CN106403367A - Fourth thermally-driven compression-absorption type heat pump - Google Patents

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

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Publication number
CN106403367A
CN106403367A CN201610822833.5A CN201610822833A CN106403367A CN 106403367 A CN106403367 A CN 106403367A CN 201610822833 A CN201610822833 A CN 201610822833A CN 106403367 A CN106403367 A CN 106403367A
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generator
solution
heat exchanger
pump
connect
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CN106403367B (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

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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 thermally-driven compression-absorption type heat pump, and belongs to the technical field of power, refrigeration and heat pumps. An absorber, a generator, a second generator, a solution pump, a second solution pump, a solution heat exchanger and a second solution heat exchanger form a solution loop, the generator is provided with a refrigerant steam channel communicating with a condenser, the second generator is provided with a refrigerant steam channel communicating with a second condenser, the condenser communicates with an evaporator through the second generator and a throttling valve and communicates with a high temperature heat exchanger, an expansion machine and the evaporator through a refrigerant liquid pump, the second condenser communicates with the evaporator through a second refrigerant liquid pump, the evaporator communicates with the absorber through a refrigerant steam channel, a low-temperature thermal medium channel arranged externally communicates with a compressor, the evaporator and a second expansion machine, the generator, the high temperature heat exchanger, the absorber, the condenser and the second condenser are respectively provided with a medium channel communicating with the exterior, the expansion machine and the second expansion machine are connected to the compressor and transmit power, and therefore the fourth thermally-driven compression-absorption type 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 common by human lives；In reality, people often need To realize refrigeration, heat supply using high temperature heat or be converted into power it is also desirable to being freezed using power or being utilized power And carry out heat supply with reference to low temperature heat energy.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 security that equipment runs, acceptable degree of environment temperature and environment etc..
Heat energy (temperature difference) with absorption heat pump technology as representative utilizes technology, is driven using high warm load and realizes heat supply Or refrigeration；Property by working media (solution and refrigerant medium) is affected, the high warm load of excessive temperature or excessively low temperature Low temperature thermic load often cannot reasonably be applied in absorption heat pump flow process, lead to its application and range of application to be subject to Larger restriction.Compression heat pump technology has preferable flexibility in terms of thermodynamic property, but the core of compression heat pump Part is that moving component has higher security it is desirable to equipment runs, and also will manage noise of reduction equipment operation etc.；For this reason, needing 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 power demand, the present invention are externally provided Propose to comprise cryogen liquid pump, decompressor, compressor, the second decompressor and high-temperature heat exchanger or add low temperature heat exchanger group The temperature difference becoming utilizes link, and comprises cryogen liquid pump, decompressor, compressor, cryogenic throttle valve and low temperature heat exchanger composition The temperature difference utilize link, the temperature difference between high temperature heat source and heated medium is carried out effectively utilizes or to high temperature heat source and environment it Between the temperature difference carry out effectively utilizes, there is the 4th class thermal drivers compressing-absorbing type heat pump of comprehensive advantage.
Content of the invention：
Present invention is primarily intended to serial 4th class thermal drivers compressing-absorbing type heat pump will be provided, concrete content of the invention divides Item is described below：
1. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, the second generator, condenser, Second condenser, evaporimeter, choke valve, cryogen liquid pump, the second cryogen liquid pump, solution pump, the second solution pump, solution heat exchange Device, the second solution heat exchanger, high-temperature heat exchanger, decompressor, compressor and the second decompressor are formed；Absorber has dilute molten Liquid pipeline is connected with generator with solution heat exchanger through solution pump, generator also have concentrated solution pipeline through solution heat exchanger and Second solution heat exchanger is connected with the second generator, and the second generator also has concentrated solution pipeline molten through the second solution pump and second Liquid heat exchanger is connected with absorber, and generator also has refrigerant steam channel to connect with condenser, and the second generator also has cryogen Steam channel is connected with the second condenser, and condenser also has cryogen liquid pipeline to connect with evaporimeter through the second generator and choke valve Logical, after condenser also has cryogen liquid pipeline to connect with high-temperature heat exchanger through cryogen liquid pump, high-temperature heat exchanger has cryogen to steam again Vapour passage is connected with decompressor, and decompressor also has refrigerant steam channel to connect with evaporimeter or the second condenser, the second condenser Cryogen liquid pipeline is also had to connect with evaporimeter through the second cryogen liquid pump, evaporimeter also has refrigerant steam channel to connect with absorber, Outside has low-temperature heat medium passage to connect with compressor, and compressor also has low-temperature heat medium passage through evaporimeter and the second decompressor Connection, the second decompressor also has low-temperature heat medium passage and ft connection, generator and high-temperature heat exchanger also to have high temperature respectively Hot media channel and ft connection, absorber and condenser also have heated medium passage and ft connection, the second condensation respectively Device also has low-temperature heat medium passage and ft connection, and decompressor and the second decompressor connect compressor and transmit power, forms the Four class thermal drivers compressing-absorbing type heat pumps；Wherein, or decompressor and the second decompressor connect compressor, cryogen liquid pump, second cold Agent liquid pump, solution pump and the second solution pump simultaneously transmit power.
2. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, the second generator, condenser, Second condenser, evaporimeter, choke valve, cryogen liquid pump, the second cryogen liquid pump, solution pump, the second solution pump, solution heat exchange Device, the second solution heat exchanger, high-temperature heat exchanger, decompressor, compressor, the second decompressor and the second compressor are formed； Absorber has weak solution pipeline to connect with generator with solution heat exchanger through solution pump, and generator also has concentrated solution pipeline through molten Liquid heat exchanger and the second solution heat exchanger are connected with the second generator, and the second generator also has concentrated solution pipeline molten through second Liquid pump and the second solution heat exchanger are connected with absorber, and generator also has refrigerant steam channel to connect with condenser, second Raw device also has refrigerant steam channel to connect with the second condenser, and condenser also has cryogen liquid pipeline through the second generator and choke valve Connect with evaporimeter, condenser also have cryogen liquid pipeline to connect with high-temperature heat exchanger through cryogen liquid pump after high-temperature heat exchanger Refrigerant steam channel is had to connect with decompressor again, decompressor also has refrigerant steam channel to connect with evaporimeter or the second condenser, Second condenser also has cryogen liquid pipeline to connect with evaporimeter through the second cryogen liquid pump, and evaporimeter also has refrigerant steam channel and suction Receive device connection, outside has low-temperature heat medium passage to connect with compressor, compressor also have low-temperature heat medium passage through evaporimeter and Second compressor connection, the second compressor also has low-temperature heat medium passage to connect with the second decompressor through evaporimeter, the second expansion Machine also has low-temperature heat medium passage and ft connection, generator and high-temperature heat exchanger also to have high temperature thermal medium passage respectively with outward Portion connects, and absorber and condenser also have heated medium passage and ft connection respectively, and the second condenser also has Low Temperature Thermal to be situated between Matter passage and ft connection, decompressor and the second decompressor connect compressor and the second compressor and transmit power, form the 4th Class thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor and the second decompressor connect compressor, the second compressor, cryogen liquid Pump, the second cryogen liquid pump, solution pump and the second solution pump simultaneously transmit power.
3. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, the second generator, condenser, Second condenser, evaporimeter, choke valve, cryogen liquid pump, the second cryogen liquid pump, solution pump, the second solution pump, solution heat exchange Device, the second solution heat exchanger, high-temperature heat exchanger, decompressor, compressor, the second decompressor and regenerator are formed；Absorb Device has weak solution pipeline to connect with generator with solution heat exchanger through solution pump, and generator also has concentrated solution pipeline through solution heat Exchanger and the second solution heat exchanger are connected with the second generator, and the second generator also has concentrated solution pipeline through the second solution pump Connect with absorber with the second solution heat exchanger, generator also has refrigerant steam channel to connect with condenser, the second generator Refrigerant steam channel is also had to connect with the second condenser, condenser also has cryogen liquid pipeline through the second generator and choke valve and steaming Send out device connection, after condenser also has cryogen liquid pipeline to connect with high-temperature heat exchanger through cryogen liquid pump there be again high-temperature heat exchanger Refrigerant steam channel is connected with decompressor, and decompressor also has refrigerant steam channel to connect with evaporimeter or the second condenser, and second Condenser also has cryogen liquid pipeline to connect with evaporimeter through the second cryogen liquid pump, and evaporimeter also has refrigerant steam channel and absorber Connection, outside has low-temperature heat medium passage to connect with compressor through regenerator, and compressor also has low-temperature heat medium passage through evaporation Device is connected with the second decompressor with regenerator, and the second decompressor also has low-temperature heat medium passage and ft connection, generator and height Temperature heat exchanger also has high temperature thermal medium passage and ft connection, absorber and condenser also to have heated medium to lead to respectively respectively Road and ft connection, the second condenser also has low-temperature heat medium passage and ft connection, decompressor and the second decompressor to connect pressure Contracting machine simultaneously transmits power, forms the 4th class thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor and the second decompressor connect Compressor, cryogen liquid pump, the second cryogen liquid pump, solution pump and the second solution pump simultaneously transmit power.
4. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, the second generator, condenser, Second condenser, evaporimeter, choke valve, cryogen liquid pump, the second cryogen liquid pump, solution pump, the second solution pump, solution heat exchange Device, the second solution heat exchanger, high-temperature heat exchanger, decompressor, compressor, the second decompressor and low temperature heat exchanger institute group Become；Absorber has weak solution pipeline to connect with generator with solution heat exchanger through solution pump, and generator also has concentrated solution pipeline Connect with the second generator through solution heat exchanger and the second solution heat exchanger, the second generator also has concentrated solution pipeline through Two solution pumps and the second solution heat exchanger are connected with absorber, and generator also has refrigerant steam channel to connect with condenser, the Two generators also have refrigerant steam channel to connect with the second condenser, and condenser also has cryogen liquid pipeline through the second generator and section Stream valve is connected with evaporimeter, condenser high warm friendship after also having cryogen liquid pipeline to connect with high-temperature heat exchanger through cryogen liquid pump Parallel operation has refrigerant steam channel to connect with decompressor again, and decompressor also has refrigerant steam channel to connect with evaporimeter or the second condenser Logical, the second condenser also has cryogen liquid pipeline to connect with evaporimeter through the second cryogen liquid pump, and evaporimeter also has refrigerant steam channel Connect with absorber, compressor has cycle fluid passage to connect with the second decompressor through evaporimeter, the second decompressor also has circulation Working medium passage is connected with compressor through low temperature heat exchanger, and generator and high-temperature heat exchanger also have high temperature thermal medium passage respectively With ft connection, absorber and condenser also have heated medium passage and ft connection, the second condenser and Low Temperature Thermal respectively Exchanger also has low-temperature heat medium passage and ft connection, decompressor and the second decompressor to connect compressor and transmit dynamic respectively Power, forms the 4th class thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor and the second decompressor connect compressor, cryogen liquid Pump, the second cryogen liquid pump, solution pump and the second solution pump simultaneously transmit power.
5. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, the second generator, condenser, Second condenser, evaporimeter, choke valve, cryogen liquid pump, the second cryogen liquid pump, solution pump, the second solution pump, solution heat exchange Device, the second solution heat exchanger, high-temperature heat exchanger, decompressor and compressor are formed；Absorber has weak solution pipeline through molten Liquid pump is connected with generator with solution heat exchanger, and generator also has concentrated solution pipeline through solution heat exchanger and the second solution heat Exchanger is connected with the second generator, and the second generator also has concentrated solution pipeline through the second solution pump and the second solution heat exchanger Connect with absorber, generator also has refrigerant steam channel to connect with condenser, the second generator also have refrigerant steam channel with Second condenser connection, condenser also has cryogen liquid pipeline to connect with evaporimeter with choke valve through the second generator, and condenser is also After having cryogen liquid pipeline to connect with high-temperature heat exchanger through cryogen liquid pump high-temperature heat exchanger have again refrigerant steam channel with swollen Swollen machine connection, decompressor also has refrigerant steam channel to connect with evaporimeter or the second condenser, and the second condenser also has cryogen liquid Pipeline is connected with evaporimeter through the second cryogen liquid pump, and evaporimeter also has refrigerant steam channel to connect with absorber, and there is low temperature outside Hot media channel is connected with compressor, and compressor also has low-temperature heat medium passage through evaporimeter and ft connection, generator and height Temperature heat exchanger also has high temperature thermal medium passage and ft connection, absorber and condenser also to have heated medium to lead to respectively respectively Road and ft connection, the second condenser also has low-temperature heat medium passage and ft connection, and decompressor connects compressor and transmits dynamic Power, forms the 4th class thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor connect compressor, cryogen liquid pump, the second cryogen Liquid pump, solution pump and the second solution pump simultaneously transmit power.
6. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, the second generator, condenser, Second condenser, evaporimeter, choke valve, cryogen liquid pump, the second cryogen liquid pump, solution pump, the second solution pump, solution heat exchange Device, the second solution heat exchanger, high-temperature heat exchanger, decompressor, compressor, low temperature heat exchanger and cryogenic throttle valve institute group Become；Absorber has weak solution pipeline to connect with generator with solution heat exchanger through solution pump, and generator also has concentrated solution pipeline Connect with the second generator through solution heat exchanger and the second solution heat exchanger, the second generator also has concentrated solution pipeline through Two solution pumps and the second solution heat exchanger are connected with absorber, and generator also has refrigerant steam channel to connect with condenser, the Two generators also have refrigerant steam channel to connect with the second condenser, and condenser also has cryogen liquid pipeline through the second generator and section Stream valve is connected with evaporimeter, condenser high warm friendship after also having cryogen liquid pipeline to connect with high-temperature heat exchanger through cryogen liquid pump Parallel operation has refrigerant steam channel to connect with decompressor again, and decompressor also has refrigerant steam channel to connect with evaporimeter or the second condenser Logical, the second condenser also has cryogen liquid pipeline to connect with evaporimeter through the second cryogen liquid pump, and evaporimeter also has refrigerant steam channel Connect with absorber, compressor has cycle fluid passage to connect with low temperature heat exchanger with cryogenic throttle valve through evaporimeter, low temperature Heat exchanger also has cycle fluid passage to connect with compressor, and generator and high-temperature heat exchanger also have high temperature thermal medium to lead to respectively Road and ft connection, absorber and condenser also have heated medium passage and ft connection, the second condenser and low temperature respectively Heat exchanger also has low-temperature heat medium passage and ft connection respectively, and decompressor connects compressor and transmits power, forms the 4th Class thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor connect compressor, cryogen liquid pump, the second cryogen liquid pump, solution pump With the second solution pump and transmit power.
7. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, the second generator, condenser, Second condenser, evaporimeter, choke valve, cryogen liquid pump, the second cryogen liquid pump, solution pump, the second solution pump, solution heat exchange Device, the second solution heat exchanger, high-temperature heat exchanger, decompressor, compressor, the second compressor, low temperature heat exchanger and low temperature Choke valve is formed；Absorber has weak solution pipeline to connect with generator with solution heat exchanger through solution pump, and generator also has Concentrated solution pipeline is connected with the second generator through solution heat exchanger and the second solution heat exchanger, and the second generator also has dense molten Liquid pipeline is connected with absorber through the second solution pump and the second solution heat exchanger, and generator also has refrigerant steam channel and condensation Device connects, and the second generator also has refrigerant steam channel to connect with the second condenser, and condenser also has cryogen liquid pipeline through second Generator is connected with evaporimeter with choke valve, and condenser also has cryogen liquid pipeline to connect it through cryogen liquid pump with high-temperature heat exchanger High-temperature heat exchanger has refrigerant steam channel to connect with decompressor more afterwards, and decompressor also has refrigerant steam channel and evaporimeter or the Two condenser connections, the second condenser also has cryogen liquid pipeline to connect with evaporimeter through the second cryogen liquid pump, and evaporimeter is also cold Agent steam channel is connected with absorber, and compressor has cycle fluid passage to connect with the second compressor through evaporimeter, the second compression Machine also has cycle fluid passage to connect with low temperature heat exchanger with cryogenic throttle valve through evaporimeter, and low temperature heat exchanger also has circulation Working medium passage is connected with compressor, and generator and high-temperature heat exchanger also have high temperature thermal medium passage and ft connection respectively, inhales Receive device and condenser also has heated medium passage and ft connection respectively, the second condenser and low temperature heat exchanger also have respectively Low-temperature heat medium passage and ft connection, decompressor connects compressor and the second compressor and transmits power, forms the 4th class heat Drive compression-absorption heat pump；Wherein, or decompressor connect compressor, the second compressor, cryogen liquid pump, the second cryogen liquid pump, Solution pump and the second solution pump simultaneously transmit power.
