CN105953467A - Fourth kind thermal-driving compression-absorption type heat pump - Google Patents

Fourth kind thermal-driving compression-absorption type heat pump Download PDF

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Publication number
CN105953467A
CN105953467A CN201610307783.7A CN201610307783A CN105953467A CN 105953467 A CN105953467 A CN 105953467A CN 201610307783 A CN201610307783 A CN 201610307783A CN 105953467 A CN105953467 A CN 105953467A
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generator
solution
heat exchanger
pump
connect
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CN105953467B (en
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李华玉
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B25/00—Machines, plants or systems, using a combination of modes of operation covered by two or more of the groups F25B1/00 - F25B23/00
    • F25B25/02—Compression-sorption machines, plants, or systems
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B41/00—Fluid-circulation arrangements
    • F25B41/30—Expansion means; Dispositions thereof
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2327/00—Compressor driving means

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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 kind thermal-driving compression-absorption type heat pump and belongs to the technical field of heat pumps and waste heat utilization. A solution loop is formed by an absorber, a generator, a second generator, a solution pump, a second solution pump, a solution heat exchanger and a second solution heat exchanger. The generator sequentially communicates with a compressor, a high-temperature heat exchanger, an expansion machine and a condenser through a refrigerant steam channel. The condenser communicates with an evaporator through a refrigerant liquid pipeline by means of the second generator and a throttling valve. The second generator communicates with a second condenser through the refrigerant steam channel. The second condenser communicates with the evaporator through a refrigerant liquid pump. The evaporator communicates with the absorber through the refrigerant steam channel. The generator and the high-temperature heat exchanger communicate with the outside through a high-temperature heat medium channel. The absorber and the condenser communicate with the outside through a heated medium channel. The second condenser communicates with the outside through a cooling medium channel. The evaporator communicates with the outside through a low-temperature heat medium channel. The expansion machine is connected with the compressor and used for transferring power. Thus, the fourth kind thermal-driving 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 for human lives common；In reality, people it is frequently necessary to High temperature heat is utilized to realize refrigeration, heat supply or be converted into power, it is also desirable to utilize power to carry out freezing or utilize power also Heat supply is carried out in conjunction with low temperature heat energy.During stating purpose in realization, many considerations will be faced or condition will limit, bag Include the type of the energy, grade and quantity, the type of user's request, grade and quantity, ambient temperature, the type of working media, The flow process of equipment, structure and manufacturing cost etc..
Heat energy (temperature difference) with absorption heat pump technology as representative utilizes technology, utilize high-temperature hot load drive realize heat supply or Refrigeration；Being affected by the character of working media (solution and refrigerant medium), high-temperature hot load often cannot reasonably be applied to In absorption heat pump flow process, cause its application and range of application by bigger restriction；Also absorption heat pump cannot have been given play to The advantage that technology refrigerant vapour latent heat is big.
Utilize the compression heat pump technology that the grade between mechanical energy and heat energy is poor, there is certain motility；But in many feelings Under condition, such compression heat pump is difficult to the Appropriate application to heat energy.Meanwhile, two kinds of heat pump techniques also have common deficiency Part cannot realize heat energy to machinery transformation of energy heating or freezing simultaneously.
In order to play the technical advantage of absorption heat pump, from the angle significantly promoting Low Temperature Thermal load temperature, for profit Carrying out heat supply or cooling with high-temperature hot load, and consider take into account power drive or externally provide power demand, the present invention proposes bag Containing components such as compressor, decompressor and high-temperature heat exchangers, by the temperature difference between high temperature heat source and heated medium and cryogen liquid with Between environment, the temperature difference carries out the most effectively utilizing, and has the 4th class thermal drivers compressing-absorbing type heat pump of comprehensive advantage.
Summary of the invention:
Present invention is primarily intended to provide series the 4th class thermal drivers compressing-absorbing type heat pump, concrete summary of the invention subitem illustrates As follows:
1. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, the second generator, compressor, Decompressor, condenser, the second condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution Heat exchanger, the second solution heat exchanger and high-temperature heat exchanger are formed；Absorber has weak solution pipeline through solution pump and molten Liquid heat exchanger connects with generator, generator also have concentrated solution pipeline through solution heat exchanger and the second solution heat exchanger with Second generator connection, the second generator also has concentrated solution pipeline through the second solution pump and the second solution heat exchanger and absorber Connection, generator also has refrigerant steam channel to connect with compressor, and compressor also has refrigerant steam channel through high-temperature heat exchanger Connecting with decompressor, decompressor also has refrigerant steam channel to connect with condenser, and condenser also has cryogen liquid pipeline and second After raw device connection, the second generator has cryogen liquid pipeline to connect with vaporizer through choke valve again, and the second generator also has cryogen to steam Vapour passage and the connection of the second condenser, the second condenser also has cryogen liquid pipeline to connect with vaporizer through cryogen liquid pump, vaporizer Also having refrigerant steam channel to connect with absorber, generator and high-temperature heat exchanger have high temperature thermal medium passage the most respectively with outside Connection, absorber and condenser have heated medium passage and ft connection, the second condenser to also have cooling medium to lead to the most respectively Road and ft connection, vaporizer also has low-temperature heat medium passage and ft connection, and decompressor connects compressor and transmits power, Form the 4th class thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor connects compressor, solution pump and the second solution pump also Transmission power.
2. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, the second generator, compressor, Decompressor, condenser, the second condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution Heat exchanger, the second solution heat exchanger, high-temperature heat exchanger and regenerator are formed；Absorber has weak solution pipeline through molten Liquid pump connects with generator with solution heat exchanger, and generator also has concentrated solution pipeline through solution heat exchanger and the second solution heat Exchanger and the connection of the second generator, the second generator also has concentrated solution pipeline through the second solution pump and the second solution heat exchanger Connecting with absorber, generator also has refrigerant steam channel to connect with compressor, and compressor also has refrigerant steam channel through backheat Device connects with decompressor with high-temperature heat exchanger, and decompressor also has refrigerant steam channel to connect with condenser through regenerator, condensation After device also has cryogen liquid pipeline and the connection of the second generator, the second generator has cryogen liquid pipeline through choke valve with vaporizer even again Logical, the second generator also has refrigerant steam channel to connect with the second condenser, and the second condenser also has cryogen liquid pipeline through cryogen Liquid pump connects with vaporizer, and vaporizer also has refrigerant steam channel to connect with absorber, and generator and high-temperature heat exchanger also divide High temperature thermal medium passage and ft connection, absorber and condenser is not had to have heated medium passage and ft connection the most respectively, Second condenser also has coolant guiding channel and ft connection, and vaporizer also has low-temperature heat medium passage and ft connection, expands Machine connects compressor and transmits power, forms the 4th class thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor connect compression Machine, solution pump and the second solution pump also transmit power.
3. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, the second generator, compressor, Decompressor, condenser, the second condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution Heat exchanger, the second solution heat exchanger, high-temperature heat exchanger, the second compressor and the second high-temperature heat exchanger 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 and the second generator connect, and the second generator also has concentrated solution pipeline molten through second Liquid pump and the second solution heat exchanger connect with absorber, and generator also has refrigerant steam channel to connect with compressor, compressor Also having refrigerant steam channel through the connection of high-temperature heat exchanger and the second compressor, the second compressor also has refrigerant steam channel through the Two high-temperature heat exchangers connect with decompressor, and decompressor also has refrigerant steam channel to connect with condenser, and condenser also has cryogen After liquid pipeline and the connection of the second generator, the second generator has cryogen liquid pipeline to connect with vaporizer through choke valve again, second Raw device also has refrigerant steam channel to connect with the second condenser, and the second condenser also has cryogen liquid pipeline through cryogen liquid pump and evaporation Device connects, and vaporizer also has refrigerant steam channel to connect with absorber, and generator, high-temperature heat exchanger and the second high-temperature hot are handed over Parallel operation has high temperature thermal medium passage and ft connection, absorber and condenser to have heated medium passage the most respectively with outer the most respectively Portion connects, and the second condenser also has coolant guiding channel and ft connection, and vaporizer also has low-temperature heat medium passage to connect with outside Logical, decompressor connects compressor and the second compressor and transmits power, forms the 4th class thermal drivers compressing-absorbing type heat pump；Its In, or decompressor connects compressor, the second compressor, solution pump and the second solution pump and transmits power.
4. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, the second generator, compressor, Decompressor, condenser, the second condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution Heat exchanger, the second solution heat exchanger, high-temperature heat exchanger, the second high-temperature heat exchanger and the second decompressor 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 and the second generator connect, and the second generator also has concentrated solution pipeline molten through second Liquid pump and the second solution heat exchanger connect with absorber, and generator also has refrigerant steam channel to connect with compressor (4), pressure Contracting machine also has refrigerant steam channel to connect through high-temperature heat exchanger and the second decompressor, and the second decompressor also has refrigerant steam channel Connecting with decompressor through the second high-temperature heat exchanger, decompressor also has refrigerant steam channel to connect with condenser, and decompressor also has Refrigerant steam channel connects with condenser, condenser also have cryogen liquid pipeline and the second generator connection after the second generator again Having cryogen liquid pipeline to connect with vaporizer through choke valve, the second generator also has refrigerant steam channel to connect with the second condenser, Second condenser also has cryogen liquid pipeline to connect with vaporizer through cryogen liquid pump, and vaporizer also has refrigerant steam channel and absorber Connecting, generator, high-temperature heat exchanger and the second high-temperature heat exchanger have high temperature thermal medium passage and ft connection the most respectively, Absorber and condenser have heated medium passage and ft connection, the second condenser to also have coolant guiding channel with outer the most respectively Portion connects, and vaporizer also has low-temperature heat medium passage and ft connection, decompressor and the second decompressor connect compressor and transmit Power, forms the 4th class thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor and the second decompressor connect compressor, molten Liquid pump and the second solution pump also transmit power.
5. the 4th class thermal drivers compressing-absorbing type heat pump, is at the described arbitrary 4th class thermal drivers compressing-absorbing type of 1-4 item In heat pump, cancel choke valve, the second generator has cryogen liquid pipeline connect with vaporizer through choke valve and is adjusted to the second generation Device has cryogen liquid pipeline to connect with vaporizer, forms the 4th class thermal drivers compressing-absorbing type heat pump.
6. the 4th class thermal drivers compressing-absorbing type heat pump, is at the described arbitrary 4th class thermal drivers compressing-absorbing type of 1-4 item In heat pump, increase the 3rd generator, second throttle, the 3rd solution pump, the 3rd solution heat exchanger and heater, absorb Device sets up weak solution pipeline through the 3rd solution pump and the 3rd solution heat exchanger and the connection of the 3rd generator, and the 3rd generator also has Generator, through the 3rd solution heat exchanger and the second solution heat exchanger and the connection of the second generator, is had cryogen by concentrated solution pipeline Steam channel connects with compressor and is adjusted to after generator has refrigerant steam channel to connect with the 3rd generator the 3rd generator again Having cryogen liquid pipeline to connect with vaporizer with second throttle through heater, the second generator, the 3rd generator also has cryogen to steam Vapour passage connects with compressor, and heater also has heated medium passage and ft connection, forms the 4th class thermal drivers compression-suction Receipts formula heat pump.
7. the 4th class thermal drivers compressing-absorbing type heat pump, is at the described arbitrary 4th class thermal drivers compressing-absorbing type of 1-4 item In heat pump, increase the 3rd generator, second throttle, the 3rd solution heat exchanger and heater, absorber is had weak solution Pipeline connects 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 connect with generator, generator have concentrated solution pipeline through solution heat exchanger and second Solution heat exchanger and the connection of the second generator are adjusted to generator has concentrated solution pipeline through the 3rd solution heat exchanger and the 3rd Raw device connection, the 3rd generator has concentrated solution pipeline again through solution heat exchanger and the second solution heat exchanger and the second generator Connection, has generator refrigerant steam channel to connect with compressor and is adjusted to generator and has refrigerant steam channel and the 3rd generator After connection, the 3rd generator has cryogen liquid pipeline to connect with vaporizer with second throttle through heater, the second generator again, 3rd generator also has refrigerant steam channel to connect with compressor, and heater also has heated medium passage and ft connection, shape Become the 4th class thermal drivers compressing-absorbing type heat pump.
8. the 4th class thermal drivers compressing-absorbing type heat pump, is at the described arbitrary 4th class thermal drivers compressing-absorbing type of 1-4 item In heat pump, increase the 3rd generator, second throttle, the 3rd solution pump, the 3rd solution heat exchanger and heater, will inhale Receive device to have 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 molten Liquid pump connects with solution heat exchanger and the 3rd generator, and the 3rd generator has concentrated solution pipeline again through the 3rd solution pump and the 3rd Solution heat exchanger connects with generator, generator has concentrated solution pipeline through solution heat exchanger and the second solution heat exchanger Connect with the second generator and be adjusted to generator and have concentrated solution pipeline through the 3rd solution heat exchanger, solution heat exchanger and second Solution heat exchanger and the connection of the second generator, have generator refrigerant steam channel to connect with compressor and be adjusted to generator and have Refrigerant steam channel connect with the 3rd generator after the 3rd generator have again cryogen liquid pipeline through heater, the second generator and Second throttle connects with vaporizer, and the 3rd generator also has refrigerant steam channel to connect with compressor, and heater is also added Hot media channel and ft connection, form the 4th class thermal drivers compressing-absorbing type heat pump.
