
10. the 4th class thermal drivers compressing-absorbing type heat pump, be described in claim 4-6 arbitrary 4th class thermal drivers compression- Absorption heat pump, the 3rd generator (16) is set up high temperature thermal medium passage and ft connection, is formed the 4th class thermal drivers compression-suction Receipts formula heat pump.
11. the 4th class thermal drivers compressing-absorbing type heat pumps, be described in claim 7-9 arbitrary 4th class thermal drivers compression- Absorption heat pump, the 4th generator (22) is set up high temperature thermal medium passage and ft connection, is formed the 4th class thermal drivers compression-suction Receipts formula heat pump.
12. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the arbitrary 4th class thermal drivers pressure described in claim 4-11 Contracting-absorption heat pump, cancels choke valve and second throttle, generator (1) has cryogen liquid pipeline through choke valve (7) and evaporation Device (6) connection is adjusted to generator (1) has cryogen liquid pipeline to connect with vaporizer (6), and generator (1) is had cryogen liquid pipeline warp Second throttle (20) connects with vaporizer (6) and is adjusted to generator (1) and has cryogen liquid pipeline to connect with vaporizer (6), is formed 4th class thermal drivers compressing-absorbing type heat pump.
13. the 4th class thermal drivers compressing-absorbing type heat pumps, are at the 4th class thermal drivers compressing-absorbing type described in claim 1 In heat pump, increase the 3rd generator, the second absorber, the second solution pump and the 3rd solution heat exchanger, generator (1) is had dense Solution line is through solution pump (10), solution heat exchanger (11) and the second solution heat exchanger (12) with the second generator (2) even Logical it be adjusted to generator (1) and have concentrated solution pipeline to connect with the second absorber (17) through solution heat exchanger (11), the second absorption Device (17) has weak solution pipeline to connect with the second generator (2) with the second solution heat exchanger (12) through solution pump (10) again, will Second generator (2) has concentrated solution pipeline to connect with absorber (3) through the second solution heat exchanger (12) to be adjusted to the second generation Device (2) has concentrated solution pipeline to connect with the 3rd generator (16) through the second solution heat exchanger (12), and the 3rd generator (16) is again Concentrated solution pipeline is had to connect with absorber (3) with the 3rd solution heat exchanger (19) through the second solution pump (18), by absorber (3) Have weak solution pipeline to connect with generator (1) through solution heat exchanger (11) to be adjusted to absorber (3) and have weak solution pipeline through Three solution heat exchangers (19) connect with generator (1) with solution heat exchanger (11), and the second condenser (5) is had cryogen liquid pipe Road connects with vaporizer (6) through generator (1) and choke valve (7) and is adjusted to the second condenser (5) and has cryogen liquid pipeline through occurring Device (1), the 3rd generator (16) connect with vaporizer (6) with choke valve (7), and the 3rd generator (16) also has refrigerant steam channel Connecting with the second absorber (17), the second absorber (17) also has coolant guiding channel and ft connection, forms the 4th class heat and drives Dynamic pressure contracting-absorption heat pump.
14. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the 4th class thermal drivers compression-absorption described in claim 13 In formula heat pump, cancel choke valve, have cryogen liquid pipeline to connect tune through choke valve (7) with vaporizer (6) in the 3rd generator (16) Whole is that the 3rd generator (16) has cryogen liquid pipeline to connect with vaporizer (6), forms the 4th class thermal drivers compressing-absorbing type heat Pump.
15. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the 4th class thermal drivers compression-absorption described in claim 13 In formula heat pump, increasing the 4th generator, second throttle, the 3rd solution pump, the 4th solution heat exchanger and heater, second inhales Receive device (17) and set up weak solution pipeline through the 3rd solution pump (23) and the 4th solution heat exchanger (24) and the 4th generator (22) Connection, the 4th generator (22) also has concentrated solution pipeline to connect with the 3rd generator (16) through the 4th solution heat exchanger (24), Second generator (2) has refrigerant steam channel connect with the second condenser (5) be adjusted to the second generator (2) and have refrigerant vapour After passage and the connection of the 4th generator (22), the 4th generator (22) has cryogen liquid pipeline again through heater (21), generator (1), the 3rd generator (16) connect with vaporizer (6) with second throttle (20), the 4th generator (22) also have refrigerant vapour Passage and the second condenser (5) connection, heater (21) also has heated medium passage and ft connection, forms the 4th class heat and drives Dynamic pressure contracting-absorption heat pump.
16. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the 4th class thermal drivers compression-absorption described in claim 13 In formula heat pump, increase the 4th generator, second throttle, the 4th solution heat exchanger and heater, by the second absorber (17) There is weak solution pipeline to connect with the second generator (2) through solution pump (10) and the second solution heat exchanger (12) and be adjusted to the second suction Receive device (17) have weak solution pipeline through solution pump (10), the second solution heat exchanger (12) and the 4th solution heat exchanger (24) and Second generator (2) connects, and the second generator (2) has concentrated solution pipeline occur with the 3rd through the second solution heat exchanger (12) Device (16) connection is adjusted to the second generator (2) has concentrated solution pipeline through the 4th solution heat exchanger (24) and the 4th generator (22) connection, the 4th generator (22) has concentrated solution pipeline through the second solution heat exchanger (12) with the 3rd generator (16) even again Logical, the second generator (2) has refrigerant steam channel connect with the second condenser (5) and is adjusted to the second generator (2) and has cryogen After steam channel and the connection of the 4th generator (22), the 4th generator (22) has cryogen liquid pipeline through heater (21) again, occurs Device (1), the 3rd generator (16) connect with vaporizer (6) with second throttle (20), and the 4th generator (22) also has cryogen to steam Vapour passage and the second condenser (5) connection, heater (21) also has heated medium passage and ft connection, forms the 4th class heat Drive compression-absorption heat pump.
17. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the 4th class thermal drivers compression-absorption described in claim 13 In formula heat pump, increase the 4th generator, second throttle, the 3rd solution pump, the 4th solution heat exchanger and heater, by second Absorber (17) has weak solution pipeline to connect tune with the second solution heat exchanger (12) with the second generator (2) through solution pump (10) Whole is that the second absorber (17) has weak solution pipeline through solution pump (10) and the second solution heat exchanger (12) and the 4th generator (22) connection, the 4th generator (22) have concentrated solution pipeline through the 3rd solution pump (23) and the 4th solution heat exchanger (24) again and Second generator (2) connects, and the second generator (2) has concentrated solution pipeline occur with the 3rd through the second solution heat exchanger (12) Device (16) connection is adjusted to the second generator (2) has concentrated solution pipeline to hand over through the 4th solution heat exchanger (24) and the second solution heat Parallel operation (12) connects with the 3rd generator (16), has refrigerant steam channel to connect with the second condenser (5) in the second generator (2) It is adjusted to the 4th generator (22) after the second generator (2) has refrigerant steam channel to connect with the 4th generator (22) and has cold again Agent liquid pipeline connects with vaporizer (6) with second throttle (20) through heater (21), generator (1), the 3rd generator (16), 4th generator (22) also has refrigerant steam channel to connect with the second condenser (5), and heater (21) also has heated medium to lead to Road and ft connection, form the 4th class thermal drivers compressing-absorbing type heat pump.
18. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the arbitrary 4th class thermal drivers pressure described in claim 15-17 Contracting-absorption heat pump, the 4th generator (22) is set up high temperature thermal medium passage and ft connection, is formed the 4th class thermal drivers pressure Contracting-absorption heat pump.
19. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the arbitrary 4th class thermal drivers pressure described in claim 15-18 In contracting-absorption heat pump, cancel choke valve and second throttle, the 3rd generator (16) is had cryogen liquid pipeline through choke valve (7) connect with vaporizer (6) and be adjusted to the 3rd generator (16) and have cryogen liquid pipeline to connect with vaporizer (6), occur the 3rd Device (16) has cryogen liquid pipeline to connect with vaporizer (6) through second throttle (20) to be adjusted to the 3rd generator (16) and have cryogen liquid Pipeline connects with vaporizer (6), forms the 4th class thermal drivers compressing-absorbing type heat pump.
20. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the 4th class thermal drivers compression-absorption arbitrary described in claim 2 In formula heat pump, increase the 4th generator, the 3rd absorber, the 3rd solution pump and the 4th solution heat exchanger, generator (1) is had Concentrated solution pipeline is through solution pump (10), solution heat exchanger (11) and the second solution heat exchanger (12) and the second absorber (17) Connection is adjusted to generator (1) has concentrated solution pipeline to connect with the 3rd absorber (25) through solution heat exchanger (11), and the 3rd inhales Receiving device (25) has weak solution pipeline to connect with the second absorber (17) with the second solution heat exchanger (12) through solution pump (10) again, 3rd generator (16) has concentrated solution pipeline connect with absorber (3) through the second solution heat exchanger (12) and is adjusted to the 3rd Raw device (16) has concentrated solution pipeline to connect with the 4th generator (22) through the second solution heat exchanger (12), the 4th generator (22) Concentrated solution pipeline is had to connect with absorber (3) with the 4th solution heat exchanger (24), by absorber through the 3rd solution pump (23) again (3) have weak solution pipeline to connect with generator (1) through solution heat exchanger (11) to be adjusted to absorber (3) and have weak solution pipeline warp 4th solution heat exchanger (24) connects with generator (1) with solution heat exchanger (11), and the second condenser (5) is had cryogen liquid Pipeline connects with vaporizer (6) through generator (1) and choke valve (7) and is adjusted to the second condenser (5) and has cryogen liquid pipeline through sending out Raw device (1), the 4th generator (22) connect with vaporizer (6) with choke valve (7), and the 4th generator (22) also has refrigerant vapour to lead to Road and the connection of the 3rd absorber (25), the 3rd absorber (25) also has coolant guiding channel and ft connection, forms the 4th class heat Drive compression-absorption heat pump.