8. the 4th class thermal drivers compressing-absorbing type heat pump, be described in 1-7 item arbitrary 4th class thermal drivers compression- In absorption heat pump, increase the 3rd generator, the second absorber, the 3rd solution pump and the 3rd solution heat exchanger, by absorber There is weak solution pipeline to connect with generator through solution pump and solution heat exchanger to be adjusted to absorber and have weak solution pipeline through solution Pump is connected with the second absorber with solution heat exchanger, and the second absorber has weak solution pipeline molten through the 3rd solution pump and the 3rd again Liquid heat exchanger is connected with generator, by generator have concentrated solution pipeline through solution heat exchanger and the second solution heat exchanger with Second generator connection is adjusted to generator has concentrated solution pipeline to connect with the 3rd generator through the 3rd solution heat exchanger, and the 3rd Generator has concentrated solution pipeline to connect with the second generator through solution heat exchanger and the second solution heat exchanger again, the 3rd generation Device also has refrigerant steam channel to connect with the second absorber, and the 3rd generator also has high temperature thermal medium passage and ft connection, the Two absorbers also have heated 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, be described in 1-8 item arbitrary 4th class thermal drivers compression- In absorption heat pump, cancel choke valve, condenser is had cryogen liquid pipeline to connect with evaporimeter with choke valve through the second generator Being adjusted to condenser has cryogen liquid pipeline to connect with evaporimeter through the second generator, forms the 4th class thermal drivers compressing-absorbing type Heat pump.
10. the 4th class thermal drivers compressing-absorbing type heat pump, is arbitrary fourth class thermal drivers compression-suction described in 1-7 item In receipts formula heat pump, increase the 3rd generator, second throttle, the 3rd solution pump, the 3rd solution heat exchanger and heater, absorb Device is set up weak solution pipeline and is connected with the 3rd generator through the 3rd solution pump and the 3rd solution heat exchanger, and the 3rd generator also has Concentrated solution pipeline is connected with the second generator through the 3rd solution heat exchanger and the second solution heat exchanger, and generator is had cryogen Steam channel is connected with condenser and is adjusted to the 3rd generator after generator has refrigerant steam channel to connect with the 3rd generator Cryogen liquid pipeline is had to connect with evaporimeter with second throttle through heater, the second generator again, the 3rd generator also has cryogen Steam channel is connected with condenser, and heater also has heated medium passage and ft connection, formed the 4th class thermal drivers compression- Absorption heat pump.
11. the 4th class thermal drivers compressing-absorbing type heat pumps, are arbitrary fourth class thermal drivers compression-suctions described in 1-7 item In receipts formula heat pump, increase the 3rd generator, second throttle, the 3rd solution heat exchanger and heater, absorber is had dilute molten Liquid pipeline is connected with generator through solution pump and solution heat exchanger and is adjusted to absorber and has weak solution pipeline through solution pump, solution Heat exchanger and the 3rd solution heat exchanger are connected with generator, and generator is had concentrated solution pipeline through solution heat exchanger and Two solution heat exchangers are connected with the second generator and are adjusted to generator and have concentrated solution pipeline through the 3rd solution heat exchanger and Three generator connections, the 3rd generator has concentrated solution pipeline again through solution heat exchanger and the second solution heat exchanger and second Raw device connection, generator is had refrigerant steam channel to connect with condenser and is adjusted to generator and has refrigerant steam channel and the 3rd After raw device connection, the 3rd generator has cryogen liquid pipeline to connect through heater, the second generator and second throttle and evaporimeter again Logical, the 3rd generator also has refrigerant steam channel to connect with condenser, and heater also has heated medium passage and ft connection, Form the 4th class thermal drivers compressing-absorbing type heat pump.
12. the 4th class thermal drivers compressing-absorbing type heat pumps, are arbitrary fourth class thermal drivers compression-suctions described in 1-7 item In receipts formula heat pump, increase the 3rd generator, second throttle, the 3rd solution pump, the 3rd solution heat exchanger and heater, will inhale Receive device and have weak solution pipeline to connect with generator through solution pump and solution heat exchanger and be adjusted to absorber and have weak solution pipeline warp Solution pump is connected with the 3rd generator with solution heat exchanger, and the 3rd generator has concentrated solution pipeline again through the 3rd solution pump and Three solution heat exchangers are connected with generator, and generator is had concentrated solution pipeline through solution heat exchanger and the second solution heat exchange Device is connected with the second generator and is adjusted to generator and has concentrated solution pipeline through the 3rd solution heat exchanger, solution heat exchanger and Two solution heat exchangers are connected with the second generator, generator is had refrigerant steam channel to connect with condenser and is adjusted to generator After having refrigerant steam channel to connect with the 3rd generator, the 3rd generator has cryogen liquid pipeline again through heater, the second generator Connect with evaporimeter with second throttle, the 3rd generator also has refrigerant steam channel to connect with condenser, and heater also has quilt Heating medium passage and ft connection, form the 4th class thermal drivers compressing-absorbing type heat pump.
13. the 4th class thermal drivers compressing-absorbing type heat pumps, are the arbitrary 4th class thermal drivers compression-suctions described at the 8th In receipts formula heat pump, increase the 4th generator, second throttle, the 4th solution pump, the 4th solution heat exchanger and heater, second Absorber is set up weak solution pipeline and is connected with the 4th generator through the 4th solution pump and the 4th solution heat exchanger, the 4th generator Also have concentrated solution pipeline to connect with the 3rd generator through the 4th solution heat exchanger, generator is had refrigerant steam channel and condensation Device connection is adjusted to the 4th generator after generator has refrigerant steam channel to connect with the 4th generator cryogen liquid pipeline again Connect with evaporimeter with second throttle through heater, the second generator, the 4th generator also has refrigerant steam channel and condensation Device connects, and heater also has heated medium passage 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 arbitrary 4th class thermal drivers compression-suctions described at the 8th In receipts formula heat pump, increase the 4th generator, second throttle, the 4th solution heat exchanger and heater, the second absorber is had Weak solution pipeline is connected with generator through the 3rd solution pump and the 3rd solution heat exchanger and is adjusted to the second absorber and has weak solution Pipeline is connected with generator through the 3rd solution pump, the 3rd solution heat exchanger and the 4th solution heat exchanger, generator is had dense Solution line is connected with the 3rd generator through the 3rd solution heat exchanger and is adjusted to generator and has concentrated solution pipeline through the 4th solution Heat exchanger is connected with the 4th generator, and the 4th generator has concentrated solution pipeline again through the 3rd solution heat exchanger and the 3rd generation Device connects, and generator is had refrigerant steam channel to connect with condenser and is adjusted to generator and has refrigerant steam channel and the 4th generation After device connection, the 4th generator has cryogen liquid pipeline to connect through heater, the second generator and second throttle and evaporimeter again Logical, the 4th generator also has refrigerant steam channel to connect with condenser, and heater also has heated medium passage and ft connection, Form the 4th class thermal drivers compressing-absorbing type heat pump.
15. the 4th class thermal drivers compressing-absorbing type heat pumps, are the arbitrary 4th class thermal drivers compression-suctions described at the 8th In receipts formula heat pump, increase the 4th generator, second throttle, the 4th solution pump, the 4th solution heat exchanger and heater, by the Two absorbers have weak solution pipeline to connect with generator and be adjusted to the second absorption through the 3rd solution pump and the 3rd solution heat exchanger Device has weak solution pipeline to connect with the 4th generator through the 3rd solution pump and the 3rd solution heat exchanger, and the 4th generator has dense again Solution line is connected with generator through the 4th solution pump and the 4th solution heat exchanger, and generator is had concentrated solution pipeline through the 3rd Solution heat exchanger is connected with the 3rd generator and is adjusted to generator and has concentrated solution pipeline through the 4th solution heat exchanger and the 3rd Solution heat exchanger is connected with the 3rd generator, generator is had refrigerant steam channel to connect with condenser and is adjusted to generator and has Refrigerant steam channel connect with the 4th generator after the 4th generator have again cryogen liquid pipeline through heater, the second generator and Second throttle is connected with evaporimeter, and the 4th generator also has refrigerant steam channel to connect with condenser, and heater is also added Hot media channel and ft connection, form the 4th class thermal drivers compressing-absorbing type heat pump.
16. the 4th class thermal drivers compressing-absorbing type heat pumps, be 10-12 item described arbitrary 4th class thermal drivers compression- Absorption heat pump, the 3rd generator sets up high temperature thermal medium passage and ft connection, forms the 4th class thermal drivers compressing-absorbing type Heat pump.
17. the 4th class thermal drivers compressing-absorbing type heat pumps, be 13-15 item described arbitrary 4th class thermal drivers compression- Absorption heat pump, the 4th generator sets up high temperature thermal 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 10-17 item described arbitrary 4th class thermal drivers compression- Absorption heat pump, cancels choke valve and second throttle, and the second generator is had cryogen liquid pipeline through choke valve with evaporimeter even Logical be adjusted to the second generator and have cryogen liquid pipeline to connect with evaporimeter, the second generator is had cryogen liquid pipeline to throttle through second Valve is connected with evaporimeter and is adjusted to the second generator and has cryogen liquid pipeline to be connected with evaporimeter, formed the 4th class thermal drivers compression- Absorption heat pump.
19. the 4th class thermal drivers compressing-absorbing type heat pumps, be described in 1-7 item arbitrary 4th class thermal drivers compression- In absorption heat pump, increase the 3rd generator, the second absorber and the 3rd solution heat exchanger, absorber is had weak solution pipeline Connect with generator through solution pump and solution heat exchanger and be adjusted to absorber and have weak solution pipeline through the 3rd solution heat exchanger Connect with the second absorber, the second absorber has weak solution pipeline to connect with generator with solution heat exchanger through solution pump again, Second generator there is is concentrated solution pipeline to connect with absorber and be adjusted to second through the second solution pump and the second solution heat exchanger Generator has concentrated solution pipeline to connect with the 3rd generator through the second solution heat exchanger, and the 3rd generator has concentrated solution pipeline again Connect with absorber through the second solution pump and the 3rd solution heat exchanger, condenser is had cryogen liquid pipeline through the second generator and Choke valve is connected with evaporimeter and is adjusted to condenser and has cryogen liquid pipeline through the second generator, the 3rd generator and choke valve and steaming Send out device connection, the 3rd generator also has refrigerant steam channel to connect with the second absorber, the second absorber also has cooling medium to lead to Road or low-temperature heat medium passage and ft connection, form the 4th class thermal drivers compressing-absorbing type heat pump.
20. the 4th class thermal drivers compressing-absorbing type heat pumps, be described at the 19th arbitrary 4th class thermal drivers compression- In absorption heat pump, cancel choke valve, the 3rd generator is had cryogen liquid pipeline to connect with evaporimeter through choke valve and is adjusted to the Three generators have cryogen liquid pipeline to connect with evaporimeter, form the 4th class thermal drivers compressing-absorbing type heat pump.
21. the 4th class thermal drivers compressing-absorbing type heat pumps, be described at the 19th arbitrary 4th class thermal drivers compression- In absorption heat pump, increase the 4th generator, second throttle, the 3rd solution pump, the 4th solution heat exchanger and heater, the Two absorbers are set up weak solution pipeline and are connected with the 4th generator through the 3rd solution pump and the 4th solution heat exchanger, the 4th generation Device also has concentrated solution pipeline to connect with the second generator through the 4th solution heat exchanger and the second solution heat exchanger, by generator There is refrigerant steam channel to connect with condenser to be adjusted to the 4th after generator has refrigerant steam channel to connect with the 4th generator Generator has cryogen liquid pipeline to connect with evaporimeter with second throttle through heater, the second generator, the 3rd generator again, the Four generators also have refrigerant steam channel to connect with condenser, and heater also has heated medium passage and ft connection, are formed 4th class thermal drivers compressing-absorbing type heat pump.
22. the 4th class thermal drivers compressing-absorbing type heat pumps, be described at the 19th arbitrary 4th class thermal drivers compression- In absorption heat pump, increase the 4th generator, second throttle, the 4th solution heat exchanger and heater, by the second absorber There is weak solution pipeline to connect with generator through solution pump and solution heat exchanger to be adjusted to the second absorber and have weak solution pipeline warp Solution pump, solution heat exchanger and the 4th solution heat exchanger are connected with generator, and generator is had concentrated solution pipeline through solution Heat exchanger and the second solution heat exchanger are connected with the second generator and are adjusted to generator and have concentrated solution pipeline through the 4th solution Heat exchanger is connected with the 4th generator, and the 4th generator has concentrated solution pipeline to hand over through solution heat exchanger and the second solution heat again Parallel operation is connected with the second generator, generator is had refrigerant steam channel to connect with condenser and is adjusted to generator and has refrigerant vapour After passage is connected with the 4th generator, the 4th generator has cryogen liquid pipeline again through heater, the second generator, the 3rd generation Device is connected with evaporimeter with second throttle, and the 4th generator also has refrigerant steam channel to connect with condenser, and heater 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, be described at the 19th arbitrary 4th class thermal drivers compression- In absorption heat pump, increase the 4th generator, second throttle, the 3rd solution pump, the 4th solution heat exchanger and heater, will Second absorber have weak solution pipeline connect with generator through solution pump and solution heat exchanger be adjusted to the second absorber have dilute Solution line is connected with the 4th generator with solution heat exchanger through solution pump, and the 4th generator has concentrated solution pipeline again through the 3rd Solution pump and the 4th solution heat exchanger are connected with generator, and generator is had concentrated solution pipeline through solution heat exchanger and second Solution heat exchanger connect with the second generator be adjusted to generator have concentrated solution pipeline through the 4th solution heat exchanger, solution heat Exchanger and the second solution heat exchanger are connected with the second generator, and generator is had refrigerant steam channel to connect tune with condenser Whole have refrigerant steam channel to connect with the 4th generator for generator after the 4th generator have again cryogen liquid pipeline through heater, Second generator, the 3rd generator are connected with evaporimeter with second throttle, the 4th generator also have refrigerant steam channel with cold Condenser connects, and heater also has heated medium passage and ft connection, forms the 4th class thermal drivers compressing-absorbing type heat pump.
24. the 4th class thermal drivers compressing-absorbing type heat pumps, be 21-23 item described arbitrary 4th class thermal drivers compression- Absorption heat pump, the 4th generator sets up high temperature thermal medium passage and ft connection, forms the 4th class thermal drivers compressing-absorbing type Heat pump.
25. the 4th class thermal drivers compressing-absorbing type heat pumps, be 21-24 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 evaporimeter Connection is adjusted to the 3rd generator has cryogen liquid pipeline to connect with evaporimeter, and the 3rd generator is had cryogen liquid pipeline through second section Stream valve is connected with evaporimeter and is adjusted to the 3rd generator and has cryogen liquid pipeline to be connected with evaporimeter, formation the 4th class thermal drivers pressure Contracting-absorption heat pump.
26. the 4th class thermal drivers compressing-absorbing type heat pumps, are the arbitrary 4th class thermal drivers compression-suctions described at the 8th In receipts formula heat pump, increase the 4th generator, the 3rd absorber and the 4th solution heat exchanger, absorber is had weak solution pipeline warp Solution pump is connected with the second absorber with solution heat exchanger and is adjusted to absorber and has weak solution pipeline the 4th solution heat exchanger Connect with the 3rd absorber, the 3rd absorber has weak solution pipeline to connect through solution pump and solution heat exchanger and the second absorber again Logical, the second generator there is is concentrated solution pipeline to connect with absorber through the second solution pump and the second solution heat exchanger and is adjusted to the Two generators have concentrated solution pipeline to connect with the 4th generator through the second solution heat exchanger, and the 4th generator has concentrated solution pipe again Road the second solution pump and the 4th solution heat exchanger are connected with absorber, and condenser is had cryogen liquid pipeline through the second generator Connect with evaporimeter with choke valve be adjusted to condenser have cryogen liquid pipeline through the second generator, the 4th generator and choke valve with Evaporimeter connects, and the 4th generator also has refrigerant steam channel to connect with the 3rd absorber, and the 3rd absorber also has cooling medium Passage or low-temperature heat medium passage and ft connection, form the 4th class thermal drivers compressing-absorbing type heat pump.
27. the 4th class thermal drivers compressing-absorbing type heat pumps, be described at the 26th arbitrary 4th class thermal drivers compression- In absorption heat pump, cancel choke valve, the 4th generator is had cryogen liquid pipeline to connect with evaporimeter through choke valve and is adjusted to the Four generators have cryogen liquid pipeline to connect with evaporimeter, form the 4th class thermal drivers compressing-absorbing type heat pump.