9. the 4th class thermal drivers compressing-absorbing type heat pump, is at the described arbitrary 4th class thermal drivers compressing-absorbing type of 6-8 item In heat pump, the 3rd generator sets up high temperature thermal medium pipeline and ft connection, forms the 4th class thermal drivers compressing-absorbing type heat pump.
10. the 4th class thermal drivers compressing-absorbing type heat pump, is in the described arbitrary 4th class thermal drivers compression-absorption of 6-9 item In formula heat pump, cancel choke valve and second throttle, have cryogen liquid pipeline to connect with vaporizer through choke valve in the second generator Being adjusted to the second generator has cryogen liquid pipeline to connect with vaporizer, and the second generator is had cryogen liquid pipeline through second throttle Connect with vaporizer and be adjusted to the second generator and have cryogen liquid pipeline to connect with vaporizer, form the 4th class thermal drivers compression-absorb Formula heat pump.
11. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the described arbitrary 4th class thermal drivers compression-absorption of 1-4 item In formula heat pump, increase the 3rd generator, the 3rd solution heat exchanger and the second absorber, absorber is had weak solution pipeline warp Solution pump and solution heat exchanger connect with generator and are adjusted to absorber and have weak solution pipeline through the 3rd solution heat exchanger and Two absorbers connections, the second absorber has weak solution pipeline to connect with generator with solution heat exchanger through solution pump again, by the Two generators have concentrated solution pipeline to connect with absorber through the second solution pump and the second solution heat exchanger to be adjusted to the second generator Having concentrated solution pipeline to connect through the second solution heat exchanger and the 3rd generator, the 3rd generator has concentrated solution pipeline again through second Solution pump and the 3rd solution heat exchanger connect with absorber, and the second generator is had cryogen liquid pipeline through choke valve and vaporizer Connection is adjusted to the second generator has cryogen liquid pipeline to connect with vaporizer with choke valve through the 3rd generator, and the 3rd generator is also Having refrigerant steam channel to connect with the second absorber, the second absorber also has coolant guiding channel and ft connection, forms the 4th Class thermal drivers compressing-absorbing type heat pump.
12. the 4th class thermal drivers compressing-absorbing type heat pumps, are the 11st described arbitrary 4th class thermal drivers compression-absorption In formula heat pump, cancel choke valve, the 3rd generator has cryogen liquid pipeline connect with vaporizer through choke valve and is adjusted to the 3rd Raw device has cryogen liquid pipeline to connect with vaporizer, forms the 4th class thermal drivers compressing-absorbing type heat pump.
13. the 4th class thermal drivers compressing-absorbing type heat pumps, are the 11st described arbitrary 4th class thermal drivers compression-absorption In formula heat pump, increase the 4th generator, second throttle, the 3rd solution pump, the 4th solution heat exchanger and heater, the Two absorbers set up weak solution pipeline through the 3rd solution pump and the 4th solution heat exchanger and the connection of the 4th generator, and the 4th occurs Device also has concentrated solution pipeline through the 4th solution heat exchanger and the second solution heat exchanger and the connection of the second generator, by generator There is refrigerant steam channel to connect with compressor and be adjusted to after generator has refrigerant steam channel to connect with the 4th generator the 4th Raw device has cryogen liquid pipeline to connect with vaporizer with second throttle through heater, the second generator, the 3rd generator again, the Four generators also have refrigerant steam channel to connect with compressor, and heater also has heated medium passage and ft connection, are formed 4th class thermal drivers compressing-absorbing type heat pump.
14. the 4th class thermal drivers compressing-absorbing type heat pumps, are at the 11st described arbitrary 4th class thermal drivers compressing-absorbing type In heat pump, increase the 4th generator, second throttle, the 4th solution heat exchanger and heater, the second absorber is had dilute Solution line connects with generator through solution pump and solution heat exchanger and is adjusted to the second absorber and has weak solution pipeline through solution Pump, solution heat exchanger and the 4th solution heat exchanger connect with generator, and generator has concentrated solution pipeline hand over through solution heat Parallel operation and the second solution heat exchanger and the connection of the second generator are adjusted to generator and have concentrated solution pipeline through the 4th solution heat exchange Device and the connection of the 4th generator, the 4th generator have again concentrated solution pipeline through solution heat exchanger and the second solution heat exchanger with Second generator connection, generator is had refrigerant steam channel connect with compressor be adjusted to generator have refrigerant steam channel and After 4th generator connection, the 4th generator has cryogen liquid pipeline again through heater, the second generator, the 3rd generator and the Two choke valves connect with vaporizer, and the 4th generator also has refrigerant steam channel to connect with compressor, and heater also has heated Medium channel 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 at the 11st described arbitrary 4th class thermal drivers compressing-absorbing type In heat pump, increase the 4th generator, second throttle, the 3rd solution pump, the 4th solution heat exchanger and heater, by the Two absorbers have 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 connects with solution heat exchanger and the 4th generator through solution pump, and the 4th generator has concentrated solution pipeline again through the 3rd solution Pump and the 4th solution heat exchanger connect with generator, generator have concentrated solution pipeline through solution heat exchanger and the second solution Heat exchanger and the connection of the second generator are adjusted to generator and have concentrated solution pipeline through the 4th solution heat exchanger, solution heat exchange Device and the second solution heat exchanger and the second generator connect, and generator has refrigerant steam channel connect with compressor and is adjusted to Generator have refrigerant steam channel to connect with the 4th generator after the 4th generator have again cryogen liquid pipeline through heater, second Generator, the 3rd generator connect with vaporizer with second throttle, and the 4th generator also has refrigerant steam channel and compressor Connection, heater also has heated medium passage and ft connection, forms the 4th class thermal drivers compressing-absorbing type heat pump.
16. the 4th class thermal drivers compressing-absorbing type heat pumps, be described in 13-15 item arbitrary 4th class thermal drivers compression- In absorption heat pump, the 4th generator sets up high temperature thermal medium pipeline and ft connection, forms the 4th class thermal drivers compression-absorption Formula heat pump.
17. the 4th class thermal drivers compressing-absorbing type heat pumps, be described in 13-16 item arbitrary 4th class thermal drivers compression- In absorption heat pump, cancel choke valve and second throttle, the 3rd generator is had cryogen liquid pipeline through choke valve and vaporizer Connection is adjusted to the 3rd generator has cryogen liquid pipeline to connect with vaporizer, and the 3rd generator is had cryogen liquid pipeline through second section Stream valve connect with vaporizer and is adjusted to the 3rd generator and has cryogen liquid pipeline to connect with vaporizer, and formation the 4th class thermal drivers compresses- Absorption heat pump.
18. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the described arbitrary 4th class thermal drivers compression-absorption of 1-4 item In formula heat pump, increase the 3rd generator, the 3rd solution pump, the 3rd solution heat exchanger and the second absorber, absorber is had Weak solution pipeline through solution pump and solution heat exchanger connect with generator be adjusted to absorber have weak solution pipeline through solution pump and Solution heat exchanger and the connection of the second absorber, the second absorber has weak solution pipeline again through the 3rd solution pump and the 3rd solution heat Exchanger connects with generator, generator has concentrated solution pipeline through solution heat exchanger and the second solution heat exchanger and second Generator connection is adjusted to generator has concentrated solution pipeline to connect through the 3rd solution heat exchanger and the 3rd generator, and the 3rd occurs Device has concentrated solution pipeline again through solution heat exchanger and the second solution heat exchanger and the connection of the second generator, and the 3rd generator is also Having refrigerant steam channel to connect with the second absorber, the 3rd generator also has high temperature thermal medium passage and ft connection, and second inhales Receive device and also have heated medium passage and ft connection, form the 4th class thermal drivers compressing-absorbing type heat pump.
19. the 4th class thermal drivers compressing-absorbing type heat pumps, are the 18th the 4th described class thermal drivers compressing-absorbing type heat In pump, cancel choke valve, the second generator has cryogen liquid pipeline connect with vaporizer through choke valve and is adjusted to the second generator There is cryogen liquid pipeline to connect with vaporizer, form the 4th class thermal drivers compressing-absorbing type heat pump.
20. the 4th class thermal drivers compressing-absorbing type heat pumps, are the 18th the 4th described class thermal drivers compressing-absorbing type heat In pump, increasing the 4th generator, second throttle, the 4th solution pump, the 4th solution heat exchanger and heater, second inhales Receiving device to set up weak solution pipeline and connect with the 4th generator through the 4th solution pump and the 4th solution heat exchanger, the 4th generator is also There is concentrated solution pipeline to connect through the 4th solution heat exchanger and the 3rd generator, generator is had refrigerant steam channel and compressor Connection is adjusted to the 4th generator after generator has refrigerant steam channel to connect with the 4th generator has cryogen liquid pipeline again through supplying Hot device, the second generator connect with vaporizer with second throttle, and the 4th generator also has refrigerant steam channel with compressor even Logical, heater also has heated medium passage and ft connection, forms the 4th class thermal drivers compressing-absorbing type heat pump.
21. the 4th class thermal drivers compressing-absorbing type heat pumps, are the 18th the 4th described class thermal drivers compressing-absorbing type heat In pump, increase the 4th generator, second throttle, the 4th solution heat exchanger and heater, the second absorber is had dilute molten Liquid pipeline connects 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 warp 3rd solution pump, the 3rd solution heat exchanger and the 4th solution heat exchanger connect with generator, and generator has concentrated solution pipe Lu Jing tri-solution heat exchanger and the connection of the 3rd generator are adjusted to generator and have concentrated solution pipeline through the 4th solution heat exchanger Connecting with the 4th generator, the 4th generator has concentrated solution pipeline to connect through the 3rd solution heat exchanger and the 3rd generator again, Generator has refrigerant steam channel connect with compressor be adjusted to generator and have refrigerant steam channel to connect it with the 4th generator Rear 4th generator has cryogen liquid pipeline to connect with vaporizer with second throttle through heater, the second generator again, the 4th Raw device also has refrigerant steam channel to connect with compressor, and heater also has heated medium passage and ft connection, forms the 4th Class thermal drivers compressing-absorbing type heat pump.
22. the 4th class thermal drivers compressing-absorbing type heat pumps, are the 18th the 4th described class thermal drivers compressing-absorbing type heat In pump, increase the 4th generator, second throttle, the 4th solution pump, the 4th solution heat exchanger and heater, by second Absorber has weak solution pipeline to connect with generator through the 3rd solution pump and the 3rd solution heat exchanger to be adjusted to the second absorber and have Weak solution pipeline is through the 3rd solution pump and the 3rd solution heat exchanger and the connection of the 4th generator, and the 4th generator has concentrated solution again Pipeline connects with generator through the 4th solution pump and the 4th solution heat exchanger, generator has concentrated solution pipeline through the 3rd solution Heat exchanger and the connection of the 3rd generator are adjusted to generator has concentrated solution pipeline through the 4th solution heat exchanger and the 3rd solution heat Exchanger and the connection of the 3rd generator, have generator refrigerant steam channel to connect with compressor and be adjusted to generator and have cryogen to steam After vapour passage and the connection of the 4th generator, the 4th generator has cryogen liquid pipeline again through heater, the second generator and second section Stream valve connects with vaporizer, and the 4th generator also has refrigerant steam channel to connect with compressor, and heater also has heated medium Passage and ft connection, form the 4th class thermal drivers compressing-absorbing type heat pump.
23. the 4th class thermal drivers compressing-absorbing type heat pumps, be described in 20-22 item arbitrary 4th class thermal drivers compression- In absorption heat pump, the 4th generator sets up high temperature thermal medium pipeline and ft connection, forms the 4th class thermal drivers compression-absorption Formula heat pump.
24. the 4th class thermal drivers compressing-absorbing type heat pumps, be described in 20-23 item arbitrary 4th class thermal drivers compression- In absorption heat pump, cancel choke valve and second throttle, the second generator is had cryogen liquid pipeline through choke valve and vaporizer Connection is adjusted to the second generator has cryogen liquid pipeline to connect with vaporizer, and the second generator is had cryogen liquid pipeline through second section Stream valve connect with vaporizer and is adjusted to the second generator and has cryogen liquid pipeline to connect with vaporizer, and formation the 4th class thermal drivers compresses- Absorption heat pump.
