CN105910341A - First kind thermal driving compression-absorption heat pump - Google Patents

First kind thermal driving compression-absorption heat pump Download PDF

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Publication number
CN105910341A
CN105910341A CN201610243619.4A CN201610243619A CN105910341A CN 105910341 A CN105910341 A CN 105910341A CN 201610243619 A CN201610243619 A CN 201610243619A CN 105910341 A CN105910341 A CN 105910341A
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generator
solution
heat exchanger
connect
decompressor
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CN105910341B (en
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李华玉
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B30/00—Heat pumps
    • F25B30/06—Heat pumps characterised by the source of low potential heat
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B25/00—Machines, plants or systems, using a combination of modes of operation covered by two or more of the groups F25B1/00 - F25B23/00
    • F25B25/02—Compression-sorption machines, plants, or systems

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

Abstract

The invention provides a first kind thermal driving compression-absorption heat pump, and belongs to the heat pump and thermal energy utilization technical field; an absorber is connected with a generator through a solution pump and a solution heat exchanger; the generator is connected with the absorber through the solution heat exchanger, and connected with a condenser through a cryogen steam channel; the condenser uses a cryogen liquid pipeline to connect with an evaporator through a throttle; the evaporator is connected with the absorber through the cryogen steam channel; an outer low temperature thermal medium channel is connected with a compressor; the compressor uses the low temperature thermal medium channel to connect with an expander through a high temperature heat exchanger; the expander uses the low temperature thermal medium channel to connected with a second expander through the evaporator; the second expander is connected with the outer side through the low temperature thermal medium channel; the generator and the high temperature heat exchanger are connected with the outer side through a high temperature thermal medium channel; the absorber and the condenser are connected with the outer side through a heated medium channel; the expander and the second expander are connected with the compressor for power transmission, thus forming the first kind thermal driving compression-absorption heat pump.