28. the 4th class thermal drivers compressing-absorbing type heat pumps, are arbitrary fourth class thermal drivers compression-suctions described in 1-7 item In receipts formula heat pump, increase the 3rd generator, the second absorber, the 3rd solution pump and the 3rd solution heat exchanger, generator is had Refrigerant steam channel is connected with condenser and is adjusted to generator and has refrigerant steam channel to be connected with the second absorber, the second absorber Weak solution pipeline is also had to connect with the 3rd generator through the 3rd solution pump and the 3rd solution heat exchanger, the 3rd generator is also dense Solution line is connected with the second absorber through the 3rd solution heat exchanger, and the 3rd generator also has refrigerant steam channel and condenser Connection, the 3rd generator also has high temperature thermal medium passage and ft connection, and the second absorber also has heated medium passage with outward Portion connects, and forms the 4th class thermal drivers compressing-absorbing type heat pump.
29. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the 28th described arbitrary 4th class thermal drivers compression-suction In receipts formula heat pump, cancel choke valve, the second generator is had cryogen liquid pipeline to connect with evaporimeter through choke valve and is adjusted to second Generator has cryogen liquid pipeline to connect with evaporimeter, forms the 4th class thermal drivers compressing-absorbing type heat pump.
30. the 4th class thermal drivers compressing-absorbing type heat pumps, are the arbitrary 4th class thermal drivers pressures described in 1-29 item In contracting-absorption heat pump, decompressor there is is refrigerant steam channel to connect with evaporimeter or the second condenser and is adjusted to decompressor and has Refrigerant steam channel is connected with condenser, forms the 4th class thermal drivers compressing-absorbing type heat pump.
31. the 4th class thermal drivers compressing-absorbing type heat pumps, are the arbitrary 4th class thermal drivers pressures described in 1-30 item In contracting-absorption heat pump, increase engine, engine connects compressor and transmits power to compressor, forms additional external and moves The 4th class thermal drivers compressing-absorbing type heat pump that power drives.
32. the 4th class thermal drivers compressing-absorbing type heat pumps, are the arbitrary 4th class thermal drivers pressures described in 1-30 item In contracting-absorption heat pump, increase 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.
Brief description：
Fig. 1 is according to 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 according to 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 according to 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 according to 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 according to 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 according to 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 according to 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 according to 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 according to 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 according to the 4th the 10th kind of principle heating power system of class thermal drivers compressing-absorbing type heat pump provided by the present invention System figure.
Figure 11 is according to the 4th the 11st kind of principle heating power system of class thermal drivers compressing-absorbing type heat pump provided by the present invention System figure.
Figure 12 is according to the 4th the 12nd kind of principle heating power system of class thermal drivers compressing-absorbing type heat pump provided by the present invention System figure.
Figure 13 is according to the 4th the 13rd kind of principle heating power system of class thermal drivers compressing-absorbing type heat pump provided by the present invention System figure.
Figure 14 is according to the 4th the 14th kind of principle heating power system of class thermal drivers compressing-absorbing type heat pump provided by the present invention System figure.
Figure 15 is according to the 4th the 15th kind of principle heating power system of class thermal drivers compressing-absorbing type heat pump provided by the present invention System figure.
Figure 16 is according to the 4th the 16th kind of principle heating power system of class thermal drivers compressing-absorbing type heat pump provided by the present invention System figure.
Figure 17 is according to the 4th the 17th kind of principle heating power system of class thermal drivers compressing-absorbing type heat pump provided by the present invention System figure.
Figure 18 is according to the 4th the 18th kind of principle heating power system of class thermal drivers compressing-absorbing type heat pump provided by the present invention System figure.
Figure 19 is according to the 4th the 19th kind of principle heating power system of class thermal drivers compressing-absorbing type heat pump provided by the present invention System figure.
Figure 20 is according to the 4th the 20th kind of principle heating power system of class thermal drivers compressing-absorbing type heat pump provided by the present invention System figure.
Figure 21 is according to the 4th the 21st kind of principle heating power system of class thermal drivers compressing-absorbing type heat pump provided by the present invention System figure.
In figure, 1- absorber, 2- generator, 3- second generator, 4- condenser, 5- second condenser, 6- evaporimeter, 7- Choke valve, 8- cryogen liquid pump, 9- the second cryogen liquid pump, 10- solution pump, 11- the second solution pump, 12- solution heat exchanger, 13- Second solution heat exchanger, 14- high-temperature heat exchanger, 15- decompressor, 16- compressor, 17- second decompressor, 18- second presses Contracting machine, 19- regenerator, 20- low temperature heat exchanger, 21- cryogenic throttle valve, 22- the 3rd generator, 23- second absorber, 24- 3rd solution pump, 25- the 3rd solution heat exchanger, 26- second throttle, 27- heater, 28- the 4th generator, 29- the 4th Solution pump, 30- the 3rd solution heat exchanger, 31- the 3rd absorber.
Specific embodiment：
First it is noted that in the statement of structure and flow process, inessential in the case of do not repeat；To apparent Flow process do not state.To describe the present invention with example in detail below in conjunction with the accompanying drawings.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 1 is realized in：
(1) in structure, it mainly by absorber, generator, the second generator, condenser, the second condenser, evaporimeter, Choke valve, cryogen liquid pump, the second cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, High-temperature heat exchanger, decompressor, compressor and the second decompressor are formed；Absorber 1 has weak solution pipeline through solution pump 10 He Solution heat exchanger 12 is connected with generator 2, and generator 2 also has concentrated solution pipeline through solution heat exchanger 12 and the second solution heat Exchanger 13 is connected with the second generator 3, and the second generator 3 also has concentrated solution pipeline through the second solution pump 11 and the second solution heat Exchanger 13 is connected with absorber 1, and generator 2 also has refrigerant steam channel to connect with condenser 4, and the second generator 3 is also cold Agent steam channel is connected with the second condenser 5, and condenser 4 also has cryogen liquid pipeline through the second generator 3 and choke valve 7 and evaporation Device 6 connects, condenser 4 also have cryogen liquid pipeline connect with high-temperature heat exchanger 14 through cryogen liquid pump 8 after high-temperature heat exchanger 14 have refrigerant steam channel to connect with decompressor 15 again, and decompressor 15 also has refrigerant steam channel to connect with evaporimeter 6, and second is cold Condenser 5 also has cryogen liquid pipeline to connect with evaporimeter 6 through the second cryogen liquid pump 9, and evaporimeter 6 also has refrigerant steam channel and absorption Device 1 connects, and outside has low-temperature heat medium passage to connect with compressor 16, and compressor 16 also has low-temperature heat medium passage through evaporimeter 6 are connected with the second decompressor 17, and the second decompressor 17 also has low-temperature heat medium passage and ft connection, generator 2 and high warm Exchanger 14 also has high temperature thermal medium passage and ft connection, absorber 1 and condenser 4 also to have heated medium to lead to respectively respectively Road and ft connection, the second condenser 5 also has low-temperature heat medium passage and ft connection, decompressor 15 and the second decompressor 17 even Connect compressor 16 and transmit power.
(2), in flow process, the weak solution of absorber 1 enters generator 2 through solution pump 10 and solution heat exchanger 12, high warm Medium flows through generator 2, heating enters its interior solution release refrigerant vapour and provides to condenser 4, the concentrated solution of generator 2 Enter the second generator 3 through solution heat exchanger 12 and the second solution heat exchanger 13, cryogen liquor stream through the second generator 3, plus Heat enters its interior solution release refrigerant vapour and provides to the second condenser 5, and the concentrated solution of the second generator 3 is through the second solution Pump 11 and the second solution heat exchanger 13 enter absorber 1, absorption refrigerant vapour heat release in heated medium；Condenser 4 Refrigerant vapour heat release becomes cryogen liquid in heated medium, and the cryogen liquid of condenser 4 is divided into the two-way first via and flows through second Evaporimeter 6 is entered through choke valve 7 reducing pressure by regulating flow again, the second tunnel flows through high temperature through after cryogen liquid pump 8 pressurization after raw device 3 heat release Heat exchanger 14 absorbs heat into refrigerant vapour and provides to decompressor 15, and refrigerant vapour enters after flowing through decompressor 15 step-down work done Evaporimeter 6；The refrigerant vapour heat release of the second condenser 5 becomes cryogen liquid in low-temperature heat medium, and the cryogen liquid of the second condenser 5 is through Two cryogen liquid pump 9 pressurization enters evaporimeter 6；The work(of decompressor 15 and the second decompressor 17 output is supplied to compressor 16 start Power, low-temperature heat medium flows through compressor 16 boosting and heats up, and the low-temperature heat medium of compressor 16 discharge flows through evaporimeter 6 heat release, Flow through decompressor 17 step-down work done afterwards and externally discharge；The cryogen liquid of evaporimeter 6 absorbs heat into refrigerant vapour, and evaporimeter 6 discharges Refrigerant vapour enter absorber 1, formed 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 realized in：
In the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 1, decompressor 15 there are refrigerant steam channel and evaporation Device 6 connection is adjusted to decompressor 15 has refrigerant steam channel to connect with the second condenser 5, forms the 4th class thermal drivers compression-suction Receipts formula heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 3 is realized in：
(1) in structure, it mainly by absorber, generator, the second generator, condenser, the second condenser, evaporimeter, Choke valve, cryogen liquid pump, the second cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, High-temperature heat exchanger, decompressor, compressor, the second decompressor and the second compressor are formed；Absorber 1 has weak solution pipeline warp Solution pump 10 is connected with generator 2 with solution heat exchanger 12, and generator 2 also has concentrated solution pipeline through solution heat exchanger 12 He Second solution heat exchanger 13 is connected with the second generator 3, and the second generator 3 also has concentrated solution pipeline through the second solution pump 11 He Second solution heat exchanger 13 is connected with absorber 1, and generator 2 also has refrigerant steam channel to connect with condenser 4, the second generation Device 3 also has refrigerant steam channel to connect with the second condenser 5, and condenser 4 also has cryogen liquid pipeline through the second generator 3 and throttling Valve 7 is connected with evaporimeter 6, condenser 4 also have cryogen liquid pipeline connect with high-temperature heat exchanger 14 through cryogen liquid pump 8 after high temperature Heat exchanger 14 has refrigerant steam channel to connect with decompressor 15 again, and decompressor 15 also has refrigerant steam channel with evaporimeter 6 even Logical, the second condenser 5 also has cryogen liquid pipeline to connect with evaporimeter 6 through the second cryogen liquid pump 9, and evaporimeter 6 also has refrigerant vapour Passage is connected with absorber 1, and outside has low-temperature heat medium passage to connect with compressor 16, and compressor 16 also has low-temperature heat medium to lead to Road is connected with the second compressor 18 through evaporimeter 6, and the second compressor 18 also has low-temperature heat medium passage swollen with second through evaporimeter 6 Swollen machine 17 connects, and the second decompressor 17 also has low-temperature heat medium passage and ft connection, generator 2 and high-temperature heat exchanger 14 also High temperature thermal medium passage and ft connection, absorber 1 and condenser 4 is had also to have heated medium passage and outside to connect respectively respectively Logical, the second condenser 5 also has low-temperature heat medium passage and ft connection, decompressor 15 and the second decompressor 17 to connect compressor 16 With the second compressor 18 and transmit power.
(2), in flow process, the weak solution of absorber 1 enters generator 2 through solution pump 10 and solution heat exchanger 12, high warm Medium flows through generator 2, heating enters its interior solution release refrigerant vapour and provides to condenser 4, the concentrated solution of generator 2 Enter the second generator 3 through solution heat exchanger 12 and the second solution heat exchanger 13, cryogen liquor stream through the second generator 3, plus Heat enters its interior solution release refrigerant vapour and provides to the second condenser 5, and the concentrated solution of the second generator 3 is through the second solution Pump 11 and the second solution heat exchanger 13 enter absorber 1, absorption refrigerant vapour heat release in heated medium；Condenser 4 Refrigerant vapour heat release becomes cryogen liquid in heated medium, and the cryogen liquid of condenser 4 is divided into the two-way first via and flows through second Evaporimeter 6 is entered through choke valve 7 reducing pressure by regulating flow again, the second tunnel flows through high temperature through after cryogen liquid pump 8 pressurization after raw device 3 heat release Heat exchanger 14 absorbs heat into refrigerant vapour and provides to decompressor 15, and refrigerant vapour enters after flowing through decompressor 15 step-down work done Evaporimeter 6；The refrigerant vapour heat release of the second condenser 5 becomes cryogen liquid in low-temperature heat medium, and the cryogen liquid of the second condenser 5 is through Two cryogen liquid pump 9 pressurization enters evaporimeter 6；The work(of decompressor 15 and the second decompressor 17 output is supplied to compressor 16 and second Compressor 18 is used as power, and low-temperature heat medium flows through compressor 16 boosting and heats up, and the low-temperature heat medium of compressor 16 discharge flows through steaming Send out device 6 heat release, flow through the second compressor 18 boosting afterwards and heat up；The low-temperature heat medium of the second compressor 18 discharge flows through evaporation Device 6 heat release, flow through decompressor 17 step-down work done afterwards and externally discharge；The cryogen liquid of evaporimeter 6 absorbs heat into refrigerant vapour, steams The refrigerant vapour sending out device 6 release is supplied to absorber 1, forms 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 realized in：
(1) in structure, it mainly by absorber, generator, the second generator, condenser, the second condenser, evaporimeter, Choke valve, cryogen liquid pump, the second cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, High-temperature heat exchanger, decompressor, compressor, the second decompressor and regenerator are formed；Absorber 1 has weak solution pipeline through solution Pump 10 is connected with generator 2 with solution heat exchanger 12, and generator 2 also has concentrated solution pipeline through solution heat exchanger 12 and second Solution heat exchanger 13 is connected with the second generator 3, and the second generator 3 also has concentrated solution pipeline through the second solution pump 11 and second Solution heat exchanger 13 is connected with absorber 1, and generator 2 also has refrigerant steam channel to connect with condenser 4, the second generator 3 Refrigerant steam channel is also had to connect with the second condenser 5, condenser 4 also has cryogen liquid pipeline through the second generator 3 and choke valve 7 Connect with evaporimeter 6, after condenser 4 also has cryogen liquid pipeline to connect with high-temperature heat exchanger 14 through cryogen liquid pump 8, height warms Exchanger 14 has refrigerant steam channel to connect with decompressor 15 again, and decompressor 15 also has refrigerant steam channel to connect with evaporimeter 6, Second condenser 5 also has cryogen liquid pipeline to connect with evaporimeter 6 through the second cryogen liquid pump 9, and evaporimeter 6 also has refrigerant steam channel Connect with absorber 1, outside has low-temperature heat medium passage to connect with compressor 16 through regenerator 19, compressor 16 also has Low Temperature Thermal Medium channel is connected with the second decompressor 17 with regenerator 19 through evaporimeter 6, and the second decompressor 17 also has low-temperature heat medium passage With ft connection, generator 2 and high-temperature heat exchanger 14 also have high temperature thermal medium passage and ft connection, absorber 1 He respectively Condenser 4 also has heated medium passage and ft connection respectively, and the second condenser 5 also has low-temperature heat medium passage to connect with outside Lead to, decompressor 15 and the second decompressor 17 connect compressor 16 and transmit power.