25. the 4th class thermal drivers compressing-absorbing type heat pumps, are at the 18th described arbitrary 4th class thermal drivers compressing-absorbing type In heat pump, increase the 4th generator, the 4th solution heat exchanger and the 3rd absorber, absorber is had weak solution pipeline through molten Liquid pump connect with solution heat exchanger and the second absorber be adjusted to absorber have weak solution pipeline through the 4th solution heat exchanger with 3rd absorber connection, the 3rd absorber has weak solution pipeline to connect with solution heat exchanger and the second absorber through solution pump again, Second generator has concentrated solution pipeline connect with absorber through the second solution pump and the second solution heat exchanger and is adjusted to second Raw device has concentrated solution pipeline to connect through the second solution heat exchanger and the 4th generator, and the 4th generator has concentrated solution pipeline warp again Second solution pump and the 4th solution heat exchanger connect with absorber, and the 4th generator also has refrigerant steam channel and the 3rd absorption Device connects, and the second generator has cryogen liquid pipeline connect with vaporizer through choke valve and is adjusted to the second generator and has cryogen liquid pipe Lu Jing tetra-generator connects with vaporizer with choke valve, and the 3rd absorber also has coolant guiding channel and ft connection, is formed 4th class thermal drivers compressing-absorbing type heat pump.
26. the 4th class thermal drivers compressing-absorbing type heat pumps, are at the 25th described arbitrary 4th class thermal drivers compressing-absorbing type In heat pump, cancel choke valve, the 4th generator has cryogen liquid pipeline connect with vaporizer through choke valve and is adjusted to the 4th generation Device has cryogen liquid pipeline to connect with vaporizer, forms the 4th class thermal drivers compressing-absorbing type heat pump.
27. the 4th class thermal drivers compressing-absorbing type heat pumps, mainly by absorber, generator, the second generator, compressor, Decompressor, condenser, the second condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution Heat exchanger, the second solution heat exchanger, high-temperature heat exchanger and regenerator are formed；Absorber has weak solution pipeline through molten Liquid pump connects with generator with solution heat exchanger, and generator also has concentrated solution pipeline through solution heat exchanger and the second solution heat Exchanger and the connection of the second generator, the second generator also has concentrated solution pipeline through the second solution pump and the second solution heat exchanger Connecting with absorber, generator also has refrigerant steam channel to connect with compressor through regenerator, and compressor also has refrigerant vapour to lead to Road connects with decompressor through high-temperature heat exchanger, and decompressor also has refrigerant steam channel to connect with condenser through regenerator, condensation After device also has cryogen liquid pipeline and the connection of the second generator, the second generator has cryogen liquid pipeline through choke valve with vaporizer even again Logical, the second generator also has refrigerant steam channel to connect with the second condenser, and the second condenser also has cryogen liquid pipeline through cryogen Liquid pump connects with vaporizer, and vaporizer also has refrigerant steam channel to connect with absorber, and generator and high-temperature heat exchanger also divide High temperature thermal medium passage and ft connection, absorber and condenser is not had to have heated medium passage and ft connection the most respectively, Second condenser also has coolant guiding channel and ft connection, and vaporizer also has low-temperature heat medium passage and ft connection, expands Machine connects compressor and transmits power, forms the 4th class thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor connect compression Machine, solution pump and the second solution pump also transmit power.
28. the 4th class thermal drivers compressing-absorbing type heat pumps, are at the 27th described 4th class thermal drivers compressing-absorbing type heat pump In, cancel choke valve, the second generator has cryogen liquid pipeline connect with vaporizer through choke valve and is adjusted to the second generator and has Cryogen liquid pipeline connects with vaporizer, forms the 4th class thermal drivers compressing-absorbing type heat pump.
29. the 4th class thermal drivers compressing-absorbing type heat pumps, be described in 1-28 item arbitrary first kind thermal drivers compress- In absorption heat pump, increasing working machine, decompressor connects working machine and provides power to working machine, and being formed to add externally provides 4th class thermal drivers compressing-absorbing type heat pump of living load.
30. the 4th class thermal drivers compressing-absorbing type heat pumps, be described in 1-28 item arbitrary first kind thermal drivers compress- In absorption heat pump, increasing engine, engine connects compressor and provides power to compressor, forms additional external power The 4th class thermal drivers compressing-absorbing type heat pump driven.
Accompanying drawing illustrates:
Fig. 1 is based on the 4th the 1st kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 2 is based on the 4th the 2nd kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 3 is based on the 4th the 3rd kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 4 is based on the 4th the 4th kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 5 is based on the 4th the 5th kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 6 is based on the 4th the 6th kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 7 is based on the 4th the 7th kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 8 is based on the 4th the 8th kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 9 is based on the 4th the 9th kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 10 is based on the 4th the 10th kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 11 is based on the 4th the 11st kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 12 is based on the 4th the 12nd kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 13 is based on the 4th the 13rd kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 14 is based on the 4th the 14th kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 15 is based on the 4th the 15th kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 16 is based on the 4th the 16th kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 17 is based on the 4th the 17th kind of principled thermal system figure of class thermal drivers compressing-absorbing type heat pump provided by the present invention.
In figure, 1-absorber, 2-generator, 3-the second generator, 4-compressor, 5-decompressor, 6-condenser, 7-the second condenser, 8-vaporizer, 9-choke valve, 10-cryogen liquid pump, 11-solution pump, 12-the second solution pump, 13-solution heat exchanger, 14-the second solution heat exchanger, 15-high-temperature heat exchanger, 16-regenerator, 17-second Compressor, 18-the second high-temperature heat exchanger, 19-the second decompressor, 20-the 3rd generator, 21-second throttle, 22-the 3rd solution pump, 23-the 3rd solution heat exchanger, 24-heater, 25-the second absorber, 26-the 4th occurs Device, 27-the 4th solution heat exchanger, 28-the 4th solution pump, 29-the 3rd absorber.
For ease of understanding, provide following description:
As a example by the 4th class thermal drivers compressing-absorbing type heat pump shown in accompanying drawing 1, the choke valve 9 arranged in cryogen liquid pipeline, can Substitute with gravitational pressure drop；When coolant temperature is relatively low, the cryogen liquid temp flowing through the second generator 3 is cooled to vaporizer 8 During internal evaporating temperature, it is not provided with choke valve 9, and power pressure reduction is used in the second generator 3 inner heat exchanger pipeline.
Detailed description of the invention:
First be noted that in the statement of structure and flow process, inessential in the case of do not repeat；To obviously Flow process is not stated.The present invention is described in detail below in conjunction with the accompanying drawings with example.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 1 is achieved in that
(1) in structure, it mainly by absorber, generator, the second generator, compressor, decompressor, condenser, second Condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat Exchanger and high-temperature heat exchanger are formed；Absorber 1 have weak solution pipeline through solution pump 11 and solution heat exchanger 13 with Generator 2 connects, and generator 2 also has concentrated solution pipeline through solution heat exchanger 13 and the second solution heat exchanger 14 and the Two generators 3 connect, and the second generator 3 also has concentrated solution pipeline through the second solution pump 12 and the second solution heat exchanger 14 Connecting with absorber 1, generator 2 also refrigerant steam channel connects with compressor 4, and compressor 4 also has refrigerant vapour to lead to Road connects with decompressor 5 through high-temperature heat exchanger 15, and decompressor 5 also refrigerant steam channel connects with condenser 6, condensation After device 6 also cryogen liquid pipeline and the connection of the second generator 3 second generator 3 have again cryogen liquid pipeline through choke valve 9 with Vaporizer 8 connects, and the second generator 3 also refrigerant steam channel connects with the second condenser 7, and the second condenser 7 also has Cryogen liquid pipeline connects with vaporizer 8 through cryogen liquid pump 10, and vaporizer 8 also refrigerant steam channel connects with absorber 1, Generator 2 and high-temperature heat exchanger 15 have high temperature thermal medium passage and ft connection, absorber 1 and condenser 6 also the most respectively Heated medium passage and ft connection, the second condenser 7 is had to also have coolant guiding channel and ft connection, vaporizer 8 respectively Also having low-temperature heat medium passage and ft connection, decompressor 5 connects compressor 4 and transmits power.
(2) in flow process, the weak solution of absorber 1 enters generator 2 through solution pump 11 and solution heat exchanger 13, and high-temperature hot is situated between Mass flow enters its interior solution release refrigerant vapour through generator 2, heating and provides to compressor 4, the concentrated solution of generator 2 Enter the second generator 3 through solution heat exchanger 13 and the second solution heat exchanger 14, absorbing heat discharges refrigerant vapour and to second Condenser 7 provides, and the concentrated solution of the second generator 3 enters through the second solution pump 12 and the second solution heat exchanger 14 and absorbs Device 1, absorption refrigerant vapour heat release are in heated medium；Refrigerant vapour flows through compressor 4 boosting and heats up, and flows through high-temperature hot and hands over Parallel operation 15 also absorbs heat, and enters decompressor 5 blood pressure lowering work done afterwards；The refrigerant vapour of decompressor 5 discharge enters condenser 6 and puts Heat becomes cryogen liquid in heated medium, and the cryogen liquid stream of condenser 6 saves through choke valve 9 after the second generator 3 heat release again Stream enters vaporizer 8, and the refrigerant vapour heat release of the second condenser 7 becomes cryogen liquid, the cryogen of the second condenser 7 in cooling medium Liquid enters vaporizer 8 through cryogen liquid pump 10 pressurization；Low-temperature heat medium flows through vaporizer 8, heating enters its interior cryogen liquid and becomes Refrigerant vapour, the refrigerant vapour that vaporizer 8 produces is supplied to absorber 1；The merit of decompressor 5 output is supplied to compressor 4 and makees Power, forms the 4th class thermal drivers compressing-absorbing type heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 2 is achieved in that
(1) in structure, it mainly by absorber, generator, the second generator, compressor, decompressor, condenser, second Condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat Exchanger, high-temperature heat exchanger and regenerator are formed；Absorber 1 has weak solution pipeline through solution pump 11 and solution heat exchange Device 13 connects with generator 2, and generator 2 also has concentrated solution pipeline through solution heat exchanger 13 and the second solution heat exchanger 14 connect with the second generator 3, and the second generator 3 also has concentrated solution pipeline through the second solution pump 12 and the second solution heat exchange Device 14 connects with absorber 1, and generator 2 also refrigerant steam channel connects with compressor 4, and compressor 4 also has cryogen to steam Vapour passage connects with decompressor 5 with high-temperature heat exchanger 15 through regenerator 16, and decompressor 5 also has refrigerant steam channel through returning Hot device 16 connects with condenser 6, and condenser 6 also has the second generator 3 after cryogen liquid pipeline and the connection of the second generator 3 Having cryogen liquid pipeline to connect with vaporizer 8 through choke valve 9 again, the second generator 3 also has refrigerant steam channel and the second condensation Device 7 connects, and the second condenser 7 also cryogen liquid pipeline connects with vaporizer 8 through cryogen liquid pump 10, and vaporizer 8 is the coldest Agent steam channel connects with absorber 1, and generator 2 and high-temperature heat exchanger 15 have high temperature thermal medium passage the most respectively with outside Connection, absorber 1 and condenser 6 have heated medium passage and ft connection, the second condenser 7 to also have cooling the most respectively Medium channel and ft connection, vaporizer 8 also has low-temperature heat medium passage and ft connection, and decompressor 5 connects compressor 4 And transmit power.
(2) in flow process, the weak solution of absorber 1 enters generator 2 through solution pump 11 and solution heat exchanger 13, and high-temperature hot is situated between Mass flow enters its interior solution release refrigerant vapour through generator 2, heating and provides to compressor 4, the concentrated solution of generator 2 Enter the second generator 3 through solution heat exchanger 13 and the second solution heat exchanger 14, absorbing heat discharges refrigerant vapour and to second Condenser 7 provides, and the concentrated solution of the second generator 3 enters through the second solution pump 12 and the second solution heat exchanger 14 and absorbs Device 1, absorption refrigerant vapour heat release are in heated medium；Refrigerant vapour flows through compressor 4 boosting and heats up, and flows through backheat successively Device 16 and high-temperature heat exchanger 15 also progressively absorb heat, and enter decompressor 5 blood pressure lowering work done afterwards；The cryogen of decompressor 5 discharge Steam flows through regenerator 16 heat release, enters condenser 6 afterwards and heat release becomes cryogen liquid in heated medium；Condenser 6 Cryogen liquid stream enters vaporizer 8 through choke valve 9 throttling after the second generator 3 heat release again, and the cryogen of the second condenser 7 steams Vapour heat release becomes cryogen liquid in cooling medium, and the cryogen liquid of the second condenser 7 enters vaporizer 8 through cryogen liquid pump 10 pressurization；Low Warm flows through vaporizer 8, heating enters its interior cryogen liquid and becomes refrigerant vapour, and the refrigerant vapour that vaporizer 8 produces provides To absorber 1；The merit of decompressor 5 output is supplied to compressor 4 and is used as power, and forms the 4th class thermal drivers compressing-absorbing type heat Pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 3 is achieved in that
(1) in structure, it mainly by absorber, generator, the second generator, compressor, decompressor, condenser, second Condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat Exchanger, high-temperature heat exchanger, the second compressor and the second high-temperature heat exchanger are formed；Absorber 1 has weak solution pipeline Connecting with generator 2 with solution heat exchanger 13 through solution pump 11, generator 2 also has concentrated solution pipeline through solution heat exchange Device 13 connects with the second generator 3 with the second solution heat exchanger 14, and the second generator 3 also has concentrated solution pipeline through second Solution pump 12 connects with absorber 1 with the second solution heat exchanger 14, and generator 2 also has refrigerant steam channel and compressor 4 Connection, compressor 4 also refrigerant steam channel connects with the second compressor 17 through high-temperature heat exchanger 15, the second compressor 17 also refrigerant steam channel connect with decompressor 5 through the second high-temperature heat exchanger 18, decompressor 5 also has refrigerant steam channel Connecting with condenser 6, after condenser 6 also cryogen liquid pipeline and the connection of the second generator 3, the second generator 3 has cold again Agent liquid pipeline connects with vaporizer 8 through choke valve 9, and the second generator 3 also has refrigerant steam channel with the second condenser 7 even Logical, the second condenser 7 also cryogen liquid pipeline connects with vaporizer 8 through cryogen liquid pump 10, and vaporizer 8 also has refrigerant vapour Passage connects with absorber 1, and generator 2, high-temperature heat exchanger 15 and the second high-temperature heat supply device 24 have high-temperature hot to be situated between the most respectively Matter passage and ft connection, absorber 1 and condenser 6 have heated medium passage and ft connection, the second condensation the most respectively Device 7 also has coolant guiding channel and ft connection, vaporizer 8 to also have low-temperature heat medium passage and ft connection, decompressor 5 Connect compressor 4 and the second compressor 17 and transmit power.