21. the 4th class thermal drivers compressing-absorbing type heat pumps, be described in claim 20 arbitrary 4th class thermal drivers compression- In absorption heat pump, cancel choke valve, the 4th generator (22) has cryogen liquid pipeline through choke valve (7) with vaporizer (6) even Logical it be adjusted to the 4th generator (22) and have cryogen liquid pipeline to connect with vaporizer (6), formation the 4th class thermal drivers compressing-absorbing type Heat pump.
22. the 4th class thermal drivers compressing-absorbing type heat pumps, are at the 4th class thermal drivers compressing-absorbing type described in claim 1 In heat pump, increase the 3rd generator, the second absorber, the second solution pump and the 3rd solution heat exchanger, by the second generator (2) Have refrigerant steam channel connect with the second condenser (5) be adjusted to the second generator (2) have refrigerant steam channel with second absorb Device (17) connects, and the second absorber (17) also has weak solution pipeline through the second solution pump (18) and the 3rd solution heat exchanger (19) Connecting with the 3rd generator (16), the 3rd generator (16) also has concentrated solution pipeline through the 3rd solution heat exchanger (19) and second Absorber (17) connects, and the 3rd generator (16) also has refrigerant steam channel to connect with the second condenser (5), the 3rd generator (16) also having high temperature thermal medium passage and ft connection, the second absorber (17) also has heated medium passage and ft connection, Form the 4th class thermal drivers compressing-absorbing type heat pump.
23. the 4th class thermal drivers compressing-absorbing type heat pumps, are at the 4th class thermal drivers compressing-absorbing type described in claim 22 In heat pump, cancel choke valve, generator (1) has cryogen liquid pipeline connect with vaporizer (6) through choke valve (7) and is adjusted to generation Device (1) has cryogen liquid pipeline to connect with vaporizer (6), forms the 4th class thermal drivers compressing-absorbing type heat pump.
24. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the arbitrary 4th class thermal drivers pressure described in claim 1-23 In contracting-absorption heat pump, decompressor (14) have refrigerant steam channel connect be adjusted to swollen with absorber (3) or condenser (4) Swollen machine (14) has refrigerant steam channel to connect with the second condenser (5), forms the 4th class thermal drivers compressing-absorbing type heat pump.
25. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the arbitrary 4th class thermal drivers pressure described in claim 1-24 In contracting-absorption heat pump, increasing engine, engine connects compressor (15) and transmits power to compressor (15), is formed attached Add the 4th class thermal drivers compressing-absorbing type heat pump that external impetus drives.
26. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the arbitrary 4th class thermal drivers pressure described in claim 1-24 In contracting-absorption heat pump, increasing working machine, decompressor (14) connects working machine and transmits power to working machine, and it is additional right to be formed 4th class thermal drivers compressing-absorbing type heat pump of outer offer living load.
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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112944722A (en) * 2020-02-21 2021-06-11 李华玉 Absorption-compression heat pump of the third kind and absorption-compression heat pump of the fourth kind
CN115200255A (en) * 2020-03-02 2022-10-18 李华玉 Thermally driven compression-absorption heat pump
CN115218548A (en) * 2020-03-01 2022-10-21 李华玉 Compression-absorption heat pump
CN115218537A (en) * 2020-02-21 2022-10-21 李华玉 Third and fourth class thermally driven absorption-compression heat pumps
CN115218528A (en) * 2020-02-21 2022-10-21 李华玉 Third-class absorption heat pump and fourth-class absorption heat pump

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0893633A (en) * 1994-09-20 1996-04-09 Saga Univ Energy converter
JP2007120872A (en) * 2005-10-28 2007-05-17 Rinnai Corp Hybrid heat pump system
CN103542604A (en) * 2013-10-28 2014-01-29 刘辉 Backheating typed fourth heat pump cycle
CN104833128A (en) * 2014-04-07 2015-08-12 李华玉 Fourth type absorption heat pump

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0893633A (en) * 1994-09-20 1996-04-09 Saga Univ Energy converter
JP2007120872A (en) * 2005-10-28 2007-05-17 Rinnai Corp Hybrid heat pump system
CN103542604A (en) * 2013-10-28 2014-01-29 刘辉 Backheating typed fourth heat pump cycle
CN104833128A (en) * 2014-04-07 2015-08-12 李华玉 Fourth type absorption heat pump

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112944722A (en) * 2020-02-21 2021-06-11 李华玉 Absorption-compression heat pump of the third kind and absorption-compression heat pump of the fourth kind
CN115218537A (en) * 2020-02-21 2022-10-21 李华玉 Third and fourth class thermally driven absorption-compression heat pumps
CN115218528A (en) * 2020-02-21 2022-10-21 李华玉 Third-class absorption heat pump and fourth-class absorption heat pump
CN115218548A (en) * 2020-03-01 2022-10-21 李华玉 Compression-absorption heat pump
CN115200255A (en) * 2020-03-02 2022-10-18 李华玉 Thermally driven compression-absorption heat pump

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