(2), in flow process, the weak solution of absorber 1 enters generator 2 through solution pump 10 and solution heat exchanger 12, high warm Medium flows through generator 2, heating enters its interior solution release refrigerant vapour and provides to condenser 4, the concentrated solution of generator 2 Enter the second generator 3 through solution heat exchanger 12 and the second solution heat exchanger 13, cryogen liquor stream through the second generator 3, plus Heat enters its interior solution release refrigerant vapour and provides to the second condenser 5, and the concentrated solution of the second generator 3 is through the second solution Pump 11 and the second solution heat exchanger 13 enter absorber 1, absorption refrigerant vapour heat release in heated medium；Condenser 4 Refrigerant vapour heat release becomes cryogen liquid in heated medium, and the cryogen liquid of condenser 4 is divided into the two-way first via and flows through second Evaporimeter 6 is entered through choke valve 7 reducing pressure by regulating flow again, the second tunnel flows through high temperature through after cryogen liquid pump 8 pressurization after raw device 3 heat release Heat exchanger 14 absorbs heat into refrigerant vapour and provides to decompressor 15, and refrigerant vapour enters after flowing through decompressor 15 step-down work done Evaporimeter 6；The refrigerant vapour heat release of the second condenser 5 becomes cryogen liquid in low-temperature heat medium, and the cryogen liquid of the second condenser 5 is through Two cryogen liquid pump 9 pressurization enters evaporimeter 6；Outer low temperature thermal medium flows through regenerator 19 and absorbs heat, and enters compressor 16 afterwards Boosting heats up；The low-temperature heat medium of compressor 16 discharge flows through evaporimeter 6 and regenerator 19 progressively heat release successively, enters afterwards Externally discharge after second decompressor 17 step-down work done；The work(of decompressor 15 and the second decompressor 17 output is supplied to compressor 16 It is used as power, the cryogen liquid of evaporimeter 6 absorbs heat into refrigerant vapour, the refrigerant vapour of evaporimeter 6 release enters absorber 1, form the Four class thermal drivers compressing-absorbing type heat pumps.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 5 is realized in：
(1) in structure, it mainly by absorber, generator, the second generator, condenser, the second condenser, evaporimeter, Choke valve, cryogen liquid pump, the second cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, High-temperature heat exchanger, decompressor, compressor, the second decompressor and low temperature heat exchanger are formed；Absorber 1 has weak solution pipeline Connect with generator 2 with solution heat exchanger 12 through solution pump 10, generator 2 also has concentrated solution pipeline through solution heat exchanger 12 Connect with the second generator 3 with the second solution heat exchanger 13, the second generator 3 also has concentrated solution pipeline through the second solution pump 11 Connect with absorber 1 with the second solution heat exchanger 13, generator 2 also has refrigerant steam channel to connect with condenser 4, second Raw device 3 also has refrigerant steam channel to connect with the second condenser 5, and condenser 4 also has cryogen liquid pipeline through the second generator 3 and section Stream valve 7 is connected with evaporimeter 6, and condenser 4 also has cryogen liquid pipeline high after connecting with high-temperature heat exchanger 14 through cryogen liquid pump 8 Temperature heat exchanger 14 has refrigerant steam channel to connect with decompressor 15 again, and decompressor 15 also has refrigerant steam channel and evaporimeter 6 Connection, the second condenser 5 also has cryogen liquid pipeline to connect with evaporimeter 6 through the second cryogen liquid pump 9, and evaporimeter 6 also has cryogen to steam Vapour passage is connected with absorber 1, and compressor 16 has cycle fluid passage to connect with the second decompressor 17 through evaporimeter 6, and second is swollen Swollen machine 17 also has cycle fluid passage to connect with compressor 16 through low temperature heat exchanger 20, generator 2 and high-temperature heat exchanger 14 High temperature thermal medium passage and ft connection, absorber 1 and condenser 4 is also had also to have heated medium passage and outside respectively respectively Connection, the second condenser 5 and low temperature heat exchanger 20 also have low-temperature heat medium passage and ft connection respectively, decompressor 15 and the Two decompressor 17 connects compressor 16 and transmits power.
(2), in flow process, the weak solution of absorber 1 enters generator 2 through solution pump 10 and solution heat exchanger 12, high warm Medium flows through generator 2, heating enters its interior solution release refrigerant vapour and provides to condenser 4, the concentrated solution of generator 2 Enter the second generator 3 through solution heat exchanger 12 and the second solution heat exchanger 13, cryogen liquor stream through the second generator 3, plus Heat enters its interior solution release refrigerant vapour and provides to the second condenser 5, and the concentrated solution of the second generator 3 is through the second solution Pump 11 and the second solution heat exchanger 13 enter absorber 1, absorption refrigerant vapour heat release in heated medium；Condenser 4 Refrigerant vapour heat release becomes cryogen liquid in heated medium, and the cryogen liquid of condenser 4 is divided into the two-way first via and flows through second Evaporimeter 6 is entered through choke valve 7 reducing pressure by regulating flow again, the second tunnel flows through high temperature through after cryogen liquid pump 8 pressurization after raw device 3 heat release Heat exchanger 14 absorbs heat into refrigerant vapour and provides to decompressor 15, and refrigerant vapour enters after flowing through decompressor 15 step-down work done Evaporimeter 6；The refrigerant vapour heat release of the second condenser 5 becomes cryogen liquid in low-temperature heat medium, and the cryogen liquid of the second condenser 5 is through Two cryogen liquid pump 9 pressurization enters evaporimeter 6；The cycle fluid of compressor 16 discharge flows through evaporimeter 6 heat release, enters the afterwards Two decompressor 17 is depressured work done；Second decompressor 17 discharge cycle fluid flow through low temperature heat exchanger 20 and absorb heat, laggard Enter compressor 16 boosting to heat up；The work(of decompressor 15 and the second decompressor 17 output is supplied to compressor 16 and is used as power, evaporimeter 6 Cryogen liquid absorb heat into refrigerant vapour, the refrigerant vapour of evaporimeter 6 release enters absorber 1, formed the 4th class thermal drivers compression- Absorption heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 6 is realized in：
(1) in structure, it mainly by absorber, generator, the second generator, condenser, the second condenser, evaporimeter, Choke valve, cryogen liquid pump, the second cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, High-temperature heat exchanger, decompressor and compressor are formed；Absorber 1 has weak solution pipeline through solution pump 10 and solution heat exchanger 12 are connected with generator 2, and generator 2 also has concentrated solution pipeline through solution heat exchanger 12 and the second solution heat exchanger 13 and the Two generators 3 connect, and the second generator 3 also has concentrated solution pipeline through the second solution pump 11 and the second solution heat exchanger 13 and suction Receive device 1 to connect, generator 2 also has refrigerant steam channel to connect with condenser 4, the second generator 3 also have refrigerant steam channel and Second condenser 5 connects, and condenser 4 also has cryogen liquid pipeline to connect with evaporimeter 6 with choke valve 7 through the second generator 3, condensation After device 4 also has cryogen liquid pipeline to connect with high-temperature heat exchanger 14 through cryogen liquid pump 8, high-temperature heat exchanger 14 has cryogen to steam again Vapour passage is connected with decompressor 15, and decompressor 15 also has refrigerant steam channel to connect with evaporimeter 6, and the second condenser 5 is also cold Agent liquid pipeline is connected with evaporimeter 6 through the second cryogen liquid pump 9, and evaporimeter 6 also has refrigerant steam channel to connect with absorber 1, outward Portion has low-temperature heat medium passage to connect with compressor 16, and compressor 16 also has low-temperature heat medium passage to connect through evaporimeter 6 and outside Lead to, generator 2 and high-temperature heat exchanger 14 also have high temperature thermal medium passage and ft connection, absorber 1 and condenser 4 also respectively There are heated medium passage and ft connection respectively, the second condenser 5 also has low-temperature heat medium passage and ft connection, decompressor 15 connection compressors 16 simultaneously transmit power.
(2), in flow process, the weak solution of absorber 1 enters generator 2 through solution pump 10 and solution heat exchanger 12, high warm Medium flows through generator 2, heating enters its interior solution release refrigerant vapour and provides to condenser 4, the concentrated solution of generator 2 Enter the second generator 3 through solution heat exchanger 12 and the second solution heat exchanger 13, cryogen liquor stream through the second generator 3, plus Heat enters its interior solution release refrigerant vapour and provides to the second condenser 5, and the concentrated solution of the second generator 3 is through the second solution Pump 11 and the second solution heat exchanger 13 enter absorber 1, absorption refrigerant vapour heat release in heated medium；Condenser 4 Refrigerant vapour heat release becomes cryogen liquid in heated medium, and the cryogen liquid of condenser 4 is divided into the two-way first via and flows through second Evaporimeter 6 is entered through choke valve 7 reducing pressure by regulating flow again, the second tunnel flows through high temperature through after cryogen liquid pump 8 pressurization after raw device 3 heat release Heat exchanger 14 absorbs heat into refrigerant vapour and provides to decompressor 15, and refrigerant vapour enters after flowing through decompressor 15 step-down work done Evaporimeter 6；The refrigerant vapour heat release of the second condenser 5 becomes cryogen liquid in low-temperature heat medium, and the cryogen liquid of the second condenser 5 is through Two cryogen liquid pump 9 pressurization enters evaporimeter 6；Outer low temperature thermal medium enters compressor 16 boosting and heats up, and flows through evaporimeter 6 heat release Externally discharge afterwards；The work(of decompressor 15 output is supplied to compressor 16 and is used as power, and the cryogen liquid of evaporimeter 6 absorbs heat into cryogen and steams Vapour, the refrigerant vapour of evaporimeter 6 release provides to absorber 1, forms the 4th class thermal drivers compressing-absorbing type heat pump.
This example focuses on and flows through compressor 16 boosting intensification for low-temperature heat medium for low-pressure steam during low-pressure steam, Flow through evaporimeter 6 heat release and condense, externally discharge afterwards.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 7 is realized in：
(1) in structure, it mainly by absorber, generator, the second generator, condenser, the second condenser, evaporimeter, Choke valve, cryogen liquid pump, the second cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, High-temperature heat exchanger, decompressor, compressor, low temperature heat exchanger and cryogenic throttle valve are formed；Absorber 1 has weak solution pipeline Connect with generator 2 with solution heat exchanger 12 through solution pump 10, generator 2 also has concentrated solution pipeline through solution heat exchanger 12 Connect with the second generator 3 with the second solution heat exchanger 13, the second generator 3 also has concentrated solution pipeline through the second solution pump 11 Connect with absorber 1 with the second solution heat exchanger 13, generator 2 also has refrigerant steam channel to connect with condenser 4, second Raw device 3 also has refrigerant steam channel to connect with the second condenser 5, and condenser 4 also has cryogen liquid pipeline through the second generator 3 and section Stream valve 7 is connected with evaporimeter 6, and condenser 4 also has cryogen liquid pipeline high after connecting with high-temperature heat exchanger 14 through cryogen liquid pump 8 Temperature heat exchanger 14 has refrigerant steam channel to connect with decompressor 15 again, and decompressor 15 also has refrigerant steam channel and evaporimeter 6 Connection, the second condenser 5 also has cryogen liquid pipeline to connect with evaporimeter 6 through the second cryogen liquid pump 9, and evaporimeter 6 also has cryogen to steam Vapour passage is connected with absorber 1, and compressor 16 has cycle fluid passage through evaporimeter 6 and cryogenic throttle valve 21 and low temperature heat exchange Device 20 connects, and low temperature heat exchanger 20 also has cycle fluid passage to connect with compressor 16, generator 2 and high-temperature heat exchanger 14 High temperature thermal medium passage and ft connection, absorber 1 and condenser 4 is also had also to have heated medium passage and outside respectively respectively Connection, the second condenser 5 and low temperature heat exchanger 20 also have low-temperature heat medium passage and ft connection respectively, and decompressor 15 connects Compressor 16 simultaneously transmits power.
(2), in flow process, the weak solution of absorber 1 enters generator 2 through solution pump 10 and solution heat exchanger 12, high warm Medium flows through generator 2, heating enters its interior solution release refrigerant vapour and provides to condenser 4, the concentrated solution of generator 2 Enter the second generator 3 through solution heat exchanger 12 and the second solution heat exchanger 13, cryogen liquor stream through the second generator 3, plus Heat enters its interior solution release refrigerant vapour and provides to the second condenser 5, and the concentrated solution of the second generator 3 is through the second solution Pump 11 and the second solution heat exchanger 13 enter absorber 1, absorption refrigerant vapour heat release in heated medium；Condenser 4 Refrigerant vapour heat release becomes cryogen liquid in heated medium, and the cryogen liquid of condenser 4 is divided into the two-way first via and flows through second Evaporimeter 6 is entered through choke valve 7 reducing pressure by regulating flow again, the second tunnel flows through high temperature through after cryogen liquid pump 8 pressurization after raw device 3 heat release Heat exchanger 14 absorbs heat into refrigerant vapour and provides to decompressor 15, and refrigerant vapour enters after flowing through decompressor 15 step-down work done Evaporimeter 6；The refrigerant vapour heat release of the second condenser 5 becomes cryogen liquid in low-temperature heat medium, and the cryogen liquid of the second condenser 5 is through Two cryogen liquid pump 9 pressurization enters evaporimeter 6；The cycle fluid of compressor 16 discharge flows through evaporimeter 6 and heat release becomes cryogen liquid, it By cryogenic throttle valve 21 reducing pressure by regulating flow and enter low temperature heat exchanger 20；Low-temperature heat medium flows through low temperature heat exchanger 20 and adds Heat enters its interior cryogen liquid and becomes refrigerant vapour, and the refrigerant vapour that low temperature heat exchanger 20 produces enters compressor 16 boosting and rises Temperature；The work(of decompressor 15 output is supplied to compressor 16 and is used as power, and the cryogen liquid of evaporimeter 6 absorbs heat into refrigerant vapour, evaporimeter 6 The refrigerant vapour of release enters absorber 1, 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 realized in：
(1) in structure, it mainly by absorber, generator, the second generator, condenser, the second condenser, evaporimeter, Choke valve, cryogen liquid pump, the second cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger, High-temperature heat exchanger, decompressor, compressor, the second compressor, low temperature heat exchanger and cryogenic throttle valve are formed；Absorber 1 Weak solution pipeline is had to connect with generator 2 with solution heat exchanger 12 through solution pump 10, generator 2 also has concentrated solution pipeline through molten Liquid heat exchanger 12 is connected with the second generator 3 with the second solution heat exchanger 13, and the second generator 3 also has concentrated solution pipeline warp Second solution pump 11 is connected with absorber 1 with the second solution heat exchanger 13, and generator 2 also has refrigerant steam channel and condenser 4 connections, the second generator 3 also has refrigerant steam channel to connect with the second condenser 5, condenser 4 also cryogen liquid pipeline through the Two generators 3 are connected with evaporimeter 6 with choke valve 7, and condenser 4 also has cryogen liquid pipeline through cryogen liquid pump 8 and high temperature heat exchange After device 14 connection, high-temperature heat exchanger 14 has refrigerant steam channel to connect with decompressor 15 again, and decompressor 15 also has refrigerant vapour Passage is connected with evaporimeter 6, and the second condenser 5 also has cryogen liquid pipeline to connect with evaporimeter 6 through the second cryogen liquid pump 9, evaporation Device 6 also has refrigerant steam channel to connect with absorber 1, and compressor 16 has cycle fluid passage through evaporimeter 6 and the second compressor 18 connections, the second compressor 18 also has cycle fluid passage to connect with low temperature heat exchanger 20 through evaporimeter 6 and cryogenic throttle valve 21 Logical, low temperature heat exchanger 20 also has cycle fluid passage to connect with compressor 16, and generator 2 and high-temperature heat exchanger 14 are also distinguished High temperature thermal medium passage and ft connection, absorber 1 and condenser 4 is had also to have heated medium passage and ft connection respectively, Second condenser 5 and low temperature heat exchanger 20 also have low-temperature heat medium passage and ft connection respectively, and decompressor 15 connects compression Machine 16 and the second compressor 18 simultaneously transmit power.
(2), in flow process, the weak solution of absorber 1 enters generator 2 through solution pump 10 and solution heat exchanger 12, high warm Medium flows through generator 2, heating enters its interior solution release refrigerant vapour and provides to condenser 4, the concentrated solution of generator 2 Enter the second generator 3 through solution heat exchanger 12 and the second solution heat exchanger 13, cryogen liquor stream through the second generator 3, plus Heat enters its interior solution release refrigerant vapour and provides to the second condenser 5, and the concentrated solution of the second generator 3 is through the second solution Pump 11 and the second solution heat exchanger 13 enter absorber 1, absorption refrigerant vapour heat release in heated medium；Condenser 4 Refrigerant vapour heat release becomes cryogen liquid in heated medium, and the cryogen liquid of condenser 4 is divided into the two-way first via and flows through second Evaporimeter 6 is entered through choke valve 7 reducing pressure by regulating flow again, the second tunnel flows through high temperature through after cryogen liquid pump 8 pressurization after raw device 3 heat release Heat exchanger 14 absorbs heat into refrigerant vapour and provides to decompressor 15, and refrigerant vapour enters after flowing through decompressor 15 step-down work done Evaporimeter 6；The refrigerant vapour heat release of the second condenser 5 becomes cryogen liquid in low-temperature heat medium, and the cryogen liquid of the second condenser 5 is through Two cryogen liquid pump 9 pressurization enters evaporimeter 6；The cycle fluid of compressor 16 discharge flows through evaporimeter 6 heat release, enters the afterwards Two compressor 18 boosting heats up；The cycle fluid of the second compressor 18 discharge flows through evaporimeter 6 and heat release becomes cryogen liquid, after warp Cryogenic throttle valve 21 reducing pressure by regulating flow enters low temperature heat exchanger 20；Low-temperature heat medium flows through low temperature heat exchanger 20 and heats entrance Its interior cryogen liquid becomes refrigerant vapour, and the refrigerant vapour that low temperature heat exchanger 20 produces enters compressor 16 boosting and heats up；Expand The work(of machine 15 output is supplied to compressor 16 and the second compressor 18 is used as power, and the cryogen liquid of evaporimeter 6 absorbs heat into refrigerant vapour, The refrigerant vapour of evaporimeter 6 release enters absorber 1, forms 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 realized in：
(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 3rd solution pump and the 3rd solution heat exchanger, absorber 1 is had weak solution pipeline to hand over through solution pump 10 and solution heat Parallel operation 12 is connected with generator 2 and is adjusted to absorber 1 and has weak solution pipeline through solution pump 10 and solution heat exchanger 12 and second Absorber 23 connects, and the second absorber 23 has weak solution pipeline through the 3rd solution pump 24 and the 3rd solution heat exchanger 25 and to send out again Raw device 2 connects, and generator 2 is had concentrated solution pipeline through solution heat exchanger 12 and the second solution heat exchanger 13 and the second generation Device 3 connection is adjusted to generator 2 has concentrated solution pipeline to connect with the 3rd generator 22 through the 3rd solution heat exchanger 25, the 3rd Raw device 22 has concentrated solution pipeline to connect with the second generator 3 with the second solution heat exchanger 13 through solution heat exchanger 12 again, the Three generators 22 also have refrigerant steam channel to connect with the second absorber 23, the 3rd generator 22 also have high temperature thermal medium passage and Ft connection, the second absorber 23 also has heated medium passage and ft connection.