(2) in flow process, the weak solution of absorber 1 enters generator 2 through solution pump 11 and solution heat exchanger 13, and high-temperature hot is situated between Mass flow enters its interior solution release refrigerant vapour through generator 2, heating and provides to compressor 4, the concentrated solution of generator 2 Enter the second generator 3 through solution heat exchanger 13 and the second solution heat exchanger 14, absorbing heat discharges refrigerant vapour and to second Condenser 7 provides, and the concentrated solution of the second generator 3 enters through the second solution pump 12 and the second solution heat exchanger 14 and absorbs Device 1, absorption refrigerant vapour heat release are in heated medium；Refrigerant vapour flows through compressor 4 boosting and heats up, and flows through high-temperature hot and hands over Parallel operation 15 also absorbs heat, and enters the second compressor 17 boosting afterwards and heats up；The refrigerant vapour of the second compressor 17 discharge flows through the Two high-temperature heat exchangers 18 also absorb heat, and enter decompressor 5 blood pressure lowering work done afterwards；The refrigerant vapour of decompressor 5 discharge enters cold Condenser 6 heat release become cryogen liquid in heated medium, the cryogen liquid stream of condenser 6 warp again after the second generator 3 heat release Choke valve 9 throttling enters vaporizer 8, and the refrigerant vapour heat release of the second condenser 7 becomes cryogen liquid, the second condensation in cooling medium The cryogen liquid of device 7 enters vaporizer 8 through cryogen liquid pump 10 pressurization；Low-temperature heat medium flows through vaporizer 8, heating enters in it Cryogen liquid become refrigerant vapour, the refrigerant vapour that vaporizer 8 produces is supplied to absorber 1；The merit of decompressor 5 output is supplied to Compressor 4 and the second compressor 17 are used as power, and form the 4th class thermal drivers compressing-absorbing type heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 4 is achieved in that
(1) in structure, it mainly by absorber, generator, the second generator, compressor, decompressor, condenser, second Condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat Exchanger, high-temperature heat exchanger, the second high-temperature heat exchanger and the second decompressor are formed；Absorber 1 has weak solution pipeline Connecting with generator 2 with solution heat exchanger 13 through solution pump 11, generator 2 also has concentrated solution pipeline through solution heat exchange Device 13 connects with the second generator 3 with the second solution heat exchanger 14, and the second generator 3 also has concentrated solution pipeline through second Solution pump 12 connects with absorber 1 with the second solution heat exchanger 14, and generator 2 also has refrigerant steam channel and compressor 4 Connection, compressor 4 also refrigerant steam channel connects with the second decompressor 19 through high-temperature heat exchanger 15, the second decompressor 19 also refrigerant steam channel connect with decompressor 5 through the second high-temperature heat exchanger 18, decompressor 5 also has refrigerant steam channel Connecting with condenser 6, after condenser 6 also cryogen liquid pipeline and the connection of the second generator 3, the second generator 3 has cold again Agent liquid pipeline connects with vaporizer 8 through choke valve 9, and the second generator 3 also has refrigerant steam channel with the second condenser 7 even Logical, the second condenser 7 also cryogen liquid pipeline connects with vaporizer 8 through cryogen liquid pump 10, and vaporizer 8 also has refrigerant vapour Passage connects with absorber 1, and generator 2, high-temperature heat exchanger 15 and the second high-temperature heat exchanger 18 have high-temperature hot the most respectively Medium channel and ft connection, absorber 1 and condenser 6 have heated medium passage and ft connection the most respectively, and second is cold Condenser 7 also has coolant guiding channel and ft connection, vaporizer 8 to also have low-temperature heat medium passage and ft connection, decompressor 5 Connect compressor 4 with the second decompressor 19 and transmit power.
(2) in flow process, the weak solution of absorber 1 enters generator 2 through solution pump 11 and solution heat exchanger 13, and high-temperature hot is situated between Mass flow enters its interior solution release refrigerant vapour through generator 2, heating and provides to compressor 4, the concentrated solution of generator 2 Enter the second generator 3 through solution heat exchanger 13 and the second solution heat exchanger 14, absorbing heat discharges refrigerant vapour and to second Condenser 7 provides, and the concentrated solution of the second generator 3 enters through the second solution pump 12 and the second solution heat exchanger 14 and absorbs Device 1, absorption refrigerant vapour heat release are in heated medium；Refrigerant vapour flows through compressor 4 boosting and heats up, and flows through high-temperature hot and hands over Parallel operation 15 also absorbs heat, and enters the second decompressor 19 blood pressure lowering work done afterwards；The refrigerant vapour of the second decompressor 19 discharge flows through the Two high-temperature heat exchangers 18 also absorb heat, and enter decompressor 5 blood pressure lowering work done afterwards；The refrigerant vapour of decompressor 5 discharge enters cold Condenser 6 heat release become cryogen liquid in heated medium, the cryogen liquid stream of condenser 6 warp again after the second generator 3 heat release Choke valve 9 throttling enters vaporizer 8, and the refrigerant vapour heat release of the second condenser 7 becomes cryogen liquid, the second condensation in cooling medium The cryogen liquid of device 7 enters vaporizer 8 through cryogen liquid pump 10 pressurization；Low-temperature heat medium flows through vaporizer 8, heating enters in it Cryogen liquid become refrigerant vapour, the refrigerant vapour that vaporizer 8 produces is supplied to absorber 1；Decompressor 5 and the second decompressor The merit of 19 outputs is supplied to compressor 4 and is used as power, and forms the 4th class thermal drivers compressing-absorbing type heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 5 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 1, the 3rd generator, the second throttling are increased Valve, the 3rd solution pump, the 3rd solution heat exchanger and heater, absorber 1 sets up weak solution pipeline through the 3rd solution pump 22 Connecting with the 3rd generator 20 with the 3rd solution heat exchanger 23, the 3rd generator 20 also has concentrated solution pipeline through the 3rd solution Heat exchanger 23 connects with the second generator 3 with the second solution heat exchanger 14, generator 2 is had refrigerant steam channel with Compressor 4 connection is adjusted to after generator 2 has refrigerant steam channel to connect the 3rd generator 20 with the 3rd generator 20 again Cryogen liquid pipeline is had to connect with vaporizer 8 with second throttle 21 through heater the 24, second generator 3, the 3rd generator 20 also refrigerant steam channel connect with compressor 4, heater 24 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 20 and makees to drive thermal medium, absorber 1 Part weak solution enters the 3rd generator 20 through the 3rd solution pump 22 and the 3rd solution heat exchanger 23, and refrigerant vapour flows through Three generators 20, heating enter its interior solution release refrigerant vapour and also provide to compressor 4, the 3rd generator 20 dense molten Liquid enters the second generator 3 through the 3rd solution heat exchanger 23 and the second solution heat exchanger 14；Flow through the 3rd generator 20 Refrigerant vapour heat release become cryogen liquid after flow through heater 24 and the second generator 3 progressively heat release successively, after through second Choke valve 21 throttling enters vaporizer 8, forms the 4th class thermal drivers compressing-absorbing type heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 6 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 1, the 3rd generator, the second throttling are increased Valve, the 3rd solution heat exchanger and heater, have weak solution pipeline through solution pump 11 and solution heat exchanger 13 by absorber 1 Connect with generator 2 be adjusted to absorber 1 have weak solution pipeline through solution pump 11, solution heat exchanger 13 and the 3rd solution heat Exchanger 23 connects with generator 2, and generator 2 has concentrated solution pipeline hand over through solution heat exchanger 13 and the second solution heat Parallel operation 14 connects with the second generator 3 and is adjusted to generator 2 and has concentrated solution pipeline through the 3rd solution heat exchanger 23 and the 3rd Generator 20 connects, and the 3rd generator 20 has concentrated solution pipeline again through solution heat exchanger 13 and the second solution heat exchanger 14 Connect with the second generator 3, generator 2 has refrigerant steam channel connect with compressor 4 and is adjusted to generator 2 and has cryogen After steam channel and the connection of the 3rd generator 20, the 3rd generator 20 has cryogen liquid pipeline to occur through heater 24, second again Device 3 connects with vaporizer 8 with second throttle 21, and the 3rd generator 20 also refrigerant steam channel connects with compressor 4, Heater 24 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 20 and makees to drive thermal medium, absorber 1 Weak solution enters generator 2 through solution pump 11, solution heat exchanger 13 and the 3rd solution heat exchanger 23, generator 2 Concentrated solution enters the 3rd generator 20 through the 3rd solution heat exchanger 23, refrigerant vapour flow through the 3rd generator 20, heat into Entering its interior solution release refrigerant vapour and provide to compressor 4, the concentrated solution of the 3rd generator 20 is through solution heat exchanger 13 The second generator 3 is entered with the second solution heat exchanger 14；Flow through the refrigerant vapour heat release of the 3rd generator 20 become cryogen liquid it After pass through heater 24 and the second generator 3 progressively heat release, after through second throttle 21 throttling enter vaporizer 8, Form the 4th class thermal drivers compressing-absorbing type heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 7 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 1, the 3rd generator, the second throttling are increased Valve, the 3rd solution pump, the 3rd solution heat exchanger and heater, have weak solution pipeline through solution pump 11 and molten by absorber 1 Liquid heat exchanger 13 connects with generator 2 and is adjusted to absorber 1 and has weak solution pipeline through solution pump 11 and solution heat exchanger 13 connect with the 3rd generator 20, and the 3rd generator 20 has concentrated solution pipeline to hand over through the 3rd solution pump 22 and the 3rd solution heat again Parallel operation 23 connects with generator 2, generator 2 has concentrated solution pipeline through solution heat exchanger 13 and the second solution heat exchange Device 14 connect with the second generator 3 be adjusted to generator 2 have concentrated solution pipeline through the 3rd solution heat exchanger 23, solution heat hand over Parallel operation 13 connects with the second generator 3 with the second solution heat exchanger 14, and generator 2 is had refrigerant steam channel and compression Machine 4 connection is adjusted to the 3rd generator 20 after generator 2 has refrigerant steam channel to connect with the 3rd generator 20 to be had cold again Agent liquid pipeline connects with vaporizer 8 with second throttle 21 through heater the 24, second generator 3, and the 3rd generator 20 is also Having refrigerant steam channel to connect with compressor 4, heater 24 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 20 and makees to drive thermal medium, absorber 1 Weak solution enters the 3rd generator 20 through solution pump 11 and solution heat exchanger 13, refrigerant vapour flow through the 3rd generator 20, Heating enters its interior solution release refrigerant vapour and provides to compressor 4, and the concentrated solution of the 3rd generator 20 is through the 3rd solution Pump 22 and the 3rd solution heat exchanger 23 enter generator 2, the concentrated solution of generator 2 through the 3rd solution heat exchanger 23, Solution heat exchanger 13 and the second solution heat exchanger 14 enter the second generator 3；The cryogen flowing through the 3rd generator 20 steams Vapour heat release flows through heater 24 and the second generator 3 progressively heat release after becoming cryogen liquid, after save through second throttle 21 Stream enters vaporizer 8, forms the 4th class thermal drivers compressing-absorbing type heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 8 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 1, the 3rd generator, the 3rd solution are increased Heat exchanger and the second absorber, have weak solution pipeline through solution pump 11 and solution heat exchanger 13 and to occur by absorber 1 Device 2 connection is adjusted to absorber 1 has weak solution pipeline to connect with the second absorber 25 through the 3rd solution heat exchanger 23, the Two absorbers 25 have weak solution pipeline to connect with generator 2 with solution heat exchanger 13 through solution pump 11 again, occur second Device 3 has concentrated solution pipeline to connect with absorber 1 through the second solution pump 12 and the second solution heat exchanger 14 to be adjusted to second Raw device 3 has concentrated solution pipeline to connect with the 3rd generator 20 through the second solution heat exchanger 14, and the 3rd generator 20 has dense again Solution line connects with absorber 1 with the 3rd solution heat exchanger 23 through the second solution pump 12, has cold by the second generator 3 Agent liquid pipeline through choke valve 9 connect with vaporizer 8 be adjusted to the second generator 3 have cryogen liquid pipeline through the 3rd generator 20 and Choke valve 9 connects with vaporizer 8, and the 3rd generator 20 also refrigerant steam channel connects with the second absorber 25, and second Absorber 25 also has coolant guiding channel and ft connection.