(2) in flow process, the weak solution of absorber 1 through solution pump 10 and solution heat exchanger 12 enter the second absorber 23, Absorb refrigerant vapour and heat release is in heated medium, the weak solution of the second absorber 23 is through the 3rd solution pump 24 and the 3rd solution heat Exchanger 25 enters generator 2, and the concentrated solution of generator 2 enters the 3rd generator 22, high temperature through the 3rd solution heat exchanger 25 Thermal medium flows through the 3rd generator 22, heating enters its interior solution release refrigerant vapour and provides to the second absorber 23, the The concentrated solution of three generators 22 enters the second generator 3 through solution heat exchanger 12 and the second solution heat exchanger 13, forms the Four class thermal drivers compressing-absorbing type heat pumps.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Figure 10 is realized in：
(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 pump, the 3rd solution heat exchanger and heater, absorber 1 sets up weak solution pipeline through the 3rd solution pump 24 are connected with the 3rd generator 22 with the 3rd solution heat exchanger 25, and the 3rd generator 22 also has concentrated solution pipeline through the 3rd solution Heat exchanger 25 is connected with the second generator 3 with the second solution heat exchanger 13, and generator 2 is had refrigerant steam channel and condensation Device 4 connection is adjusted to the 3rd generator 22 after generator 2 has refrigerant steam channel to connect with the 3rd generator 22 cryogen again Liquid pipeline is connected with evaporimeter 6 with second throttle 26 through heater 27, the second generator 3, and the 3rd generator 22 also has cryogen Steam channel is connected with condenser 4, and heater 27 also has heated medium passage and ft connection.
(2), in flow process, the refrigerant vapour that generator 2 produces is supplied to the 3rd generator 22 and makees to drive thermal medium, absorber 1 Part weak solution enter the 3rd generator 22 through the 3rd solution pump 24 and the 3rd solution heat exchanger 25, refrigerant vapour flows through the Three generators 22, heating enter its interior solution release refrigerant vapour and provide to condenser 4, the concentrated solution of the 3rd generator 22 Enter the second generator 3 through the 3rd solution heat exchanger 25 and the second solution heat exchanger 13；Flow through the cold of the 3rd generator 22 Agent steam heat release becomes cryogen liquid, cryogen liquor stream through heater 27 and the second generator 3 progressively heat release, after through second throttle 26 throttlings enter evaporimeter 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 11 is realized in：
(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, absorber 1 is had weak solution pipeline through solution pump 10 and solution heat exchanger 12 connect with generator 2 be adjusted to absorber 1 have weak solution pipeline through solution pump 10, solution heat exchanger 12 and the 3rd solution heat Exchanger 25 is connected with generator 2, and generator 2 is had concentrated solution pipeline through solution heat exchanger 12 and the second solution heat exchanger 13 are connected with the second generator 3 and are adjusted to generator 2 and have concentrated solution pipeline through the 3rd solution heat exchanger 25 and the 3rd generator 22 connections, the 3rd generator 22 has concentrated solution pipeline again through solution heat exchanger 12 and the second solution heat exchanger 13 and second Raw device 3 connects, and generator 2 is had refrigerant steam channel to connect with condenser 4 and is adjusted to generator 2 and has refrigerant steam channel and the After three generator 22 connection, the 3rd generator 22 has cryogen liquid pipeline again through heater 27, the second generator 3 and the second throttling Valve 26 is connected with evaporimeter 6, and the 3rd generator 22 also has refrigerant steam channel to connect with condenser 4, and heater 27 is also added Hot media channel and ft connection, the 3rd generator 22 also has high temperature thermal medium passage and ft connection.
(2), in flow process, the refrigerant vapour of high temperature thermal medium and generator 2 generation is supplied to the 3rd generator 22 and makees to drive heat Medium, the weak solution of absorber 1 enters generator 2 through solution pump 10, solution heat exchanger 12 and the 3rd solution heat exchanger 25, The concentrated solution of generator 2 enters the 3rd generator 22, high temperature thermal medium and refrigerant vapour flow point through the 3rd solution heat exchanger 25 Do not provide through the 3rd generator 22, its interior solution release refrigerant vapour of heating entrance and to condenser 4, the 3rd generator 22 Concentrated solution enters the second generator 3 through solution heat exchanger 12 and the second solution heat exchanger 13；Flow through the 3rd generator 22 Refrigerant vapour heat release becomes cryogen liquid, cryogen liquor stream through heater 27 and the second generator 3 progressively heat release, after through second section stream Valve 26 throttling enters evaporimeter 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 realized in：
(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 pump, the 3rd solution heat exchanger and heater, absorber 1 is had weak solution pipeline through solution pump 10 He Solution heat exchanger 12 is connected with generator 2 and is adjusted to absorber 1 and has weak solution pipeline through solution pump 10 and solution heat exchanger 12 are connected with the 3rd generator 22, and the 3rd generator 22 has concentrated solution pipeline again through the 3rd solution pump 24 and the 3rd solution heat exchange Device 25 is connected with generator 2, by generator 2 have concentrated solution pipeline through solution heat exchanger 12 and the second solution heat exchanger 13 with Second generator 3 connection is adjusted to generator 2 has concentrated solution pipeline through the 3rd solution heat exchanger 25, solution heat exchanger 12 and Second solution heat exchanger 13 is connected with the second generator 3, and generator 2 is had refrigerant steam channel to connect adjustment with condenser 4 After having refrigerant steam channel to connect with the 3rd generator 22 for generator 2, the 3rd generator 22 has cryogen liquid pipeline again through heat supply Device 27, the second generator 3 are connected with evaporimeter 6 with second throttle 26, the 3rd generator 22 also have refrigerant steam channel with cold Condenser 4 connects, and heater 27 also has heated medium passage and ft connection.
(2), in flow process, the refrigerant vapour that generator 2 produces is supplied to the 3rd generator 22 and makees to drive thermal medium, absorber 1 Weak solution enter the 3rd generator 22 through solution pump 10 and solution heat exchanger 12, refrigerant vapour flow through the 3rd generator 22, Heating enters its interior solution release refrigerant vapour and provides to condenser 4, and the concentrated solution of the 3rd generator 22 is through the 3rd solution Pump 24 and the 3rd solution heat exchanger 25 enter generator 2, and the concentrated solution of generator 2 is through the 3rd solution heat exchanger 25, solution Heat exchanger 12 and the second solution heat exchanger 13 enter the second generator 3；Flow through the refrigerant vapour heat release of the 3rd generator 22 Become cryogen liquid, cryogen liquor stream through heater 27 and the second generator 3 and progressively heat release, after through second throttle 26 throttling entrance Evaporimeter 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 13 is realized in：
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 9, increase the 4th generator, second Choke valve, the 4th solution pump, the 4th solution heat exchanger and heater, it is molten through the 4th that weak solution pipeline set up by the second absorber 23 Liquid pump 29 is connected with the 4th generator 28 with the 4th solution heat exchanger 30, and the 4th generator 28 also has concentrated solution pipeline through the 4th Solution heat exchanger 30 is connected with the 3rd generator 22, by generator 2 have refrigerant steam channel connect with condenser 4 be adjusted to send out After raw device 2 has refrigerant steam channel to connect with the 4th generator 28, the 4th generator 28 has cryogen liquid pipeline again through heater 27th, the second generator 3 is connected with evaporimeter 6 with second throttle 26, and the 4th generator 28 also has refrigerant steam channel and condensation Device 4 connects, and heater 27 also has heated medium passage and ft connection.
(2), in flow process, the refrigerant vapour that generator 2 produces is supplied to the 4th generator 28 and makees to drive thermal medium, the second suction The part weak solution receiving device 23 enters the 4th generator 28, refrigerant vapour through the 4th solution pump 29 and the 4th solution heat exchanger 30 Flow through the 4th generator 28, heating enters its interior solution release refrigerant vapour and provides to condenser 4, the 4th generator 28 Concentrated solution enters the 3rd generator 22 through the 4th solution heat exchanger 30；Flow through the refrigerant vapour heat release Cheng Leng of the 4th generator 28 Agent liquid, cryogen liquor stream through heater 27 and the second generator 3 progressively heat release, after through second throttle 26 throttling enter evaporation Device 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 14 is realized in：
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 9, cancel choke valve, by second Raw device 3 has cryogen liquid pipeline to connect with evaporimeter 6 through choke valve 7 to be adjusted to the second generator 3 and have cryogen liquid pipeline and evaporimeter 6 Connection, increases the 4th generator, the 4th solution heat exchanger and heater, and the second absorber 23 is had weak solution pipeline through the 3rd Solution pump 24 is connected with generator 2 with the 3rd solution heat exchanger 25 and is adjusted to the second absorber 23 and has weak solution pipeline through the 3rd Solution pump 24, the 3rd solution heat exchanger 25 are connected with generator 2 with the 4th solution heat exchanger 30, generator 2 are had dense molten Liquid pipeline is connected with the 3rd generator 22 through the 3rd solution heat exchanger 25 and is adjusted to generator 2 and has concentrated solution pipeline molten through the 4th Liquid heat exchanger 30 is connected with the 4th generator 28, and the 4th generator 28 has concentrated solution pipeline again through the 3rd solution heat exchanger 25 Connect with the 3rd generator 22, by generator 2 have refrigerant steam channel connect with condenser 4 be adjusted to generator 2 have cryogen steam After vapour passage is connected with the 4th generator 28, the 4th generator 28 has cryogen liquid pipeline again through heater 27 and the second generator 3 Connect with evaporimeter 6, the 4th generator 28 also has refrigerant steam channel to connect with condenser 4, and heater 27 also has heated Jie Matter passage and ft connection, the 4th generator 28 also has high temperature thermal medium passage and ft connection.
(2), in flow process, the refrigerant vapour of high temperature thermal medium and generator 2 generation is supplied to the 4th generator 28 and makees to drive heat Medium, the weak solution of the second absorber 23 is through the 3rd solution pump 24, the 3rd solution heat exchanger 25 and the 4th solution heat exchanger 30 entrance generators 2, the concentrated solution of generator 2 enters the 4th generator 28 through the 4th solution heat exchanger 30, refrigerant vapour and High temperature thermal medium flows separately through the 4th generator 28, heating enters its interior solution release refrigerant vapour and provides to condenser 4, The concentrated solution of the 4th generator 28 enters the 3rd generator 22 through the 3rd solution heat exchanger 25；Flow through the cold of the 4th generator 22 Agent steam heat release becomes cryogen liquid, and cryogen liquid flows through heater 27 and the second generator 3 progressively heat release successively, enters evaporation afterwards Device 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 realized in：
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 9, cancel choke valve, by second Raw device 3 has cryogen liquid pipeline to connect with evaporimeter 6 through choke valve 7 to be adjusted to the second generator 3 and have cryogen liquid pipeline and evaporimeter 6 Connection, increases the 4th generator, the 4th solution pump, the 4th solution heat exchanger and heater, the second absorber 23 is had dilute molten Liquid pipeline connect with generator 2 through the 3rd solution pump 24 and the 3rd solution heat exchanger 25 be adjusted to the second absorber 23 have dilute molten Liquid pipeline is connected with the 4th generator 28 with the 3rd solution heat exchanger 25 through the 3rd solution pump 24, and the 4th generator 28 has dense again Solution line is connected with generator 2 with the 4th solution heat exchanger 30 through the 4th solution pump 29, and generator 2 is had concentrated solution pipeline Connect with the 3rd generator 22 through the 3rd solution heat exchanger 25 be adjusted to generator 2 have concentrated solution pipeline through the 4th solution heat hand over Parallel operation 30 is connected with the 3rd generator 22 with the 3rd solution heat exchanger 25, and generator 2 is had refrigerant steam channel and condenser 4 Connection is adjusted to the 4th generator 28 after generator 2 has refrigerant steam channel to connect with the 4th generator 28 cryogen liquid pipe again Road is connected with evaporimeter 6 with the second generator 3 through heater 27, and the 4th generator 28 also has refrigerant steam channel and condenser 4 Connection, heater 27 also has heated medium passage and ft connection.
(2), in flow process, the refrigerant vapour that generator 2 produces is supplied to the 4th generator 28 and makees to drive thermal medium, the second suction The weak solution receiving device 23 enters the 4th generator 28 through the 3rd solution pump 24 and the 3rd solution heat exchanger 25, and refrigerant vapour flows through 4th generator 28, heating enter its interior solution release refrigerant vapour and simultaneously provide to condenser 4, the 4th generator 28 dense molten Liquid enters generator 2 through the 4th solution pump 29 and the 4th solution heat exchanger 30, and the concentrated solution of generator 2 is handed over through the 4th solution heat Parallel operation 30 and the 3rd solution heat exchanger 25 enter the 3rd generator 22；Flow through the refrigerant vapour heat release Cheng Leng of the 4th generator 22 Agent liquid, cryogen liquid flows through heater 27 and the second generator 3 progressively heat release successively, enters evaporimeter 6 afterwards, forms the 4th class Thermal drivers compressing-absorbing type heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Figure 16 is realized in：
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 1, increase the 3rd generator, second Absorber and the 3rd solution heat exchanger, absorber 1 is had weak solution pipeline through solution pump 10 and solution heat exchanger 12 and to send out Raw device 2 connection is adjusted to absorber 1 has weak solution pipeline to connect with the second absorber 23 through the 3rd solution heat exchanger 25, and second Absorber 23 has weak solution pipeline to connect with generator 2 with solution heat exchanger 12 through solution pump 10 again, and the second generator 3 is had Concentrated solution pipeline is connected with absorber 1 through the second solution pump 11 and the second solution heat exchanger 13 and is adjusted to the second generator 3 and has Concentrated solution pipeline is connected with the 3rd generator 22 through the second solution heat exchanger 13, and the 3rd generator 22 has concentrated solution pipeline warp again Second solution pump 11 is connected with absorber 1 with the 3rd solution heat exchanger 25, and condenser 4 is had cryogen liquid pipeline through the second generation Device 3 is connected with evaporimeter 6 with choke valve 7 and is adjusted to condenser 4 and has cryogen liquid pipeline through the second generator 3, the 3rd generator 22 Connect with evaporimeter 6 with choke valve 7, the 3rd generator 22 also has refrigerant steam channel to connect with the second absorber 23, the second suction Receive device 23 and also have coolant guiding channel and ft connection.
(2), in flow process, the weak solution of absorber 1 is cold through the 3rd solution heat exchanger 25 entrance the second absorber 23, absorption Agent steam heat release enter through solution pump 10 and solution heat exchanger 12 and occur in cooling medium, the weak solution of the second absorber 23 Device 2；The concentrated solution of the second generator 3 enters the 3rd generator 22, heat absorption release refrigerant vapour through the second solution heat exchanger 13 And provide to the second absorber 23, the concentrated solution of the 3rd generator 22 is entered through the second solution pump 11 and the 3rd solution heat exchanger 25 Enter absorber 1；The part cryogen liquid of condenser 4 flows through the second generator 3 and the 3rd generator 22 progressively heat release, afterwards successively Enter evaporimeter 6 through choke valve 7 reducing pressure by regulating flow, form the 4th class thermal drivers compressing-absorbing type heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Figure 17 is realized in：
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Figure 16, 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 weak solution pipeline set up by the second absorber 23 Liquid pump 24 is connected with the 4th generator 28 with the 4th solution heat exchanger 30, and the 4th generator 28 also has concentrated solution pipeline through the 4th Solution heat exchanger 30 is connected with the second generator 3 with the second solution heat exchanger 13, by generator 2 have refrigerant steam channel with Condenser 4 connection is adjusted to the 4th generator 28 after generator 2 has refrigerant steam channel to connect with the 4th generator 28 to be had again Cryogen liquid pipeline is connected with evaporimeter 6 with second throttle 26 through heater 27, the second generator 3, the 3rd generator 22, and the 4th Generator 28 also has refrigerant steam channel to connect with condenser 4, and heater 27 also has heated medium passage and ft connection.
(2), in flow process, the refrigerant vapour that generator 2 produces is supplied to the 4th generator 28 and makees to drive thermal medium, the second suction The part weak solution receiving device 23 enters the 4th generator 28, refrigerant vapour through the 3rd solution pump 24 and the 4th solution heat exchanger 30 Flow through the 4th generator 28, heating enters its interior solution release refrigerant vapour and provides to condenser 4, the 4th generator 28 Concentrated solution enters the second generator 3 through the 4th solution heat exchanger 30 and the second solution heat exchanger 13；Flow through the 4th generator 28 refrigerant vapour heat release becomes cryogen liquid, cryogen liquid flow through successively heater 27, the second generator 3 and the 3rd generator 22 and by Step heat release, flows through second throttle 26 reducing pressure by regulating flow afterwards and enters evaporimeter 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 18 is realized in：
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Figure 16, increase the 4th generator, second Choke valve, the 4th solution heat exchanger and heater, the second absorber 23 is had weak solution pipeline through solution pump 10 and solution heat Exchanger 12 is connected with generator 2 and is adjusted to the second absorber 23 and has weak solution pipeline through solution pump 10, solution heat exchanger 12 Connect with generator 2 with the 4th solution heat exchanger 30, generator 2 is had concentrated solution pipeline through solution heat exchanger 12 and second Solution heat exchanger 13 is connected with the second generator 3 and is adjusted to generator 2 and has concentrated solution pipeline through the 4th solution heat exchanger 30 Connect with the 4th generator 28, the 4th generator 28 has concentrated solution pipeline again through solution heat exchanger 12 and the second solution heat exchange Device 13 is connected with the second generator 3, generator 2 is had refrigerant steam channel to connect with condenser 4 and is adjusted to generator 2 and has cryogen After steam channel is connected with the 4th generator 28, the 4th generator 28 has cryogen liquid pipeline again through heater 27, the second generator 3rd, the 3rd generator 22 is connected with evaporimeter 6 with second throttle 26, and the 4th generator 28 also has refrigerant steam channel and condensation Device 4 connects, and heater 27 also has heated medium passage and ft connection.
(2), in flow process, the refrigerant vapour that generator 2 produces is supplied to the 4th generator 28 and makees to drive thermal medium, the second suction The weak solution receiving device 23 enters generator 2, generator through solution pump 10, solution heat exchanger 12 and the 4th solution heat exchanger 30 2 concentrated solution through the 4th solution heat exchanger 30 enter the 4th generator 28, refrigerant vapour flow through the 4th generator 28, heat into Enter its interior solution release refrigerant vapour and provide to condenser 4, the concentrated solution of the 4th generator 28 is through solution heat exchanger 12 Enter the second generator 3 with the second solution heat exchanger 13；The refrigerant vapour heat release flowing through the 4th generator 28 becomes cryogen liquid, cold Agent liquid flows through heater 27, the second generator 3 and the 3rd generator 22 progressively heat release successively, flows through second throttle 26 afterwards Reducing pressure by regulating flow enters evaporimeter 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 19 is realized in：
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Figure 16, cancel choke valve, by the 3rd Raw device 22 has cryogen liquid pipeline to connect with evaporimeter 6 through choke valve 7 to be adjusted to the 3rd generator 22 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, the second absorber 23 is had dilute Solution line is connected with generator 2 through solution pump 10 and solution heat exchanger 12 and is adjusted to the second absorber 23 and has weak solution pipeline Connect with the 4th generator 28 with solution heat exchanger 12 through solution pump 10, the 4th generator 28 has concentrated solution pipeline again through the 3rd Solution pump 24 is connected with generator 2 with the 4th solution heat exchanger 30, and generator 2 is had concentrated solution pipeline through solution heat exchanger 12 connect with the second generator 3 with the second solution heat exchanger 13 be adjusted to generator 2 have concentrated solution pipeline through the 4th solution heat Exchanger 30, solution heat exchanger 12 are connected with the second generator 3 with the second solution heat exchanger 13, and generator 2 is had cryogen Steam channel is connected with condenser 4 and is adjusted to the 4th after generator 2 has refrigerant steam channel to connect with the 4th generator 28 Raw device 28 has cryogen liquid pipeline to connect with evaporimeter 6 with the 3rd generator 22 through heater 27, the second generator 3 again, the 4th Raw device 28 also has refrigerant steam channel to connect with condenser 4, and heater 27 also has heated medium passage and ft connection.
(2), in flow process, the refrigerant vapour that generator 2 produces is supplied to the 4th generator 28 and makees to drive thermal medium, the second suction The weak solution receiving device 23 enters the 4th generator 28 through solution pump 10 and solution heat exchanger 12, and refrigerant vapour flows through the 4th generation Device 28, heating enter its interior solution release refrigerant vapour and simultaneously provide to condenser 4, and the concentrated solution of the 4th generator 28 is through the 3rd Solution pump 24 and the 4th solution heat exchanger 30 enter generator 2, the concentrated solution of generator 2 through the 4th solution heat exchanger 30, Solution heat exchanger 12 and the second solution heat exchanger 13 enter the second generator 3；Flow through the refrigerant vapour of the 4th generator 28 Heat release becomes cryogen liquid, and cryogen liquid flows through heater 27, the second generator 3 and the 3rd generator 22 progressively heat release successively, afterwards Enter evaporimeter 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 20 is realized in：
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 9, increase the 4th generator, the 3rd Absorber and the 4th solution heat exchanger, absorber 1 is had weak solution pipeline through solution pump 10 and solution heat exchanger 12 and Two absorber 23 connection is adjusted to absorber 1 has weak solution pipeline the 4th solution heat exchanger 30 to connect with the 3rd absorber 31, 3rd absorber 31 has weak solution pipeline to connect with the second absorber 23 with solution heat exchanger 12 through solution pump 10 again, by second Generator 3 has concentrated solution pipeline to connect with absorber 1 with the second solution heat exchanger 13 through the second solution pump 11 to be adjusted to second Generator 3 has concentrated solution pipeline to connect with the 4th generator 28 through the second solution heat exchanger 13, and the 4th generator 28 has dense again Solution line is connected with absorber 1 with the 4th solution heat exchanger 30 through the second solution pump 11, and condenser 4 is had cryogen liquid pipeline Connect with evaporimeter 6 through the second generator 3 and choke valve 7 be adjusted to condenser 4 have cryogen liquid pipeline through the second generator 3, Four generators 28 are connected with evaporimeter 6 with choke valve 7, and the 4th generator 28 also has refrigerant steam channel with the 3rd absorber 31 even Logical, the 3rd absorber 31 also has coolant guiding channel and ft connection.
(2), in flow process, the weak solution of absorber 1 is cold through the 4th solution heat exchanger 30 entrance the 3rd absorber 31, absorption Agent steam heat release enter second in cooling medium, the weak solution of the 3rd absorber 31 through solution pump 10 and solution heat exchanger 12 Absorber 23；The concentrated solution of the second generator 3 enters the 4th generator 28, heat absorption release cryogen through the second solution heat exchanger 13 Steam simultaneously provides to the 3rd absorber 31, and the concentrated solution of the 4th generator 28 is through the second solution pump 11 and the 4th solution heat exchanger 30 entrance absorbers 1；The part cryogen liquid of condenser 4 flows through the second generator 3 and the 4th generator 28 progressively heat release successively, Flow through choke valve 7 reducing pressure by regulating flow afterwards and enter evaporimeter 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 21 is realized in：
(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 3rd solution pump and the 3rd solution heat exchanger, generator 2 is had refrigerant steam channel to connect adjustment with condenser 4 Refrigerant steam channel is had to connect with the second absorber 23 for generator 2, the second absorber 23 also has weak solution pipeline molten through the 3rd Liquid pump 24 is connected with the 3rd generator 22 with the 3rd solution heat exchanger 25, and the 3rd generator 22 also has concentrated solution pipeline through the 3rd Solution heat exchanger 25 is connected with the second absorber 23, and the 3rd generator 22 also has refrigerant steam channel to connect with condenser 4, the Three generators 22 also have high temperature thermal medium passage and ft connection, and the second absorber 23 also has heated medium passage to connect with outside Logical.
(2), in flow process, the refrigerant vapour that generator 2 produces enters the second absorber 23, the weak solution of the second absorber 23 Enter the 3rd generator 22 through the 3rd solution pump 24 and the 3rd solution heat exchanger 25, high temperature thermal medium flows through the 3rd generator 22nd, heating enters its interior solution release refrigerant vapour and provides to condenser 4, and the concentrated solution of the 3rd generator 22 is molten through the 3rd Liquid heat exchanger 25 enters the second absorber 23, absorbs refrigerant vapour and heat release is in heated medium, forms the 4th class thermal drivers Compressing-absorbing type heat pump.
Effect that the technology of the present invention can be realized the 4th class thermal drivers compressing-absorbing type heat proposed by the invention Pump, has the effect that and advantage：
(1) new approaches and the new technology of temperature difference utilization are proposed.
(2) heat energy (temperature difference) drives, and realizes heat supply/refrigeration, or may be selected externally to provide power simultaneously.
(3) rationally, performance index is variable and corresponding with thermodynamic parameter change, is capable of heat energy (temperature difference) for flow process Fully and efficient utilization.
(4) if necessary, realize heat supply/refrigeration by external impetus, flexibly, adaptability is good for mode.
(5) effectively utilizes of high temperature heat are realized, it is to avoid conflicting between high temperature thermal medium parameter and solution property, make up The deficiency of absorption heat pump technology.
(6) effectively utilizes of low temperature heat energy are realized, it is to avoid conflicting between low-temperature heat medium parameter and solution property, make up The deficiency of absorption heat pump technology.
(7) compare thermal drivers compression heat pump, refrigerant vapour boosting is completed using absorption heat pump flow process, reduces motion portion Part, improves device security, reduces on environmentally undesirable impact.
(8) provide multiple concrete technical schemes, cope with numerous different actual states, have the wider scope of application.
(9) extend heat pump techniques, enrich the type of compressing-absorbing type heat pump, be conducive to heat energy height is better achieved Effect utilizes.

Claims (32)

1. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, the second generator, condenser, second Condenser, evaporimeter, choke valve, cryogen liquid pump, the second cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, Two solution heat exchangers, high-temperature heat exchanger, decompressor, compressor and the second decompressor are formed；Absorber (1) has weak solution Pipeline is connected with generator (2) with solution heat exchanger (12) through solution pump (10), and generator (2) also has concentrated solution pipeline through molten Liquid heat exchanger (12) is connected with the second generator (3) with the second solution heat exchanger (13), and the second generator (3) also has dense molten Liquid pipeline is connected with absorber (1) with the second solution heat exchanger (13) through the second solution pump (11), and generator (2) also has cryogen Steam channel is connected with condenser (4), and the second generator (3) also has refrigerant steam channel to connect with the second condenser (5), condensation Device (4) also has cryogen liquid pipeline to connect with evaporimeter (6) with choke valve (7) through the second generator (3), and condenser (4) is also cold After agent liquid pipeline is connected with high-temperature heat exchanger (14) through cryogen liquid pump (8), high-temperature heat exchanger (14) has refrigerant vapour to lead to again Road is connected with decompressor (15), and decompressor (15) also has refrigerant steam channel to connect with evaporimeter (6) or the second condenser (5), Second condenser (5) also has cryogen liquid pipeline to connect with evaporimeter (6) through the second cryogen liquid pump (9), and evaporimeter (6) also has cryogen Steam channel is connected with absorber (1), and outside has low-temperature heat medium passage to connect with compressor (16), and compressor (16) is also low Warm passage is connected with the second decompressor (17) through evaporimeter (6), and the second decompressor (17) also has low-temperature heat medium passage With ft connection, generator (2) and high-temperature heat exchanger (14) also have high temperature thermal medium passage and ft connection, absorber respectively (1) and condenser (4) also has heated medium passage and ft connection respectively, the second condenser (5) also has low-temperature heat medium to lead to Road and ft connection, decompressor (15) and the second decompressor (17) connect compressor (16) and transmit power, form the 4th class heat Drive compression-absorption heat pump；Wherein, or decompressor (15) and the second decompressor (17) connect compressor (16), cryogen liquid pump (8), the second cryogen liquid pump (9), solution pump (10) and the second solution pump (11) transmit power.
2. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, the second generator, condenser, second Condenser, evaporimeter, choke valve, cryogen liquid pump, the second cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, Two solution heat exchangers, high-temperature heat exchanger, decompressor, compressor, the second decompressor and the second compressor are formed；Absorber (1) weak solution pipeline is had to connect with generator (2) with solution heat exchanger (12) through solution pump (10), generator (2) is also dense Solution line is connected with the second generator (3) with the second solution heat exchanger (13) through solution heat exchanger (12), the second generation Device (3) also has concentrated solution pipeline to connect with absorber (1) with the second solution heat exchanger (13) through the second solution pump (11), occurs Device (2) also has refrigerant steam channel to connect with condenser (4), and the second generator (3) also has refrigerant steam channel and the second condensation Device (5) connects, and condenser (4) also has cryogen liquid pipeline to connect with evaporimeter (6) with choke valve (7) through the second generator (3), cold Condenser (4) also have cryogen liquid pipeline connect with high-temperature heat exchanger (14) through cryogen liquid pump (8) after high-temperature heat exchanger (14) Refrigerant steam channel is had to connect with decompressor (15) again, decompressor (15) also has refrigerant steam channel and evaporimeter (6) or second Condenser (5) connects, and the second condenser (5) also has cryogen liquid pipeline to connect with evaporimeter (6) through the second cryogen liquid pump (9), steams Sending out device (6) also has refrigerant steam channel to connect with absorber (1), and outside has low-temperature heat medium passage to connect with compressor (16), Compressor (16) also has low-temperature heat medium passage to connect with the second compressor (18) through evaporimeter (6), and the second compressor (18) is also Low-temperature heat medium passage is had to connect with the second decompressor (17) through evaporimeter (6), the second decompressor (17) also has low-temperature heat medium Passage and ft connection, generator (2) and high-temperature heat exchanger (14) also have high temperature thermal medium passage and ft connection respectively, inhale Receive device (1) and condenser (4) also has heated medium passage and ft connection respectively, the second condenser (5) also has Low Temperature Thermal to be situated between Matter passage and ft connection, decompressor (15) and the second decompressor (17) connect compressor (16) and the second compressor (18) and pass Defeated power, forms the 4th class thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor (15) and the second decompressor (17) connect Compressor (16), the second compressor (18), cryogen liquid pump (8), the second cryogen liquid pump (9), solution pump (10) and the second solution pump And transmit power (11).
3. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, the second generator, condenser, second Condenser, evaporimeter, choke valve, cryogen liquid pump, the second cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, Two solution heat exchangers, high-temperature heat exchanger, decompressor, compressor, the second decompressor and regenerator are formed；Absorber (1) Weak solution pipeline is had to connect with generator (2) with solution heat exchanger (12) through solution pump (10), generator (2) also has concentrated solution Pipeline is connected with the second generator (3) with the second solution heat exchanger (13) through solution heat exchanger (12), the second generator (3) Concentrated solution pipeline is also had to connect with absorber (1) with the second solution heat exchanger (13) through the second solution pump (11), generator (2) Refrigerant steam channel is also had to connect with condenser (4), the second generator (3) also has refrigerant steam channel and the second condenser (5) Connection, condenser (4) also has cryogen liquid pipeline to connect with evaporimeter (6) with choke valve (7) through the second generator (3), condenser (4) after also having cryogen liquid pipeline to connect with high-temperature heat exchanger (14) through cryogen liquid pump (8), high-temperature heat exchanger (14) has again Refrigerant steam channel is connected with decompressor (15), and decompressor (15) also has refrigerant steam channel and evaporimeter (6) or the second condensation Device (5) connects, and the second condenser (5) also has cryogen liquid pipeline to connect with evaporimeter (6) through the second cryogen liquid pump (9), evaporimeter (6) refrigerant steam channel is also had to connect with absorber (1), there is low-temperature heat medium passage outside through regenerator (19) and compressor (16) connect, compressor (16) also has low-temperature heat medium passage through evaporimeter (6) and regenerator (19) and the second decompressor (17) Connection, the second decompressor (17) also has low-temperature heat medium passage and ft connection, generator (2) and high-temperature heat exchanger (14) also High temperature thermal medium passage and ft connection, absorber (1) and condenser (4) is had also to have heated medium passage respectively with outward respectively Portion connects, and the second condenser (5) also has low-temperature heat medium passage and ft connection, decompressor (15) and the second decompressor (17) even Connect compressor (16) and transmit power, form the 4th class thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor (15) and Two decompressors (17) connect compressor (16), cryogen liquid pump (8), the second cryogen liquid pump (9), solution pump (10) and the second solution pump And transmit power (11).
4. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, the second generator, condenser, second Condenser, evaporimeter, choke valve, cryogen liquid pump, the second cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, Two solution heat exchangers, high-temperature heat exchanger, decompressor, compressor, the second decompressor and low temperature heat exchanger are formed；Absorb Device (1) has weak solution pipeline to connect with generator (2) with solution heat exchanger (12) through solution pump (10), and generator (2) also has Concentrated solution pipeline is connected with the second generator (3) with the second solution heat exchanger (13) through solution heat exchanger (12), second Raw device (3) also has concentrated solution pipeline to connect with absorber (1) with the second solution heat exchanger (13) through the second solution pump (11), sends out Raw device (2) also has refrigerant steam channel to connect with condenser (4), and the second generator (3) also has refrigerant steam channel cold with second Condenser (5) connects, and condenser (4) also has cryogen liquid pipeline to connect with evaporimeter (6) with choke valve (7) through the second generator (3), Condenser (4) also have cryogen liquid pipeline connect with high-temperature heat exchanger (14) through cryogen liquid pump (8) after high-temperature heat exchanger (14) have refrigerant steam channel to connect with decompressor (15) again, decompressor (15) also have refrigerant steam channel and evaporimeter (6) or Second condenser (5) connects, and the second condenser (5) also has cryogen liquid pipeline through the second cryogen liquid pump (9) with evaporimeter (6) even Logical, evaporimeter (6) also has refrigerant steam channel to connect with absorber (1), and compressor (16) has cycle fluid passage through evaporimeter (6) connect with the second decompressor (17), the second decompressor (17) also has cycle fluid passage through low temperature heat exchanger (20) and pressure Contracting machine (16) connects, and generator (2) and high-temperature heat exchanger (14) also have high temperature thermal medium passage and ft connection respectively, absorbs Device (1) and condenser (4) also have heated medium passage and ft connection, the second condenser (5) and low temperature heat exchanger respectively (20) low-temperature heat medium passage and ft connection, decompressor (15) and the second decompressor (17) is also had to connect compressor (16) respectively And transmit power, form the 4th class thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor (15) and the second decompressor (17) Connect compressor (16), cryogen liquid pump (8), the second cryogen liquid pump (9), solution pump (10) and the second solution pump (11) and transmit dynamic Power.
5. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, the second generator, condenser, second Condenser, evaporimeter, choke valve, cryogen liquid pump, the second cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, Two solution heat exchangers, high-temperature heat exchanger, decompressor and compressor are formed；Absorber (1) has weak solution pipeline through solution Pump (10) is connected with generator (2) with solution heat exchanger (12), and generator (2) also has concentrated solution pipeline through solution heat exchanger (12) with the second solution heat exchanger (13) is connected with the second generator (3), and the second generator (3) also has concentrated solution pipeline through the Two solution pumps (11) are connected with absorber (1) with the second solution heat exchanger (13), generator (2) also have refrigerant steam channel with Condenser (4) connects, and the second generator (3) also has refrigerant steam channel to connect with the second condenser (5), and condenser (4) also has Cryogen liquid pipeline is connected with evaporimeter (6) with choke valve (7) through the second generator (3), and condenser (4) also has cryogen liquid pipeline warp After cryogen liquid pump (8) is connected with high-temperature heat exchanger (14), high-temperature heat exchanger (14) has refrigerant steam channel and decompressor again (15) connect, decompressor (15) also has refrigerant steam channel to connect with evaporimeter (6) or the second condenser (5), the second condenser (5) also have cryogen liquid pipeline connect with evaporimeter (6) through the second cryogen liquid pump (9), evaporimeter (6) also refrigerant steam channel and Absorber (1) connects, and outside has low-temperature heat medium passage to connect with compressor (16), and compressor (16) also has low-temperature heat medium to lead to Through evaporimeter (6) and ft connection, generator (2) and high-temperature heat exchanger (14) also have high temperature thermal medium passage respectively with outward in road Portion connects, and absorber (1) and condenser (4) also have heated medium passage and ft connection respectively, and the second condenser (5) also has Low-temperature heat medium passage and ft connection, decompressor (15) connects compressor (16) and transmits power, forms the 4th class thermal drivers Compressing-absorbing type heat pump；Wherein, or decompressor (15) connect compressor (16), cryogen liquid pump (8), the second cryogen liquid pump (9), Solution pump (10) and the second solution pump (11) simultaneously transmit power.
6. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, the second generator, condenser, second Condenser, evaporimeter, choke valve, cryogen liquid pump, the second cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, Two solution heat exchangers, high-temperature heat exchanger, decompressor, compressor, low temperature heat exchanger and cryogenic throttle valve are formed；Absorb Device (1) has weak solution pipeline to connect with generator (2) with solution heat exchanger (12) through solution pump (10), and generator (2) also has Concentrated solution pipeline is connected with the second generator (3) with the second solution heat exchanger (13) through solution heat exchanger (12), second Raw device (3) also has concentrated solution pipeline to connect with absorber (1) with the second solution heat exchanger (13) through the second solution pump (11), sends out Raw device (2) also has refrigerant steam channel to connect with condenser (4), and the second generator (3) also has refrigerant steam channel cold with second Condenser (5) connects, and condenser (4) also has cryogen liquid pipeline to connect with evaporimeter (6) with choke valve (7) through the second generator (3), Condenser (4) also have cryogen liquid pipeline connect with high-temperature heat exchanger (14) through cryogen liquid pump (8) after high-temperature heat exchanger (14) have refrigerant steam channel to connect with decompressor (15) again, decompressor (15) also have refrigerant steam channel and evaporimeter (6) or Second condenser (5) connects, and the second condenser (5) also has cryogen liquid pipeline through the second cryogen liquid pump (9) with evaporimeter (6) even Logical, evaporimeter (6) also has refrigerant steam channel to connect with absorber (1), and compressor (16) has cycle fluid passage through evaporimeter (6) connect with low temperature heat exchanger (20) with cryogenic throttle valve (21), low temperature heat exchanger (20) also have cycle fluid passage with Compressor (16) connects, and generator (2) and high-temperature heat exchanger (14) also have high temperature thermal medium passage and ft connection respectively, inhales Receive device (1) and condenser (4) also has heated medium passage and ft connection, the second condenser (5) and low temperature heat exchange respectively Device (20) also has low-temperature heat medium passage and ft connection respectively, and decompressor (15) connects compressor (16) and transmits power, shape Become the 4th class thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor (15) connect compressor (16), cryogen liquid pump (8), the Two cryogen liquid pumps (9), solution pump (10) and the second solution pump (11) simultaneously transmit power.
7. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, the second generator, condenser, second Condenser, evaporimeter, choke valve, cryogen liquid pump, the second cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, Two solution heat exchangers, high-temperature heat exchanger, decompressor, compressor, the second compressor, low temperature heat exchanger and cryogenic throttle valve Formed；Absorber (1) has weak solution pipeline to connect with generator (2) with solution heat exchanger (12) through solution pump (10), sends out Raw device (2) also has concentrated solution pipeline through solution heat exchanger (12) and the second solution heat exchanger (13) and the second generator (3) Connection, the second generator (3) also has concentrated solution pipeline through the second solution pump (11) and the second solution heat exchanger (13) and absorption Device (1) connects, and generator (2) also has refrigerant steam channel to connect with condenser (4), and the second generator (3) also has refrigerant vapour Passage is connected with the second condenser (5), and condenser (4) also has cryogen liquid pipeline through the second generator (3) and choke valve (7) and steaming Send out device (6) connection, condenser (4) also has cryogen liquid pipeline high after connecting with high-temperature heat exchanger (14) through cryogen liquid pump (8) Temperature heat exchanger (14) has refrigerant steam channel to connect with decompressor (15) again, and decompressor (15) also has refrigerant steam channel and steaming Send out device (6) or the second condenser (5) connection, the second condenser (5) also has cryogen liquid pipeline through the second cryogen liquid pump (9) and evaporation Device (6) connects, and evaporimeter (6) also has refrigerant steam channel to connect with absorber (1), and compressor (16) has cycle fluid passage warp Evaporimeter (6) is connected with the second compressor (18), and the second compressor (18) also has cycle fluid passage through evaporimeter (6) and low temperature Choke valve (21) is connected with low temperature heat exchanger (20), and low temperature heat exchanger (20) also has cycle fluid passage and compressor (16) Connection, generator (2) and high-temperature heat exchanger (14) also have high temperature thermal medium passage and ft connection respectively, absorber (1) and Condenser (4) also has heated medium passage and ft connection, the second condenser (5) and low temperature heat exchanger (20) also to divide respectively There are not low-temperature heat medium passage and ft connection, decompressor (15) connects compressor (16) and the second compressor (18) and transmits dynamic Power, forms the 4th class thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor (15) connect compressor (16), the second compressor (18), cryogen liquid pump (8), the second cryogen liquid pump (9), solution pump (10) and the second solution pump (11) transmit power.
8. the 4th class thermal drivers compressing-absorbing type heat pump, be described in claim 1-7 arbitrary 4th class thermal drivers compression- In absorption heat pump, increase the 3rd generator, the second absorber, the 3rd solution pump and the 3rd solution heat exchanger, by absorber (1) there is weak solution pipeline to connect with generator (2) through solution pump (10) and solution heat exchanger (12) to be adjusted to absorber (1) and have Weak solution pipeline is connected with the second absorber (23) with solution heat exchanger (12) through solution pump (10), and the second absorber (23) is again Weak solution pipeline is had to connect with generator (2) with the 3rd solution heat exchanger (25) through the 3rd solution pump (24), by generator (2) There is concentrated solution pipeline to connect with the second generator (3) with the second solution heat exchanger (13) through solution heat exchanger (12) to be adjusted to Generator (2) has concentrated solution pipeline to connect with the 3rd generator (22) through the 3rd solution heat exchanger (25), the 3rd generator (22) concentrated solution pipeline is had to connect with the second generator (3) through solution heat exchanger (12) and the second solution heat exchanger (13) again Logical, the 3rd generator (22) also has refrigerant steam channel to connect with the second absorber (23), and the 3rd generator (22) also has high temperature Hot media channel and ft connection, the second absorber (23) also has heated medium passage and ft connection, forms the 4th class heat Drive compression-absorption heat pump.
9. the 4th class thermal drivers compressing-absorbing type heat pump, be described in claim 1-8 arbitrary 4th class thermal drivers compression- In absorption heat pump, cancel choke valve, condenser (4) is had cryogen liquid pipeline through the second generator (3) and choke valve (7) and steaming Send out device (6) connection to be adjusted to condenser (4) and have cryogen liquid pipeline to connect with evaporimeter (6) through the second generator (3), formation 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 1-7 arbitrary 4th class thermal drivers compression- In absorption heat pump, increase the 3rd generator, second throttle, the 3rd solution pump, the 3rd solution heat exchanger and heater, inhale Receipts device (1) are set up weak solution pipeline and are connected with the 3rd generator (22) through the 3rd solution pump (24) and the 3rd solution heat exchanger (25) Logical, the 3rd generator (22) also have concentrated solution pipeline through the 3rd solution heat exchanger (25) and the second solution heat exchanger (13) and Second generator (3) connect, by generator (2) have refrigerant steam channel connect with condenser (4) be adjusted to generator (2) have cold Agent steam channel connect with the 3rd generator (22) after the 3rd generator (22) have again cryogen liquid pipeline through heater (27), Two generators (3) are connected with evaporimeter (6) with second throttle (26), the 3rd generator (22) also have refrigerant steam channel with cold Condenser (4) connects, and heater (27) also has heated medium passage and ft connection, forms the 4th class thermal drivers compression-absorption Formula heat pump.
11. the 4th class thermal drivers compressing-absorbing type heat pumps, be described in claim 1-7 arbitrary 4th class thermal drivers compression- In absorption heat pump, increase the 3rd generator, second throttle, the 3rd solution heat exchanger and heater, absorber (1) is had Weak solution pipeline connect with generator (2) through solution pump (10) and solution heat exchanger (12) be adjusted to absorber (1) have dilute molten Liquid pipeline is connected with generator (2) with the 3rd solution heat exchanger (25) through solution pump (10), solution heat exchanger (12), will send out Raw device (2) has concentrated solution pipeline to connect with the second generator (3) through solution heat exchanger (12) and the second solution heat exchanger (13) Logical be adjusted to generator (2) and have concentrated solution pipeline to connect with the 3rd generator (22) through the 3rd solution heat exchanger (25), the 3rd Generator (22) has concentrated solution pipeline again through solution heat exchanger (12) and the second solution heat exchanger (13) and the second generator (3) connect, generator (2) is had refrigerant steam channel to connect with condenser (4) and is adjusted to generator (2) and has refrigerant steam channel After connecting with the 3rd generator (22), the 3rd generator (22) has cryogen liquid pipeline again through heater (27), the second generator (3) connect with evaporimeter (6) with second throttle (26), the 3rd generator (22) also has refrigerant steam channel and condenser (4) Connection, heater (27) also has heated medium passage and ft connection, forms the 4th class thermal drivers compressing-absorbing type heat pump.
12. the 4th class thermal drivers compressing-absorbing type heat pumps, be described in claim 1-7 arbitrary 4th class thermal drivers compression- In absorption heat pump, increase the 3rd generator, second throttle, the 3rd solution pump, the 3rd solution heat exchanger and heater, will Absorber (1) has weak solution pipeline to connect with generator (2) with solution heat exchanger (12) through solution pump (10) to be adjusted to absorption Device (1) has weak solution pipeline to connect with the 3rd generator (22) with solution heat exchanger (12) through solution pump (10), the 3rd generation Device (22) has concentrated solution pipeline to connect with generator (2) with the 3rd solution heat exchanger (25) through the 3rd solution pump (24) again, will Generator (2) has concentrated solution pipeline through solution heat exchanger (12) and the second solution heat exchanger (13) and the second generator (3) Connection is adjusted to generator (2) has concentrated solution pipeline through the 3rd solution heat exchanger (25), solution heat exchanger (12) and second Solution heat exchanger (13) is connected with the second generator (3), and generator (2) is had refrigerant steam channel to connect with condenser (4) Being adjusted to the 3rd generator (22) after generator (2) has refrigerant steam channel to connect with the 3rd generator (22) has cryogen liquid again Pipeline is connected with evaporimeter (6) with second throttle (26) through heater (27), the second generator (3), the 3rd generator (22) Refrigerant steam channel is also had connect with condenser (4), heater (27) also heated medium passage and ft connection, formation the Four class thermal drivers compressing-absorbing type heat pumps.