(2), in flow process, the weak solution of absorber 1 enters the second absorber 25 through the 3rd solution heat exchanger 23, absorbs cryogen steaming Vapour heat release enter generator in cooling medium, the weak solution of the second absorber 25 through solution pump 11 and solution heat exchanger 13 2, the concentrated solution of generator 2 enters the second generator 3 through solution heat exchanger 13 and the second solution heat exchanger 14, and second Concentrated solution second solution heat exchanger 14 of generator 3 enters the 3rd generator 20, heat absorption release refrigerant vapour and inhales to second Receiving device 25 to provide, the concentrated solution of the 3rd generator 20 enters through the second solution pump 12 and the 3rd solution heat exchanger 23 and absorbs Device 1；The cryogen liquid of condenser 6 flow through successively the second generator 3 and the 3rd generator 20 and progressively after heat release through choke valve 9 throttlings enter vaporizer 8, form the 4th class thermal drivers compressing-absorbing type heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 9 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 8, the 4th generator, the second throttling are increased Valve, the 3rd solution pump, the 4th solution heat exchanger and heater, the second absorber 25 sets up weak solution pipeline through the 3rd solution Pump 22 connects with the 4th generator 26 with the 4th solution heat exchanger 27, and the 4th generator 26 also has concentrated solution pipeline through the Four solution heat exchangers 27 connect with the second generator 3 with the second solution heat exchanger 14, and generator 2 is had refrigerant vapour Passage connects with compressor 4 and is adjusted to the 4th generator after generator 2 has refrigerant steam channel to connect with the 4th generator 26 26 have cryogen liquid pipeline again through heater the 24, second generator the 3, the 3rd generator 20 and second throttle 21 and vaporizer 8 connections, the 4th generator 26 also refrigerant steam channel connects with compressor 4, and heater 24 also has heated medium passage With ft connection.
(2), in flow process, the refrigerant vapour that generator 2 produces is supplied to the 4th generator 26 and makees to drive thermal medium, the second absorber The part weak solution of 25 enters the 4th generator 26, refrigerant vapour stream through the 3rd solution pump 22 and the 4th solution heat exchanger 27 Enter its interior solution release refrigerant vapour through the 4th generator 26, heating and provide to compressor 4, the 4th generator 26 Concentrated solution enters the second generator 3 through the 4th solution heat exchanger 27 and the second solution heat exchanger 14；Flow through the 4th generator The refrigerant vapour heat release of 26 becomes cryogen liquid, cryogen liquid to flow through heater the 24, second generator 3 and the 3rd generator 20 successively And progressively enter vaporizer 8 through second throttle 21 throttling again after heat release, form the 4th class thermal drivers compressing-absorbing type heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Figure 10 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 8, the 4th generator, the second throttling are increased Valve, the 4th solution heat exchanger and heater, have weak solution pipeline to hand over through solution pump 11 and solution heat by the second absorber 25 Parallel operation 13 connects with generator 2 and is adjusted to the second absorber 25 and has weak solution pipeline through solution pump 11, solution heat exchanger 13 Connect with generator 2 with the 4th solution heat exchanger 27, generator 2 is had concentrated solution pipeline through solution heat exchanger 13 He Second solution heat exchanger 14 connects with the second generator 3 and is adjusted to generator 2 and has concentrated solution pipeline through the 4th solution heat exchange Device 27 connects with the 4th generator 26, and the 4th generator 26 has concentrated solution pipeline molten through solution heat exchanger 13 and second again Liquid heat exchanger 14 connects with the second generator 3, generator 2 is had refrigerant steam channel connect with compressor 4 be adjusted to send out After raw device 2 has refrigerant steam channel to connect with the 4th generator 26, the 4th generator 26 has cryogen liquid pipeline again through heater 24, the second generator the 3, the 3rd generator 20 connects with vaporizer 8 with second throttle 21, and the 4th generator 26 also has Refrigerant steam channel connects with compressor 4, and heater 24 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 26 and makees to drive thermal medium, the second absorber The weak solution of 25 enters generator 2, generator through solution pump 11, solution heat exchanger 13 and the 4th solution heat exchanger 27 The concentrated solution of 2 enters the 4th generator 26 through the 4th solution heat exchanger 27, and refrigerant vapour flows through the 4th generator 26, heating Entering its interior solution release refrigerant vapour and provide to compressor 4, the concentrated solution of the 4th generator 26 is through solution heat exchanger 13 and second solution heat exchanger 14 enter the second generator 3；The refrigerant vapour heat release flowing through the 4th generator 26 becomes cryogen Flow through heater the 24, second generator 3 and the 3rd generator 20 progressively heat release after liquid successively, after through second throttle 21 throttlings enter vaporizer 8, 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 achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 8, the 4th generator, the second throttling are increased Valve, the 3rd solution pump, the 4th solution heat exchanger and heater, have weak solution pipeline through solution pump 11 by the second absorber 25 Connect with generator 2 with solution heat exchanger 13 and be adjusted to the second absorber 25 and have weak solution pipeline through solution pump 11 and solution Heat exchanger 13 connects with the 4th generator 26, and the 4th generator 26 has concentrated solution pipeline again through the 3rd solution pump 22 and Four solution heat exchangers 27 connect with generator 2, generator 2 have concentrated solution pipeline through solution heat exchanger 13 and second Solution heat exchanger 14 connect with the second generator 3 be adjusted to generator 2 have concentrated solution pipeline through the 4th solution heat exchanger 27, Solution heat exchanger 13 connects with the second generator 3 with the second solution heat exchanger 14, has refrigerant vapour to lead in generator 2 Road connects with compressor 4 and is adjusted to the 4th generator 26 after generator 2 has refrigerant steam channel to connect with the 4th generator 26 There is cryogen liquid pipeline again through heater the 24, second generator the 3, the 3rd generator 20 and second throttle 21 and vaporizer 8 Connection, the 4th generator 26 also refrigerant steam channel connects with compressor 4, and heater 24 also has heated medium passage With ft connection.
(2), in flow process, the refrigerant vapour that generator 2 produces is supplied to the 4th generator 26 and makees to drive thermal medium, the second absorber The weak solution of 25 enters the 4th generator 26 through solution pump 11 and solution heat exchanger 13, and refrigerant vapour flows through the 4th generator 26, heating enters its interior solution release refrigerant vapour and provides to compressor 4, and the concentrated solution of the 4th generator 26 is through the 3rd Solution pump 22 and the 4th solution heat exchanger 27 enter generator 2, and the concentrated solution of generator 2 is through the 4th solution heat exchanger 27, solution heat exchanger 13 and the second solution heat exchanger 14 enter the second generator 3；Flow through the cold of the 4th generator 26 Agent steam heat release becomes cryogen liquid, flows through heater the 24, second generator 3 and the 3rd generator 20 progressively heat release the most successively, Enter vaporizer 8 through second throttle 21 throttling again, form the 4th class thermal drivers compressing-absorbing type heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Figure 12 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 1, the 3rd generator, the 3rd solution are increased Pump, the 3rd solution heat exchanger and the second absorber, have weak solution pipeline through solution pump 11 and solution heat exchange by absorber 1 Device 13 connects with generator 2 and is adjusted to absorber 1 and has weak solution pipeline through solution pump 11 and solution heat exchanger 13 and second Absorber 25 connects, and the second absorber 25 has weak solution pipeline again through the 3rd solution pump 22 and the 3rd solution heat exchanger 23 Connect with generator 2, generator 2 is had concentrated solution pipeline through solution heat exchanger 13 and the second solution heat exchanger 14 with Second generator 3 connection is adjusted to generator 2 has concentrated solution pipeline through the 3rd solution heat exchanger 23 and the 3rd generator 20 Connection, the 3rd generator 20 has concentrated solution pipeline again through solution heat exchanger 13 and the second solution heat exchanger 14 and second Raw device 3 connects, and the 3rd generator 20 also refrigerant steam channel connects with the second absorber 25, and the 3rd generator 20 also has High temperature thermal medium passage and ft connection, the second absorber 25 also has heated medium passage and ft connection.
(2) in flow process, the weak solution of absorber 1 through solution pump 11 and the 3rd solution heat exchanger 23 enter the second absorber 25, Absorb refrigerant vapour heat release to hand over through the 3rd solution pump 22 and solution heat in heated medium, the weak solution of the second absorber 25 Parallel operation 13 enters generator 2, and the concentrated solution of generator 2 enters the 3rd generator 20, high-temperature hot through solution heat exchanger 13 Medium flows through the 3rd generator 20, heating enters its interior solution release refrigerant vapour and provides to the second absorber 25, the 3rd The concentrated solution of generator 20 enters the second generator 3, shape through the 3rd solution heat exchanger 23 and the second solution heat exchanger 14 Become the 4th class thermal drivers compressing-absorbing type heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Figure 13 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Figure 12, the 4th generator, second section are increased Stream valve, the 4th solution pump, the 4th solution heat exchanger and heater, it is molten through the 4th that the second absorber 25 sets up weak solution pipeline Liquid pump 28 connects with the 4th generator 26 with the 4th solution heat exchanger 27, and the 4th generator 26 also has concentrated solution pipeline warp 4th solution heat exchanger 27 connects with the 3rd generator 20, has refrigerant steam channel to connect with compressor 4 in generator 2 It is adjusted to the 4th generator 26 after generator 2 has refrigerant steam channel to connect with the 4th generator 26 and has cryogen liquid pipeline again Connecting with vaporizer 8 with second throttle 21 through heater the 24, second generator 3, the 4th generator 26 also has cryogen to steam Vapour passage connects with compressor 4, and heater 24 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 26 and makees to drive thermal medium, the second absorber The part weak solution of 25 enters the 4th generator 26, refrigerant vapour stream through the 4th solution pump 28 and the 4th solution heat exchanger 27 Enter its interior solution release refrigerant vapour through the 4th generator 26, heating and provide to compressor 4, the 4th generator 26 Concentrated solution enters the 3rd generator 20 through the 4th solution heat exchanger 27；The refrigerant vapour heat release flowing through the 4th generator 26 becomes Cryogen liquid, cryogen liquid flows through heater 24 and the second generator 3 progressively heat release successively, after save through second throttle 21 Stream enters vaporizer 8, 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 achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Figure 12, the 4th generator, second section are increased Stream valve, the 4th solution heat exchanger and heater, have weak solution pipeline through the 3rd solution pump 22 and the by the second absorber 25 Three solution heat exchangers 23 connect with generator 2 be adjusted to the second absorber 25 have weak solution pipeline through the 3rd solution pump 22, 3rd solution heat exchanger 23 connects with generator 2 with the 4th solution heat exchanger 27, and generator 2 is had concentrated solution pipeline Connect with the 3rd generator 20 through the 3rd solution heat exchanger 23 and be adjusted to generator 2 and have concentrated solution pipeline through the 4th solution heat Exchanger 27 connects with the 4th generator 26, and the 4th generator 26 has concentrated solution pipeline again through the 3rd solution heat exchanger 23 Connect with the 3rd generator 20, generator 2 has refrigerant steam channel connect with compressor 4 and is adjusted to generator 2 and has cryogen After steam channel and the connection of the 4th generator 26, the 4th generator 26 has cryogen liquid pipeline to occur through heater 24, second again Device 3 connects with vaporizer 8 with second throttle 21, and the 4th generator 26 also refrigerant steam channel connects with compressor 4, 4th generator 26 also has high temperature thermal medium passage and ft connection, and heater 24 also heated medium passage connects with outside Logical.
(2), in flow process, the refrigerant vapour that high temperature thermal medium and generator 2 produce is supplied to the 4th generator 26 and makees to drive thermal medium, The weak solution of the second absorber 25 enters through the 3rd solution pump 22, solution heat exchanger 13 and the 4th solution heat exchanger 27 and sends out Raw device 2, the concentrated solution of generator 2 enters the 4th generator 26, high temperature thermal medium and cryogen through the 4th solution heat exchanger 27 Steam flows separately through the 4th generator 26, heating enters its interior solution release refrigerant vapour and provides to compressor 4, the 4th The concentrated solution of generator 26 enters the 3rd generator 20 through solution heat exchanger 13；Flow through the refrigerant vapour of the 4th generator 26 Heat release becomes cryogen liquid, cryogen liquid to flow through heater 24 and the second generator 3 progressively heat release successively, after through second throttle 21 throttlings enter vaporizer 8, form the 4th class thermal drivers compressing-absorbing type heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump shown in Figure 15 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Figure 12, the 4th generator, second section are increased Stream valve, the 4th solution pump, the 4th solution heat exchanger and heater, have weak solution pipeline molten through the 3rd second absorber 25 Liquid pump 22 and the 3rd solution heat exchanger 23 connect with generator 2 and are adjusted to the second absorber 25 and have weak solution pipeline through the 3rd Solution pump 22 connects with the 4th generator 26 with the 3rd solution heat exchanger 23, and the 4th generator 26 has concentrated solution pipeline again Connect with generator 2 with the 4th solution heat exchanger 27 through the 4th solution pump 28, generator 2 is had concentrated solution pipeline through Three solution heat exchangers 23 connect with the 3rd generator 20 and are adjusted to generator 2 and have concentrated solution pipeline through the 4th solution heat exchange Device 27 connects with the 3rd generator 20 with the 3rd solution heat exchanger 23, and generator 2 is had refrigerant steam channel and compressor 4 connections are adjusted to the 4th generator 26 after generator 2 has refrigerant steam channel to connect with the 4th generator 26 cryogen liquid again Pipeline connects with vaporizer 8 with second throttle 21 through heater the 24, second generator 3, and the 4th generator 26 is the coldest Agent steam channel connects with compressor 4, and heater 24 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 26 and makees to drive thermal medium, the second absorber The weak solution of 25 enters the 4th generator 26 through the second solution pump 22 and the 3rd solution heat exchanger 23, and refrigerant vapour flows through Four generators 26, heating enter its interior solution release refrigerant vapour and also provide to compressor 4, the 4th generator 26 dense molten Liquid enters generator 2 through the 4th solution pump 28 and the 4th solution heat exchanger 27, and the concentrated solution of generator 2 is through the 4th solution heat Exchanger 27 and the 3rd solution heat exchanger 23 enter the 3rd generator 20；Flow through the refrigerant vapour heat release of the 4th generator 26 Become cryogen liquid, cryogen liquid flows through heater 24 and the second generator 3 progressively heat release successively, after through second throttle 21 Throttling enters vaporizer 8, 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 achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Figure 12, the 4th generator, the 4th molten is increased Liquid heat exchanger and the 3rd absorber, have weak solution pipeline through solution pump 11 and solution heat exchanger 13 and by absorber 1 Two absorber 25 connections are adjusted to absorber 1 has weak solution pipeline to connect through the 4th solution heat exchanger 27 and the 3rd absorber 29 Logical, the 3rd absorber 29 has weak solution pipeline to connect with the second absorber 25 with solution heat exchanger 13 through solution pump 11 again, Concentrated solution pipeline is had to connect tune with the second solution heat exchanger 14 with absorber 1 through the second solution pump 12 in second generator 3 Whole is that the second generator 3 has concentrated solution pipeline to connect with the 4th generator 26 through the second solution heat exchanger 14, and the 4th occurs Device 26 has concentrated solution pipeline to connect with absorber 1 with the 4th solution heat exchanger 27 through the second solution pump 12 again, and the 4th occurs Device 26 also refrigerant steam channel connects with the 3rd absorber 29, and the second generator 3 is had cryogen liquid pipeline through choke valve 9 Connect with vaporizer 8 and be adjusted to the second generator 3 and have cryogen liquid pipeline through the 4th generator 26 and choke valve 9 and vaporizer 8 Connection, the 3rd absorber 29 also has coolant guiding channel and ft connection.
(2), in flow process, the weak solution of absorber 1 enters the 3rd absorber 29 through the 4th solution heat exchanger 27, absorbs cryogen steaming Vapour heat release enter in cooling medium, the weak solution of the 3rd absorber 29 through solution pump 11 and the second solution heat exchanger 13 Two absorbers 25；The concentrated solution of the second generator 3 enters the 4th generator 26 through the second solution heat exchanger 14, heat absorption is released Putting refrigerant vapour and provide to the 3rd absorber 29, the concentrated solution of the 4th generator 26 is through the second solution pump 12 and the 4th solution Heat exchanger 27 enters absorber 1；The cryogen liquid of condenser 6 flow through successively the second generator 3 and the 4th generator 26 and by Step heat release, enters vaporizer 8 through choke valve 9 throttling 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 17 is achieved in that
(1) in structure, it mainly by absorber, generator, the second generator, compressor, decompressor, condenser, second Condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat exchanger, the second solution heat Exchanger, high-temperature heat exchanger and regenerator are formed；Absorber 1 has weak solution pipeline through solution pump 11 and solution heat exchange Device 13 connects with generator 2, and generator 2 also has concentrated solution pipeline through solution heat exchanger 13 and the second solution heat exchanger 14 connect with the second generator 3, and the second generator 3 also has concentrated solution pipeline through the second solution pump 12 and the second solution heat exchange Device 14 connects with absorber 1, and generator 2 also refrigerant steam channel connects with compressor 4 through regenerator 16, compressor 4 Also having refrigerant steam channel to connect with decompressor 5 through high-temperature heat exchanger 15, decompressor 5 also has refrigerant steam channel through backheat Device 16 connects with condenser 6, and after condenser 6 also cryogen liquid pipeline and the connection of the second generator 3, the second generator 3 is again Having cryogen liquid pipeline to connect with vaporizer 8 through choke valve 9, the second generator 3 also has refrigerant steam channel and the second condenser 7 Connection, the second condenser 7 also cryogen liquid pipeline connects with vaporizer 8 through cryogen liquid pump 10, and vaporizer 8 also has cryogen to steam Vapour passage connects with absorber 1, and generator 2 and high-temperature heat exchanger 15 have high temperature thermal medium passage and ft connection the most respectively, Absorber 1 and condenser 6 have heated medium passage and ft connection, the second condenser 7 to also have cooling medium to lead to the most respectively Road and ft connection, vaporizer 8 also has low-temperature heat medium passage and ft connection, and decompressor 5 connects compressor 4 and transmits Power.
(2) in flow process, the weak solution of absorber 1 enters generator 2 through solution pump 11 and solution heat exchanger 13, and high-temperature hot is situated between Mass flow enters its interior solution release refrigerant vapour through generator 2, heating and provides to compressor 4 through regenerator 16, occurs The concentrated solution of device 2 enters the second generator 3, heat absorption release cryogen through solution heat exchanger 13 and the second solution heat exchanger 14 Steam also provides to the second condenser 7, and the concentrated solution of the second generator 3 is through the second solution pump 12 and the second solution heat exchanger 14 enter absorber 1, absorption refrigerant vapour heat release in heated medium；Refrigerant vapour flows through regenerator 16 and absorbs heat, it The boosting of rear entrance compressor 4 heats up；Compressor 4 discharge refrigerant vapour flow through high-temperature heat exchanger 15 and absorb heat, laggard Enter decompressor 5 blood pressure lowering work done；The refrigerant vapour of decompressor 5 discharge flows through regenerator 16 heat release, enters condenser 6 afterwards And heat release becomes cryogen liquid in heated medium；The cryogen liquid stream of condenser 6 after the second generator 3 heat release again through choke valve 9 Throttling enters vaporizer 8, and the refrigerant vapour heat release of the second condenser 7 becomes cryogen liquid in cooling medium, the second condenser 7 cold Agent liquid enters vaporizer 8 through cryogen liquid pump 10 pressurization；Low-temperature heat medium flows through vaporizer 8, heating enters its interior cryogen liquid Becoming refrigerant vapour, the refrigerant vapour that vaporizer 8 produces is supplied to absorber 1；The merit of decompressor 5 output is supplied to compressor 4 It is used as power, forms the 4th class thermal drivers compressing-absorbing type heat pump.
The 4th class thermal drivers compressing-absorbing type heat pump that effect that the technology of the present invention can realize is proposed by the invention, has Following effect and advantage:
(1) propose new approaches, new ideas and new technique that the temperature difference utilizes, the further of compressing-absorbing type heat pump techniques will be promoted Development and application.
(2) heat energy (temperature difference) drives, it is achieved heat supply/refrigeration, or externally provides power while of optional.
(3) flow process is reasonable, and performance index is variable and thermodynamic parameter change is corresponding, it is possible to realize the abundant of heat energy (temperature difference) With efficiently utilization.
(4) if desired, realizing heat supply/refrigeration by external impetus, mode is flexible, and adaptability is good.
(5) it is capable of effective utilization of high temperature heat, compensate for the deficiency of absorption heat pump technology, and avoid driving thermal medium Conflicting between parameter with solution property.
(6) rely primarily on latent heat and realize acquisition and the release of thermic load, overcome the deficiency of gas compression formula heat pump techniques.
(7) multiple concrete technical scheme is provided, it is possible to tackle numerous different actual state, have the wider scope of application.
(8) extend heat pump techniques, enrich the type of thermal drivers compressing-absorbing type heat pump, be conducive to heat energy is better achieved Efficiently utilize.

Claims (30)

1. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, the second generator, compressor, swollen Swollen machine, condenser, the second condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat are handed over Parallel operation, the second solution heat exchanger and high-temperature heat exchanger are formed；Absorber (1) has weak solution pipeline through solution pump (11) Connecting with generator (2) with solution heat exchanger (13), generator (2) also has concentrated solution pipeline through solution heat exchanger (13) Connecting with the second generator (3) with the second solution heat exchanger (14), the second generator (3) also has concentrated solution pipeline through the Two solution pumps (12) connect with absorber (1) with the second solution heat exchanger (14), and generator (2) also has refrigerant vapour Passage connects with compressor (4), and compressor (4) also has refrigerant steam channel through high-temperature heat exchanger (15) and decompressor (5) Connection, decompressor (5) also has refrigerant steam channel to connect with condenser (6), condenser (6) also cryogen liquid pipeline and the After two generators (3) connection, the second generator (3) has cryogen liquid pipeline to connect with vaporizer (8) through choke valve (9) again, Second generator (3) also has refrigerant steam channel to connect with the second condenser (7), and the second condenser (7) also has cryogen liquid pipe Road connects with vaporizer (8) through cryogen liquid pump (10), and vaporizer (8) also has refrigerant steam channel to connect with absorber (1), Generator (2) and high-temperature heat exchanger (15) have high temperature thermal medium passage and ft connection the most respectively, absorber (1) and cold Condenser (6) has heated medium passage and ft connection the most respectively, and the second condenser (7) also has coolant guiding channel with outside Connection, vaporizer (8) also has low-temperature heat medium passage and ft connection, and decompressor (5) connects compressor (4) and transmits dynamic Power, forms the 4th class thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor (5) connect compressor (4), solution pump (11) With the second solution pump (12) transmit power.
2. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, the second generator, compressor, swollen Swollen machine, condenser, the second condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat are handed over Parallel operation, the second solution heat exchanger, high-temperature heat exchanger and regenerator are formed；Absorber (1) has weak solution pipeline through solution Pump (11) connects with generator (2) with solution heat exchanger (13), and generator (2) also has concentrated solution pipeline through solution heat Exchanger (13) connects with the second generator (3) with the second solution heat exchanger (14), and the second generator (3) is the denseest Solution line connects with absorber (1) with the second solution heat exchanger (14) through the second solution pump (12), generator (2) Also having refrigerant steam channel to connect with compressor (4), compressor (4) also has refrigerant steam channel through regenerator (16) and height Temperature heat exchanger (15) connects with decompressor (5), and decompressor (5) also has refrigerant steam channel through regenerator (16) with cold Condenser (6) connects, and condenser (6) also has the second generator (3) after cryogen liquid pipeline and the second generator (3) connection Having cryogen liquid pipeline to connect with vaporizer (8) through choke valve (9) again, the second generator (3) also has refrigerant steam channel and the Two condensers (7) connect, and the second condenser (7) also has cryogen liquid pipeline to connect with vaporizer (8) through cryogen liquid pump (10), Vaporizer (8) also has refrigerant steam channel to connect with absorber (1), and generator (2) and high-temperature heat exchanger (15) also divide High temperature thermal medium passage and ft connection, absorber (1) and condenser (6) is not had to have heated medium passage the most respectively with outer Portion connects, and the second condenser (7) also has coolant guiding channel and ft connection, and vaporizer (8) also has low-temperature heat medium passage With ft connection, decompressor (5) connects compressor (4) and transmits power, forms the 4th class thermal drivers compressing-absorbing type heat pump； Wherein, or decompressor (5) connects compressor (4), solution pump (11) and the second solution pump (12) and transmits power.
3. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, the second generator, compressor, swollen Swollen machine, condenser, the second condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat are handed over Parallel operation, the second solution heat exchanger, high-temperature heat exchanger, the second compressor and the second high-temperature heat exchanger are formed；Absorber (1) weak solution pipeline is had to connect with generator (2) with solution heat exchanger (13) through solution pump (11), generator (2) Concentrated solution pipeline is also had to connect with the second generator (3) with the second solution heat exchanger (14) through solution heat exchanger (13), Second generator (3) also has concentrated solution pipeline through the second solution pump (12) and the second solution heat exchanger (14) and absorber (1) Connection, generator (2) also has refrigerant steam channel to connect with compressor (4), and compressor (4) also has refrigerant steam channel warp High-temperature heat exchanger (15) connects with the second compressor (17), and the second compressor (17) also has refrigerant steam channel through second High-temperature heat exchanger (18) connects with decompressor (5), and decompressor (5) also has refrigerant steam channel to connect with condenser (6), After condenser (6) also has cryogen liquid pipeline and the second generator (3) connection, the second generator (3) has cryogen liquid pipeline warp again Choke valve (9) connects with vaporizer (8), and the second generator (3) also has refrigerant steam channel with the second condenser (7) even Logical, the second condenser (7) also has cryogen liquid pipeline to connect with vaporizer (8) through cryogen liquid pump (10), and vaporizer (8) is also Refrigerant steam channel is had to connect with absorber (1), generator (2), high-temperature heat exchanger (15) and the second high-temperature heat exchanger (17) having high temperature thermal medium passage and ft connection the most respectively, absorber (1) and condenser (6) have heated Jie the most respectively Matter passage and ft connection, the second condenser (7) also has coolant guiding channel and ft connection, and vaporizer (8) also has low temperature Hot media channel and ft connection, decompressor (5) connects compressor (4) and the second compressor (17) and transmits power, shape Become the 4th class thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor (5) connect compressor (4), the second compressor (17), Solution pump (11) and the second solution pump (12) also transmit power.
4. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, the second generator, compressor, swollen Swollen machine, condenser, the second condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat are handed over Parallel operation, the second solution heat exchanger, high-temperature heat exchanger, the second high-temperature heat exchanger and the second decompressor are formed；Absorber (1) weak solution pipeline is had to connect with generator (2) with solution heat exchanger (13) through solution pump (11), generator (2) Concentrated solution pipeline is also had to connect with the second generator (3) with the second solution heat exchanger (14) through solution heat exchanger (13), Second generator (3) also has concentrated solution pipeline through the second solution pump (12) and the second solution heat exchanger (14) and absorber (1) Connection, generator (2) also has refrigerant steam channel to connect with compressor (4), and compressor (4) also has refrigerant steam channel warp High-temperature heat exchanger (15) connects with the second decompressor (19), and the second decompressor (19) also has refrigerant steam channel through second High-temperature heat exchanger (18) connects with decompressor (5), and decompressor (5) also has refrigerant steam channel to connect with condenser (6), After condenser (6) also has cryogen liquid pipeline and the second generator (3) connection, the second generator (3) has cryogen liquid pipeline warp again Choke valve (9) connects with vaporizer (8), and the second generator (3) also has refrigerant steam channel with the second condenser (7) even Logical, the second condenser (7) also has cryogen liquid pipeline to connect with vaporizer (8) through cryogen liquid pump (10), and vaporizer (8) is also Refrigerant steam channel is had to connect with absorber (1), generator (2), high-temperature heat exchanger (15) and the second high-temperature heat exchanger (18) having high temperature thermal medium passage and ft connection the most respectively, absorber (1) and condenser (6) have heated Jie the most respectively Matter passage and ft connection, the second condenser (7) also has coolant guiding channel and ft connection, and vaporizer (8) also has low temperature Hot media channel and ft connection, decompressor (5) and the second decompressor (19) connect compressor (4) and transmit power, shape Become the 4th class thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor (5) and the second decompressor (19) connect compressor (4), Solution pump (11) and the second solution pump (12) also transmit power.
5. the 4th class thermal drivers compressing-absorbing type heat pump, is in the 4th class thermal drivers compression-absorption arbitrary described in claim 1-4 In formula heat pump, cancel choke valve, have cryogen liquid pipeline to connect with vaporizer (8) through choke valve (9) in the second generator (3) Being adjusted to the second generator (3) has cryogen liquid pipeline to connect with vaporizer (8), forms the 4th class thermal drivers compressing-absorbing type heat Pump.
6. the 4th class thermal drivers compressing-absorbing type heat pump, is in the 4th class thermal drivers compression-absorption arbitrary described in claim 1-4 In formula heat pump, increase the 3rd generator, second throttle, the 3rd solution pump, the 3rd solution heat exchanger and heater, absorb Device (1) sets up weak solution pipeline through the 3rd solution pump (22) and the 3rd solution heat exchanger (23) and the 3rd generator (20) Connection, the 3rd generator (20) also has concentrated solution pipeline through the 3rd solution heat exchanger (23) and the second solution heat exchanger (14) Connect with the second generator (3), generator (2) has refrigerant steam channel connect with compressor (4) and is adjusted to generator (2) After having refrigerant steam channel to connect with the 3rd generator (20) the 3rd generator (20) have again cryogen liquid pipeline through heater (24), Second generator (3) connects with vaporizer (8) with second throttle (21), and the 3rd generator (20) also has refrigerant vapour Passage connects with compressor (4), and heater (24) also has heated medium passage and ft connection, forms the 4th class thermal drivers Compressing-absorbing type heat pump.
7. the 4th class thermal drivers compressing-absorbing type heat pump, is in the 4th class thermal drivers compression-absorption arbitrary described in claim 1-4 In formula heat pump, increase the 3rd generator, second throttle, the 3rd solution heat exchanger and heater, absorber (1) is had dilute Solution line connects with generator (2) through solution pump (11) and solution heat exchanger (13) and is adjusted to absorber (1) and has dilute Solution line is through solution pump (11), solution heat exchanger (13) and the 3rd solution heat exchanger (23) with generator (2) even Logical, generator (2) is had concentrated solution pipeline through solution heat exchanger (13) and the second solution heat exchanger (14) and second Raw device (3) connection is adjusted to generator (2) has concentrated solution pipeline through the 3rd solution heat exchanger (23) and the 3rd generator (20) Connection, the 3rd generator (20) has concentrated solution pipeline again through solution heat exchanger (13) and the second solution heat exchanger (14) Connect with the second generator (3), generator (2) has refrigerant steam channel connect with compressor (4) and is adjusted to generator (2) After having refrigerant steam channel to connect with the 3rd generator (20) the 3rd generator (20) have again cryogen liquid pipeline through heater (24), Second generator (3) connects with vaporizer (8) with second throttle (21), and the 3rd generator (20) also has refrigerant vapour Passage connects with compressor (4), and heater (24) also has heated medium passage and ft connection, forms the 4th class thermal drivers Compressing-absorbing type heat pump.
8. the 4th class thermal drivers compressing-absorbing type heat pump, is in the 4th class thermal drivers compression-absorption arbitrary described in claim 1-4 In formula heat pump, increase the 3rd generator, second throttle, the 3rd solution pump, the 3rd solution heat exchanger and heater, will inhale Receive device (1) to have weak solution pipeline to connect with generator (2) through solution pump (11) and solution heat exchanger (13) to be adjusted to suction Receiving device (1) has weak solution pipeline to connect with the 3rd generator (20) with solution heat exchanger (13) through solution pump (11), the Three generators (20) have concentrated solution pipeline again through the 3rd solution pump (22) and the 3rd solution heat exchanger (23) and generator (2) Connection, has concentrated solution pipeline through solution heat exchanger (13) and the second solution heat exchanger (14) and second by generator (2) Generator (3) connection is adjusted to generator (2) has concentrated solution pipeline through the 3rd solution heat exchanger (23), solution heat exchanger (13) with the second solution heat exchanger (14) connects with the second generator (3), and generator (2) is had refrigerant steam channel Connect with compressor (4) and be adjusted to after generator (2) has refrigerant steam channel to connect with the 3rd generator (20) the 3rd Raw device (20) has cryogen liquid pipeline again through heater (24), the second generator (3) and second throttle (21) and vaporizer (8) connection, the 3rd generator (20) also has refrigerant steam channel to connect with compressor (4), and heater (24) also has quilt Heating medium passage and ft connection, form the 4th class thermal drivers compressing-absorbing type heat pump.
9. the 4th class thermal drivers compressing-absorbing type heat pump, is in the 4th class thermal drivers compression-absorption arbitrary described in claim 6-8 In formula heat pump, the 3rd generator (20) sets up high temperature thermal medium pipeline and ft connection, forms the 4th class thermal drivers compression-absorption Formula heat pump.
10. the 4th class thermal drivers compressing-absorbing type heat pump, is in the 4th class thermal drivers compression-suction arbitrary described in claim 6-9 In receipts formula heat pump, cancel choke valve and second throttle, the second generator (3) is had cryogen liquid pipeline through choke valve (9) with Vaporizer (8) connection is adjusted to the second generator (3) has cryogen liquid pipeline to connect with vaporizer (8), by the second generator (3) Have cryogen liquid pipeline to connect with vaporizer (8) through second throttle (21) to be adjusted to the second generator (3) and have cryogen liquid pipeline Connect with vaporizer (8), form the 4th class thermal drivers compressing-absorbing type heat pump.
11. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the 4th class thermal drivers compression-suction arbitrary described in claim 1-4 In receipts formula heat pump, increase the 3rd generator, the 3rd solution heat exchanger and the second absorber, absorber (1) is had weak solution pipe Road connects with generator (2) through solution pump (11) and solution heat exchanger (13) and is adjusted to absorber (1) and has weak solution pipe Lu Jing tri-solution heat exchanger (23) connects with the second absorber (25), and the second absorber (25) has weak solution pipeline again Connect with generator (2) with solution heat exchanger (13) through solution pump (11), the second generator (3) is had concentrated solution pipe Road the second solution pump (12) and the second solution heat exchanger (14) connect with absorber (1) and are adjusted to the second generator (3) Having concentrated solution pipeline to connect with the 3rd generator (20) through the second solution heat exchanger (14), the 3rd generator (20) has again Concentrated solution pipeline connects with absorber (1) with the 3rd solution heat exchanger (23) through the second solution pump (12), occurs second Device (3) has cryogen liquid pipeline to connect with vaporizer (8) through choke valve (9) to be adjusted to the second generator (3) and have cryogen liquid pipe Lu Jing tri-generator (20) connects with vaporizer (8) with choke valve (9), and the 3rd generator (20) also has refrigerant vapour Passage and the second absorber (25) connection, the second absorber (25) also has coolant guiding channel 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, are in the 4th class thermal drivers compression-suction arbitrary described in claim 11 In receipts formula heat pump, cancel choke valve, the 3rd generator (20) is had cryogen liquid pipeline through choke valve (9) and vaporizer (8) Connection is adjusted to the 3rd generator (20) has cryogen liquid pipeline to connect with vaporizer (8), forms the 4th class thermal drivers compression-suction Receipts formula heat pump.
13. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the 4th class thermal drivers compression-suction arbitrary described in claim 11 In receipts formula heat pump, increase the 4th generator, second throttle, the 3rd solution pump, the 4th solution heat exchanger and heater, the Two absorbers (25) are set up weak solution pipeline and are occurred with the 4th through the 3rd solution pump (22) and the 4th solution heat exchanger (27) Device (26) connects, and the 4th generator (26) also has concentrated solution pipeline through the 4th solution heat exchanger (27) and the second solution heat Exchanger (14) connects with the second generator (3), has refrigerant steam channel to connect tune with compressor (4) in generator (2) Whole have refrigerant steam channel to connect with the 4th generator (26) for generator (2) after the 4th generator (26) have cryogen liquid again Pipeline is through heater (24), the second generator (3), the 3rd generator (20) and second throttle (21) and vaporizer (8) Connection, the 4th generator (26) also has refrigerant steam channel to connect with compressor (4), and heater (24) also has heated Jie Matter passage and ft connection, form the 4th class thermal drivers compressing-absorbing type heat pump.
14. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the 4th class thermal drivers compression-suction arbitrary described in claim 11 In receipts formula heat pump, increase the 4th generator, second throttle, the 4th solution heat exchanger and heater, by the second absorber (25) There is weak solution pipeline to connect with generator (2) through solution pump (11) and solution heat exchanger (13) and be adjusted to the second absorber (25) There is weak solution pipeline through solution pump (11), solution heat exchanger (13) and the 4th solution heat exchanger (27) and generator (2) Connection, has concentrated solution pipeline through solution heat exchanger (13) and the second solution heat exchanger (14) and second by generator (2) Generator (3) connection is adjusted to generator (2) has concentrated solution pipeline through the 4th solution heat exchanger (27) and the 4th generator (26) connection, the 4th generator (26) has concentrated solution pipeline again through solution heat exchanger (13) and the second solution heat exchanger (14) connect with the second generator (3), generator (2) is had refrigerant steam channel connect with compressor (4) be adjusted to send out After raw device (2) has refrigerant steam channel to connect with the 4th generator (26), the 4th generator (26) has cryogen liquid pipeline warp again Heater (24), the second generator (3), the 3rd generator (20) connect with vaporizer (8) with second throttle (21), 4th generator (26) also has refrigerant steam channel to connect with compressor (4), and heater (24) also has heated medium passage With 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 in the 4th class thermal drivers compression-suction arbitrary described in claim 11 In receipts formula heat pump, increase the 4th generator, second throttle, the 3rd solution pump, the 4th solution heat exchanger and heater, will Second absorber (25) has weak solution pipeline to connect tune with solution heat exchanger (13) with generator (2) through solution pump (11) Whole is that the second absorber (25) has weak solution pipeline through solution pump (11) and solution heat exchanger (13) and the 4th generator (26) Connection, the 4th generator (26) have concentrated solution pipeline through the 3rd solution pump (22) and the 4th solution heat exchanger (27) again and Generator (2) connects, and generator (2) is had concentrated solution pipeline through solution heat exchanger (13) and the second solution heat exchanger (14) connect with the second generator (3) be adjusted to generator (2) have concentrated solution pipeline through the 4th solution heat exchanger (27), Solution heat exchanger (13) connects with the second generator (3) with the second solution heat exchanger (14), is had by generator (2) Refrigerant steam channel connects with compressor (4) and is adjusted to generator (2) and has refrigerant steam channel with the 4th generator (26) even After Tong, the 4th generator (26) has cryogen liquid pipeline again through heater (24), the second generator (3), the 3rd generator (20) Connecting with vaporizer (8) with second throttle (21), the 4th generator (26) also has refrigerant steam channel and compressor (4) Connection, heater (24) also has heated medium passage and ft connection, forms the 4th class thermal drivers compressing-absorbing type heat pump.
16. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the arbitrary 4th class thermal drivers pressure described in claim 13-15 In contracting-absorption heat pump, the 4th generator (26) sets up high temperature thermal medium pipeline 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 in the arbitrary 4th class thermal drivers pressure described in claim 13-16 In contracting-absorption heat pump, cancel choke valve and second throttle, the 3rd generator (20) is had cryogen liquid pipeline through choke valve (9) Connect with vaporizer (8) and be adjusted to the 3rd generator (20) and have cryogen liquid pipeline to connect with vaporizer (8), occur the 3rd Device (20) has cryogen liquid pipeline to connect with vaporizer (8) through second throttle (21) to be adjusted to the 3rd generator (20) and have cold Agent liquid pipeline connects with vaporizer (8), forms the 4th class thermal drivers compressing-absorbing type heat pump.
18. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the 4th class thermal drivers compression-suction arbitrary described in claim 1-4 In receipts formula heat pump, increase the 3rd generator, the 3rd solution pump, the 3rd solution heat exchanger and the second absorber, by absorber (1) There is weak solution pipeline to connect with generator (2) through solution pump (11) and solution heat exchanger (13) and be adjusted to absorber (1) Weak solution pipeline is had to connect with the second absorber (25) with solution heat exchanger (13) through solution pump (11), the second absorber (25) weak solution pipeline is had to connect with generator (2) with the 3rd solution heat exchanger (23) through the 3rd solution pump (22) again, Generator (2) is had concentrated solution pipeline through solution heat exchanger (13) and the second solution heat exchanger (14) and the second generator (3) connection is adjusted to generator (2) has concentrated solution pipeline through the 3rd solution heat exchanger (23) and the 3rd generator (20) Connection, the 3rd generator (20) has concentrated solution pipeline again through solution heat exchanger (13) and the second solution heat exchanger (14) Connecting with the second generator (3), the 3rd generator (20) also has refrigerant steam channel to connect with the second absorber (25), the Three generators (20) also have high temperature thermal medium passage and ft connection, the second absorber (25) also have heated medium passage with Ft connection, forms the 4th class thermal drivers compressing-absorbing type heat pump.
19. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the 4th class thermal drivers compression-absorption described in claim 18 In formula heat pump, cancel choke valve, have cryogen liquid pipeline to connect with vaporizer (8) through choke valve (9) in the second generator (3) Being adjusted to the second generator (3) has cryogen liquid pipeline to connect with vaporizer (8), forms the 4th class thermal drivers compressing-absorbing type heat Pump.
20. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the 4th class thermal drivers compression-absorption described in claim 18 In formula heat pump, increase the 4th generator, second throttle, the 4th solution pump, the 4th solution heat exchanger and heater, second Absorber (25) sets up weak solution pipeline through the 4th solution pump (28) and the 4th solution heat exchanger (27) and the 4th generator (26) connection, the 4th generator (26) also has concentrated solution pipeline through the 4th solution heat exchanger (27) and the 3rd generator (20) Connection, has generator (2) refrigerant steam channel to connect with compressor (4) and is adjusted to generator (2) and has refrigerant steam channel After connecting with the 4th generator (26), the 4th generator (26) has cryogen liquid pipeline again through heater (24), the second generator (3) connecting with vaporizer (8) with second throttle (21), the 4th generator (26) also has refrigerant steam channel and compression Machine (4) connects, and heater (24) also has heated medium passage and ft connection, forms the 4th class thermal drivers compression-absorption Formula heat pump.
21. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the 4th class thermal drivers compression-absorption described in claim 18 In formula heat pump, increase the 4th generator, second throttle, the 4th solution heat exchanger and heater, by the second absorber (25) There is weak solution pipeline to connect with generator (2) through the 3rd solution pump (22) and the 3rd solution heat exchanger (23) and be adjusted to second Absorber (25) has weak solution pipeline through the 3rd solution pump (22), the 3rd solution heat exchanger (23) and the 4th solution heat exchange Device (27) connects with generator (2), generator (2) has concentrated solution pipeline through the 3rd solution heat exchanger (23) and the Three generators (20) connection is adjusted to generator (2) has concentrated solution pipeline to occur with the 4th through the 4th solution heat exchanger (27) Device (26) connects, and the 4th generator (26) has concentrated solution pipeline again through the 3rd solution heat exchanger (23) and the 3rd generator (20) connection, has generator (2) refrigerant steam channel to connect with compressor (4) and is adjusted to generator (2) and has cryogen to steam Vapour passage and the 4th generator (26) connection after the 4th generator (26) have again cryogen liquid pipeline through heater (24), second Raw device (3) connects with vaporizer (8) with second throttle (21), and the 4th generator (26) also has refrigerant steam channel and pressure Contracting machine (4) connects, and heater (24) also has heated medium passage and ft connection, forms the 4th class thermal drivers compression-suction Receipts formula heat pump.
22. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the 4th class thermal drivers compression-absorption described in claim 18 In formula heat pump, increase the 4th generator, second throttle, the 4th solution pump, the 4th solution heat exchanger and heater, by the Two absorbers (25) have weak solution pipeline through the 3rd solution pump (22) and the 3rd solution heat exchanger (23) and generator (2) Connection is adjusted to the second absorber (25) has weak solution pipeline through the 3rd solution pump (22) and the 3rd solution heat exchanger (23) Connecting with the 4th generator (26), the 4th generator (26) has concentrated solution pipeline molten through the 4th solution pump (28) and the 4th again Liquid heat exchanger (27) connects with generator (2), and generator (2) is had concentrated solution pipeline through the 3rd solution heat exchanger (23) Connect with the 3rd generator (20) and be adjusted to generator (2) and have concentrated solution pipeline through the 4th solution heat exchanger (27) and the 3rd Solution heat exchanger (23) connects with the 3rd generator (20), and generator (2) has refrigerant steam channel and compressor (4) Connection is adjusted to the 4th generator (26) after generator (2) has refrigerant steam channel to connect with the 4th generator (26) to be had again Cryogen liquid pipeline connects with vaporizer (8) with second throttle (21) through heater (24), the second generator (3), and the 4th Generator (26) also has refrigerant steam channel to connect with compressor (4), and heater (24) also has heated medium passage with outer Portion connects, and forms the 4th class thermal drivers compressing-absorbing type heat pump.
23. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the arbitrary 4th class thermal drivers pressure described in claim 20-22 In contracting-absorption heat pump, the 4th generator (26) sets up high temperature thermal medium pipeline and ft connection, forms the 4th class thermal drivers pressure Contracting-absorption heat pump.
24. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the arbitrary 4th class thermal drivers pressure described in claim 20-23 In contracting-absorption heat pump, cancel choke valve and second throttle, the second generator (3) is had cryogen liquid pipeline through choke valve (9) Connect with vaporizer (8) and be adjusted to the second generator (3) and have cryogen liquid pipeline to connect with vaporizer (8), by the second generator (3) have cryogen liquid pipeline to connect with vaporizer (8) through second throttle (21) to be adjusted to the second generator (3) and have cryogen liquid Pipeline connects with vaporizer (8), forms the 4th class thermal drivers compressing-absorbing type heat pump.
25. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the 4th class thermal drivers compression-suction arbitrary described in claim 18 In receipts formula heat pump, increase the 4th generator, the 4th solution heat exchanger and the 3rd absorber, absorber (1) is had weak solution pipe Road connects with the second absorber (25) through solution pump (11) and solution heat exchanger (13) and is adjusted to absorber (1) and has dilute molten Liquid pipeline connects with the 3rd absorber (29) through the 4th solution heat exchanger (27), and the 3rd absorber (29) has weak solution again Pipeline connects with the second absorber (25) with solution heat exchanger (13) through solution pump (11), is had by the second generator (3) Concentrated solution pipeline connects with absorber (1) through the second solution pump (12) and the second solution heat exchanger (14) and is adjusted to second Raw device (3) has concentrated solution pipeline to connect with the 4th generator (26) through the second solution heat exchanger (14), the 4th generator (26) Concentrated solution pipeline is had to connect with absorber (1) with the 4th solution heat exchanger (27) through the second solution pump (12) again, the 4th Raw device (26) also has refrigerant steam channel to connect with the 3rd absorber (29), and the second generator (3) is had cryogen liquid pipeline warp Choke valve (9) connect with vaporizer (8) be adjusted to the second generator (3) have cryogen liquid pipeline through the 4th generator (26) and Choke valve (9) connects with vaporizer (8), and the 3rd absorber (29) also has coolant guiding channel and ft connection, forms the Four class thermal drivers compressing-absorbing type heat pumps.
26. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the 4th class thermal drivers compression-suction arbitrary described in claim 25 In receipts formula heat pump, cancel choke valve, the 4th generator (26) is had cryogen liquid pipeline through choke valve (9) and vaporizer (8) Connection is adjusted to the 4th generator (26) has cryogen liquid pipeline to connect with vaporizer (8), forms the 4th class thermal drivers compression-suction Receipts formula heat pump.
27. the 4th class thermal drivers compressing-absorbing type heat pumps, mainly by absorber, generator, the second generator, compressor, Decompressor, condenser, the second condenser, vaporizer, choke valve, cryogen liquid pump, solution pump, the second solution pump, solution heat Exchanger, the second solution heat exchanger, high-temperature heat exchanger and regenerator are formed；Absorber (1) has weak solution pipeline through molten Liquid pump (11) connects with generator (2) with solution heat exchanger (13), and generator (2) also has concentrated solution pipeline through solution Heat exchanger (13) connects with the second generator (3) with the second solution heat exchanger (14), and the second generator (3) also has Concentrated solution pipeline connects with absorber (1) with the second solution heat exchanger (14) through the second solution pump (12), generator (2) Also having refrigerant steam channel to connect with compressor (4) through regenerator (16), compressor (4) also has refrigerant steam channel through height Temperature heat exchanger (15) connects with decompressor (5), and decompressor (5) also has refrigerant steam channel through regenerator (16) with cold Condenser (6) connects, and condenser (6) also has the second generator (3) after cryogen liquid pipeline and the second generator (3) connection Having cryogen liquid pipeline to connect with vaporizer (8) through choke valve (9) again, the second generator (3) also has refrigerant steam channel and the Two condensers (7) connect, and the second condenser (7) also has cryogen liquid pipeline to connect with vaporizer (8) through cryogen liquid pump (10), Vaporizer (8) also has refrigerant steam channel to connect with absorber (1), and generator (2) and high-temperature heat exchanger (15) also divide High temperature thermal medium passage and ft connection, absorber (1) and condenser (6) is not had to have heated medium passage the most respectively with outer Portion connects, and the second condenser (7) also has coolant guiding channel and ft connection, and vaporizer (8) also has low-temperature heat medium passage With ft connection, decompressor (5) connects compressor (4) and transmits power, forms the 4th class thermal drivers compressing-absorbing type heat pump； Wherein, or decompressor (5) connects compressor (4), solution pump (11) and the second solution pump (12) and transmits power.
28. the 4th class thermal drivers compressing-absorbing type heat pumps, are at the 4th class thermal drivers compressing-absorbing type described in claim 27 In heat pump, cancel choke valve, have cryogen liquid pipeline to connect tune through choke valve (9) with vaporizer (8) in the second generator (3) Whole is that the second generator (3) has cryogen liquid pipeline to connect with vaporizer (8), 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 arbitrary first kind thermal drivers pressure described in claim 1-28 In contracting-absorption heat pump, increasing working machine, decompressor (5) connects working machine and provides power to working machine, and it is additional right to be formed 4th class thermal drivers compressing-absorbing type heat pump of outer offer living load.
30. the 4th class thermal drivers compressing-absorbing type heat pumps, are in the arbitrary first kind thermal drivers pressure described in claim 1-28 In contracting-absorption heat pump, increasing engine, engine connects compressor (4) and provides power to compressor (4), is formed attached Add the 4th class thermal drivers compressing-absorbing type heat pump that external impetus drives.
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CN115218551A (en) * 2020-03-02 2022-10-21 李华玉 Thermally driven compression-absorption heat pump
CN115218542A (en) * 2020-02-29 2022-10-21 李华玉 Compression-absorption heat pump
CN115218539A (en) * 2020-02-29 2022-10-21 李华玉 Thermally driven compression-absorption heat pump
CN115218535A (en) * 2020-02-21 2022-10-21 李华玉 Thermally driven compression-absorption heat pump

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CN115218539A (en) * 2020-02-29 2022-10-21 李华玉 Thermally driven compression-absorption heat pump
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