13. the 4th class thermal drivers compressing-absorbing type heat pumps, are the arbitrary 4th class thermal drivers compression-suctions described in claim 8 In receipts formula heat pump, increase the 4th generator, second throttle, the 4th solution pump, the 4th solution heat exchanger and heater, second Absorber (23) sets up weak solution pipeline through the 4th solution pump (29) and the 4th solution heat exchanger (30) and the 4th generator (28) connect, the 4th generator (28) also has concentrated solution pipeline through the 4th solution heat exchanger (30) with the 3rd generator (22) even Logical, generator (2) there is is refrigerant steam channel to connect with condenser (4) and is adjusted to generator (2) and has refrigerant steam channel and the Four generators (28) connection after the 4th generator (28) have again cryogen liquid pipeline through heater (27), the second generator (3) and Second throttle (26) is connected with evaporimeter (6), and the 4th generator (28) also has refrigerant steam channel to connect with condenser (4), Heater (27) also has heated medium passage 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 arbitrary 4th class thermal drivers compression-suctions described in claim 8 In receipts formula heat pump, increase the 4th generator, second throttle, the 4th solution heat exchanger and heater, by the second absorber (23) there is weak solution pipeline to connect with generator (2) through the 3rd solution pump (24) and the 3rd solution heat exchanger (25) and be adjusted to Two absorbers (23) have weak solution pipeline through the 3rd solution pump (24), the 3rd solution heat exchanger (25) and the 4th solution heat exchange Device (30) is connected with generator (2), and generator (2) is had concentrated solution pipeline through the 3rd solution heat exchanger (25) and the 3rd generation Device (22) connection is adjusted to generator (2) has concentrated solution pipeline through the 4th solution heat exchanger (30) with the 4th generator (28) even Logical, the 4th generator (28) has concentrated solution pipeline to connect with the 3rd generator (22) through the 3rd solution heat exchanger (25) again, will Generator (2) has refrigerant steam channel to connect with condenser (4) to be adjusted to generator (2) and have refrigerant steam channel and the 4th generation After device (28) connection, the 4th generator (28) has cryogen liquid pipeline again through heater (27), the second generator (3) and second section Stream valve (26) is connected with evaporimeter (6), and the 4th generator (28) also has refrigerant steam channel to connect with condenser (4), heater (27) also have heated medium passage and ft connection, form the 4th class thermal drivers compressing-absorbing type heat pump.
15. the 4th class thermal drivers compressing-absorbing type heat pumps, are the arbitrary 4th class thermal drivers compression-suctions described in claim 8 In receipts formula heat pump, increase the 4th generator, second throttle, the 4th solution pump, the 4th solution heat exchanger and heater, by the Two absorbers (23) have weak solution pipeline to connect with generator (2) with the 3rd solution heat exchanger (25) through the 3rd solution pump (24) Being adjusted to the second absorber (23) has weak solution pipeline through the 3rd solution pump (24) and the 3rd solution heat exchanger (25) and the 4th Generator (28) connects, and the 4th generator (28) has concentrated solution pipeline again through the 4th solution pump (29) and the 4th solution heat exchanger (30) connect with generator (2), generator (2) is had concentrated solution pipeline through the 3rd solution heat exchanger (25) and the 3rd generator (22) connection is adjusted to generator (2) has concentrated solution pipeline through the 4th solution heat exchanger (30) and the 3rd solution heat exchanger (25) connect with the 3rd generator (22), generator (2) is had refrigerant steam channel to connect with condenser (4) and is adjusted to generator (2) after having refrigerant steam channel to connect with the 4th generator (28), the 4th generator (28) has cryogen liquid pipeline again through heater (27), the second generator (3) is connected with evaporimeter (6) with second throttle (26), and the 4th generator (28) also has refrigerant vapour Passage is connected with condenser (4), and heater (27) also has heated medium passage and ft connection, forms the 4th class thermal drivers pressure Contracting-absorption heat pump.
16. the 4th class thermal drivers compressing-absorbing type heat pumps, are the arbitrary 4th class thermal drivers pressures described in claim 10-12 Contracting-absorption heat pump, the 3rd generator (22) sets up high temperature thermal medium passage and ft connection, forms the 4th class thermal drivers pressure Contracting-absorption heat pump.
17. the 4th class thermal drivers compressing-absorbing type heat pumps, are the arbitrary 4th class thermal drivers pressures described in claim 13-15 Contracting-absorption heat pump, the 4th generator (28) sets up high temperature thermal medium passage and ft connection, forms the 4th class thermal drivers pressure Contracting-absorption heat pump.
18. the 4th class thermal drivers compressing-absorbing type heat pumps, are the arbitrary 4th class thermal drivers pressures described in claim 10-17 Contracting-absorption heat pump, cancels choke valve and second throttle, by the second generator (3) have cryogen liquid pipeline through choke valve (7) with Evaporimeter (6) connection is adjusted to the second generator (3) has cryogen liquid pipeline to connect with evaporimeter (6), and the second generator (3) is had Cryogen liquid pipeline is connected with evaporimeter (6) through second throttle (26) and is adjusted to the second generator (3) and has cryogen liquid pipeline and steaming Send out device (6) connection, form the 4th class thermal drivers compressing-absorbing type heat pump.
19. the 4th class thermal drivers compressing-absorbing type heat pumps, be described in claim 1-7 arbitrary 4th class thermal drivers compression- In absorption heat pump, increase the 3rd generator, the second absorber and the 3rd solution heat exchanger, absorber (1) is had weak solution Pipeline is connected with generator (2) through solution pump (10) and solution heat exchanger (12) and is adjusted to absorber (1) and has weak solution pipeline Connect with the second absorber (23) through the 3rd solution heat exchanger (25), the second absorber (23) has weak solution pipeline again through solution Pump (10) is connected with generator (2) with solution heat exchanger (12), and the second generator (3) is had concentrated solution pipeline through the second solution Pump (11) is connected with absorber (1) with the second solution heat exchanger (13) and is adjusted to the second generator (3) and has concentrated solution pipeline warp Second solution heat exchanger (13) is connected with the 3rd generator (22), and the 3rd generator (22) has concentrated solution pipeline molten through second again Liquid pump (11) is connected with absorber (1) with the 3rd solution heat exchanger (25), and condenser (4) is had cryogen liquid pipeline through second Raw device (3) connect with evaporimeter (6) with choke valve (7) be adjusted to condenser (4) have cryogen liquid pipeline through the second generator (3), 3rd generator (22) is connected with evaporimeter (6) with choke valve (7), and the 3rd generator (22) also has refrigerant steam channel and second Absorber (23) connects, and the second absorber (23) also has coolant guiding channel or low-temperature heat medium passage and ft connection, is formed 4th class thermal drivers compressing-absorbing type heat pump.
20. the 4th class thermal drivers compressing-absorbing type heat pumps, be described in claim 19 arbitrary 4th class thermal drivers compression- In absorption heat pump, cancel choke valve, the 3rd generator (22) is had cryogen liquid pipeline through choke valve (7) with evaporimeter (6) even Logical be adjusted to the 3rd generator (22) and have cryogen liquid pipeline to connect with evaporimeter (6), formation the 4th class thermal drivers compressing-absorbing type Heat pump.
21. the 4th class thermal drivers compressing-absorbing type heat pumps, be described in claim 19 arbitrary 4th class thermal drivers compression- In absorption heat pump, increase the 4th generator, second throttle, the 3rd solution pump, the 4th solution heat exchanger and heater, the Two absorbers (23) set up weak solution pipeline through the 3rd solution pump (24) and the 4th solution heat exchanger (30) and the 4th generator (28) connect, the 4th generator (28) also has concentrated solution pipeline through the 4th solution heat exchanger (30) and the second solution heat exchanger (13) connect with the second generator (3), generator (2) is had refrigerant steam channel to connect with condenser (4) and is adjusted to generator (2) after having refrigerant steam channel to connect with the 4th generator (28), the 4th generator (28) has cryogen liquid pipeline again through heater (27), the second generator (3), the 3rd generator (22) are connected with evaporimeter (6) with second throttle (26), the 4th generator (28) refrigerant steam channel is also had to connect with condenser (4), heater (27) also has heated medium passage and ft connection, shape Become the 4th class thermal drivers compressing-absorbing type heat pump.
22. the 4th class thermal drivers compressing-absorbing type heat pumps, be described in claim 19 arbitrary 4th class thermal drivers compression- In absorption heat pump, increase the 4th generator, second throttle, the 4th solution heat exchanger and heater, by the second absorber (23) there is weak solution pipeline to connect with generator (2) with solution heat exchanger (12) through solution pump (10) and be adjusted to the second absorber (23) there is weak solution pipeline through solution pump (10), solution heat exchanger (12) and the 4th solution heat exchanger (30) and generator (2) connect, generator (2) is had concentrated solution pipeline through solution heat exchanger (12) and the second solution heat exchanger (13) and second Generator (3) connection is adjusted to generator (2) has concentrated solution pipeline through the 4th solution heat exchanger (30) and the 4th generator (28) connect, the 4th generator (28) has concentrated solution pipeline again through solution heat exchanger (12) and the second solution heat exchanger (13) Connect with the second generator (3), generator (2) is had refrigerant steam channel to connect with condenser (4) and is adjusted to generator (2) and has Refrigerant steam channel connect with the 4th generator (28) after the 4th generator (28) have again cryogen liquid pipeline through heater (27), Second generator (3), the 3rd generator (22) are connected with evaporimeter (6) with second throttle (26), and the 4th generator (28) is also There is refrigerant steam channel to connect with condenser (4), heater (27) 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, be described in claim 19 arbitrary 4th class thermal drivers compression- In absorption heat pump, increase the 4th generator, second throttle, the 3rd solution pump, the 4th solution heat exchanger and heater, will Second absorber (23) has weak solution pipeline to connect with generator (2) with solution heat exchanger (12) through solution pump (10) to be adjusted to Second absorber (23) has weak solution pipeline to connect with the 4th generator (28) with solution heat exchanger (12) through solution pump (10), 4th generator (28) has concentrated solution pipeline again through the 3rd solution pump (24) and the 4th solution heat exchanger (30) and generator (2) Connection, generator (2) is had concentrated solution pipeline through solution heat exchanger (12) and the second solution heat exchanger (13) and second Raw device (3) connection is adjusted to generator (2) has concentrated solution pipeline through the 4th solution heat exchanger (30), solution heat exchanger (12) Connect with the second generator (3) with the second solution heat exchanger (13), generator (2) is had refrigerant steam channel and condenser (4) connection is adjusted to after generator (2) has refrigerant steam channel to connect the 4th generator (28) with the 4th generator (28) again There is cryogen liquid pipeline through heater (27), the second generator (3), the 3rd generator (22) and second throttle (26) and evaporimeter (6) connect, the 4th generator (28) also has refrigerant steam channel to connect with condenser (4), heater (27) also has heated Jie Matter passage and ft connection, form the 4th class thermal drivers compressing-absorbing type heat pump.
24. the 4th class thermal drivers compressing-absorbing type heat pumps, are the arbitrary 4th class thermal drivers pressures described in claim 21-23 Contracting-absorption heat pump, the 4th generator (28) sets up high temperature thermal medium passage and ft connection, forms the 4th class thermal drivers pressure Contracting-absorption heat pump.
25. the 4th class thermal drivers compressing-absorbing type heat pumps, are the arbitrary 4th class thermal drivers pressures described in claim 21-24 In contracting-absorption heat pump, cancel choke valve and second throttle, the 3rd generator (22) is had cryogen liquid pipeline through choke valve (7) connect with evaporimeter (6) and be adjusted to the 3rd generator (22) and have cryogen liquid pipeline to connect with evaporimeter (6), the 3rd is occurred Device (22) has cryogen liquid pipeline to connect with evaporimeter (6) through second throttle (26) to be adjusted to the 3rd generator (22) and have cryogen liquid Pipeline is connected with evaporimeter (6), forms the 4th class thermal drivers compressing-absorbing type heat pump.
26. the 4th class thermal drivers compressing-absorbing type heat pumps, are the arbitrary 4th class thermal drivers compression-suctions described in claim 8 In receipts formula heat pump, increase the 4th generator, the 3rd absorber and the 4th solution heat exchanger, absorber (1) is had weak solution pipe Road is connected with the second absorber (23) through solution pump (10) and solution heat exchanger (12) and is adjusted to absorber (1) and has weak solution pipe Road the 4th solution heat exchanger (30) is connected with the 3rd absorber (31), and the 3rd absorber (31) has weak solution pipeline again through solution Pump (10) is connected with the second absorber (23) with solution heat exchanger (12), and the second generator (3) is had concentrated solution pipeline through Two solution pumps (11) are connected with absorber (1) with the second solution heat exchanger (13) and are adjusted to the second generator (3) and have concentrated solution Pipeline is connected with the 4th generator (28) through the second solution heat exchanger (13), and the 4th generator (28) has concentrated solution pipeline warp again Second solution pump (11) is connected with absorber (1) with the 4th solution heat exchanger (30), and condenser (4) is had cryogen liquid pipeline warp Second generator (3) connect with evaporimeter (6) with choke valve (7) be adjusted to condenser (4) have cryogen liquid pipeline through second generation Device (3), the 4th generator (28) are connected with evaporimeter (6) with choke valve (7), and the 4th generator (28) also has refrigerant steam channel Connect with the 3rd absorber (31), the 3rd absorber (31) also has coolant guiding channel or low-temperature heat medium passage to connect with outside Logical, form the 4th class thermal drivers compressing-absorbing type heat pump.
27. the 4th class thermal drivers compressing-absorbing type heat pumps, be described in claim 26 arbitrary 4th class thermal drivers compression- In absorption heat pump, cancel choke valve, the 4th generator (28) is had cryogen liquid pipeline through choke valve (7) with evaporimeter (6) even Logical be adjusted to the 4th generator (28) and have cryogen liquid pipeline to connect with evaporimeter (6), formation the 4th class thermal drivers compressing-absorbing type Heat pump.
28. the 4th class thermal drivers compressing-absorbing type heat pumps, be described in claim 1-7 arbitrary 4th class thermal drivers compression- In absorption heat pump, increase the 3rd generator, the second absorber, the 3rd solution pump and the 3rd solution heat exchanger, by generator (2) there is refrigerant steam channel to connect with condenser (4) to be adjusted to generator (2) and have refrigerant steam channel and the second absorber (23) Connection, the second absorber (23) also has weak solution pipeline through the 3rd solution pump (24) and the 3rd solution heat exchanger (25) and the 3rd Generator (22) connects, and the 3rd generator (22) also has concentrated solution pipeline through the 3rd solution heat exchanger (25) and the second absorber (23) connect, the 3rd generator (22) also has refrigerant steam channel to connect with condenser (4), and the 3rd generator (22) also has high temperature Hot media channel and ft connection, the second absorber (23) also has heated medium passage and ft connection, forms the 4th class heat Drive compression-absorption heat pump.
29. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the 4th class thermal drivers compression-suction arbitrary described in claim 28 In receipts formula heat pump, cancel choke valve, the second generator (3) is had cryogen liquid pipeline to connect tune through choke valve (7) with evaporimeter (6) Whole is that the second generator (3) has cryogen liquid pipeline to connect with evaporimeter (6), forms the 4th class thermal drivers compressing-absorbing type heat pump.
30. the 4th class thermal drivers compressing-absorbing type heat pumps, are the arbitrary 4th class thermal drivers pressures described in claim 1-29 In contracting-absorption heat pump, decompressor (15) there is is refrigerant steam channel to connect adjustment with evaporimeter (6) or the second condenser (5) There is refrigerant steam channel to connect with condenser (4) for decompressor (15), form the 4th class thermal drivers compressing-absorbing type heat pump.
31. the 4th class thermal drivers compressing-absorbing type heat pumps, are the arbitrary 4th class thermal drivers pressures described in claim 1-30 In contracting-absorption heat pump, increase engine, engine connects compressor (16) and transmits power to compressor (16), is formed attached Plus the 4th class thermal drivers compressing-absorbing type heat pump that external impetus drive.
32. the 4th class thermal drivers compressing-absorbing type heat pumps, are the arbitrary 4th class thermal drivers pressures described in claim 1-30 In contracting-absorption heat pump, increase working machine, decompressor (15) connects working machine and transmits power to working machine, it is additional right to be formed Outer the 4th class thermal drivers compressing-absorbing type heat pump that living load is provided.
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Publication number Priority date Publication date Assignee Title
CN102095272A (en) * 2011-02-22 2011-06-15 李华玉 Two-end heat supply class II absorption type heat pump
CN104807239A (en) * 2014-03-27 2015-07-29 李华玉 Absorption heat pump of fourth class and absorption heat pump of fifth class
CN104807238A (en) * 2014-03-24 2015-07-29 李华玉 Absorption heat pump of fourth class and absorption heat pump of fifth class
CN104807241A (en) * 2014-03-30 2015-07-29 李华玉 Class four absorption type heat pump and class five absorption type heat pump
CN104833128A (en) * 2014-04-07 2015-08-12 李华玉 Fourth type absorption heat pump

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102095272A (en) * 2011-02-22 2011-06-15 李华玉 Two-end heat supply class II absorption type heat pump
CN104807238A (en) * 2014-03-24 2015-07-29 李华玉 Absorption heat pump of fourth class and absorption heat pump of fifth class
CN104807239A (en) * 2014-03-27 2015-07-29 李华玉 Absorption heat pump of fourth class and absorption heat pump of fifth class
CN104807241A (en) * 2014-03-30 2015-07-29 李华玉 Class four absorption type heat pump and class five absorption type heat pump
CN104833128A (en) * 2014-04-07 2015-08-12 李华玉 Fourth type absorption heat pump

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