Description

First kind 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 class of low-temperature heat medium Type, 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 rationally, efficiently It is applied in absorption heat pump flow process, causes its application and range of application by bigger restriction, also cannot give play to absorption The advantage that formula heat pump techniques refrigerant vapour latent heat is big.
Further, the kind of low-temperature heat source, with or without with the condition such as temperature height, restriction absorption heat pump technology plays a role Key factor.Such as, the absorption heat pump with lithium bromide water solution as working medium, it is difficult to adapt to the low-temperature heat medium of lower temperature, This seriously constrains the application of absorption heat pump.
In order to play the technical advantage of absorption heat pump, improve the value of high-temperature hot load, solve the source of low-temperature heat source And limiting factor, and consider take into account power drive or meet external impetus demand, the present invention proposes to comprise with compressor, expansion Including the component such as machine and high-temperature heat exchanger, the temperature difference between high temperature heat source and heated medium is effectively utilized or to high temperature Between thermal source and environment, the temperature difference effectively utilizes, and has the first kind thermal drivers compressing-absorbing type heat pump of comprehensive advantage.
Summary of the invention:
Present invention is primarily intended to provide series first kind thermal drivers compressing-absorbing type heat pump, concrete summary of the invention subitem to illustrate As follows:
1. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, vaporizer, throttling Valve, solution pump, solution heat exchanger, compressor, decompressor, the second decompressor and high-temperature heat exchanger are formed；Absorb Device has weak solution pipeline to connect with generator with solution heat exchanger through solution pump, and generator also has concentrated solution pipeline through solution heat Exchanger connects with absorber, and generator also has refrigerant steam channel to connect with condenser, and condenser also has cryogen liquid pipeline warp Choke valve connects with vaporizer, and vaporizer also has refrigerant steam channel to connect with absorber, outside have low-temperature heat medium passage with Compressor connects, and compressor also has low-temperature heat medium passage to connect with decompressor through high-temperature heat exchanger, and decompressor also has low temperature Hot media channel connects through vaporizer and the second decompressor, and the second decompressor also has low-temperature heat medium passage and ft connection, sends out Raw device and high-temperature heat exchanger have high temperature thermal medium passage and ft connection, absorber and condenser to have the most respectively to be added the most respectively Hot media channel and ft connection, decompressor and the second decompressor connect compressor and transmit power, form first kind thermal drivers Compressing-absorbing type heat pump；Wherein, or decompressor and the second decompressor connect compressor and solution pump and transmit power.
2. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, vaporizer, throttling Valve, solution pump, solution heat exchanger, compressor, decompressor, the second decompressor, high-temperature heat exchanger, the second compressor Formed with the second high-temperature heat exchanger；Absorber has weak solution pipeline to connect with generator with solution heat exchanger through solution pump, Generator also has concentrated solution pipeline to connect with absorber through solution heat exchanger, and generator also has refrigerant steam channel and condenser Connection, condenser also has cryogen liquid pipeline to connect with vaporizer through choke valve, and vaporizer also has refrigerant steam channel and absorber Connection, outside has low-temperature heat medium passage to connect with compressor, and compressor also has low-temperature heat medium passage through high-temperature heat exchanger Connecting with the second compressor, the second compressor also has low-temperature heat medium passage to connect with decompressor through the second high-temperature heat exchanger, Decompressor also has low-temperature heat medium passage to connect through vaporizer and the second decompressor, and the second decompressor also has low-temperature heat medium passage With ft connection, generator, high-temperature heat exchanger and the second 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, decompressor and the second decompressor to connect pressure the most respectively Contracting machine and the second compressor also transmit power, form first kind thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor and Two decompressors connect compressor, the second compressor and solution pump and transmit power.
3. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, vaporizer, throttling Valve, solution pump, solution heat exchanger, compressor, decompressor, the second decompressor, high-temperature heat exchanger, the second high-temperature hot Exchanger and the 3rd decompressor are formed；Absorber has weak solution pipeline to connect with generator with solution heat exchanger through solution pump, Generator also has concentrated solution pipeline to connect with absorber through solution heat exchanger, and generator also has refrigerant steam channel and condenser Connection, condenser also has cryogen liquid pipeline to connect with vaporizer through choke valve, and vaporizer also has refrigerant steam channel and absorber Connection, outside has low-temperature heat medium passage to connect with compressor, and compressor also has low-temperature heat medium passage through high-temperature heat exchanger Connecting with the 3rd decompressor, the 3rd decompressor also has low-temperature heat medium passage to connect with decompressor through the second high-temperature heat exchanger, Decompressor also has low-temperature heat medium passage to connect through vaporizer and the second decompressor, and the second decompressor also has low-temperature heat medium passage With ft connection, generator, high-temperature heat exchanger and the second 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, decompressor, the second decompressor and the 3rd the most respectively Decompressor connects compressor and transmits power, forms first kind thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor, Two decompressors and the 3rd decompressor connect compressor and solution pump and transmit power.
4. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, vaporizer, throttling Valve, solution pump, solution heat exchanger, compressor, decompressor, the second decompressor, high-temperature heat exchanger and the second compressor Formed；Absorber has weak solution pipeline to connect with generator with solution heat exchanger through solution pump, and generator also has concentrated solution Pipeline connects with absorber through solution heat exchanger, and generator also has refrigerant steam channel to connect with condenser, and condenser also has Cryogen liquid pipeline connects with vaporizer through choke valve, and vaporizer also has refrigerant steam channel to connect with absorber, and there is low temperature outside Hot media channel connects with compressor, and compressor also has low-temperature heat medium passage to connect with decompressor through high-temperature heat exchanger, swollen Swollen machine also has low-temperature heat medium passage to connect through vaporizer and the second compressor, and the second compressor also has low-temperature heat medium passage warp Vaporizer and the connection of the second decompressor, the second decompressor also has low-temperature heat medium passage and ft connection, generator and high-temperature hot Exchanger have the most respectively high temperature thermal medium passage and ft connection, absorber and condenser have the most respectively heated medium passage with Ft connection, decompressor and the second decompressor connect compressor and the second compressor and transmit power, form first kind thermal drivers Compressing-absorbing type heat pump；Wherein, or decompressor and the second decompressor connect compressor, the second compressor and solution pump and transmit Power.
5. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, vaporizer, throttling Valve, solution pump, solution heat exchanger, compressor, decompressor, the second decompressor, high-temperature heat exchanger and regenerator institute group Become；Absorber has weak solution pipeline to connect with generator with solution heat exchanger through solution pump, and generator also has concentrated solution pipeline Connecting with absorber through solution heat exchanger, generator also has refrigerant steam channel to connect with condenser, and condenser also has cryogen Liquid pipeline connects with vaporizer through choke valve, and vaporizer also has refrigerant steam channel to connect with absorber, and outside has Low Temperature Thermal to be situated between Matter passage connects with compressor, and compressor also has low-temperature heat medium passage to connect with decompressor with high-temperature heat exchanger through regenerator, Decompressor also has low-temperature heat medium passage to connect with vaporizer and the second decompressor through regenerator, and the second decompressor also has Low Temperature Thermal Medium channel and ft connection, generator and high-temperature heat exchanger have high temperature thermal medium passage and ft connection the most respectively, absorb Device and condenser have heated medium passage and ft connection, decompressor and the second decompressor connect compressor and transmit the most respectively Power, forms first kind thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor and the second decompressor connect compressor and molten Liquid pump also transmits power.
6. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, vaporizer, throttling Valve, solution pump, solution heat exchanger, compressor, decompressor, the second decompressor, high-temperature heat exchanger and regenerator institute group Become；Absorber has weak solution pipeline to connect with generator with solution heat exchanger through solution pump, and generator also has concentrated solution pipeline Connecting with absorber through solution heat exchanger, generator also has refrigerant steam channel to connect with condenser, and condenser also has cryogen Liquid pipeline connects with vaporizer through choke valve, and vaporizer also has refrigerant steam channel to connect with absorber, and outside has Low Temperature Thermal to be situated between Matter passage connects with compressor through regenerator, and compressor also has low-temperature heat medium passage to connect with decompressor through high-temperature heat exchanger, Decompressor also has low-temperature heat medium passage to connect with regenerator and the second decompressor through vaporizer, and the second decompressor also has Low Temperature Thermal Medium channel and ft connection, generator and high-temperature heat exchanger have high temperature thermal medium passage and ft connection the most respectively, absorb Device and condenser have heated medium passage and ft connection, decompressor and the second decompressor connect compressor and transmit the most respectively Power, forms first kind thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor and the second decompressor connect compressor and molten Liquid pump also transmits power.
7. first kind thermal drivers compressing-absorbing type heat pump, is to compress at the arbitrary first kind thermal drivers described in 1-6 item-absorb Formula heat pump, increases the second generator, second throttle, the second solution pump and the second solution heat exchanger, and absorber is set up dilute Solution line is through the second solution pump and the second solution heat exchanger and the connection of the second generator, and the second generator also has concentrated solution pipe Road the second solution heat exchanger connects with absorber, generator has refrigerant steam channel connect with condenser and is adjusted to generation After device has refrigerant steam channel to connect with the second generator, the second generator has cryogen liquid pipeline again through second throttle and condensation Device connects, and the second generator also has refrigerant steam channel to connect with condenser, forms first kind thermal drivers compressing-absorbing type heat pump.
8. first kind thermal drivers compressing-absorbing type heat pump, is to compress at the arbitrary first kind thermal drivers described in 1-6 item-absorb Formula heat pump, increases the second generator, second throttle and the second solution heat exchanger, absorber has weak solution pipeline through molten Liquid pump and solution heat exchanger connect with generator be adjusted to absorber have weak solution pipeline through solution pump, solution heat exchanger and Second solution heat exchanger connects with generator, and generator has concentrated solution pipeline connect tune with absorber through solution heat exchanger Whole have concentrated solution pipeline to connect through the second solution heat exchanger and the second generator for generator, and the second generator has concentrated solution again Pipeline connects with absorber through solution heat exchanger, generator has refrigerant steam channel connect with condenser and is adjusted to generator After having refrigerant steam channel to connect with the second generator, the second generator has cryogen liquid pipeline again through second throttle and condenser Connection, the second generator also has refrigerant steam channel to connect with condenser, forms first kind thermal drivers compressing-absorbing type heat pump.
9. first kind thermal drivers compressing-absorbing type heat pump, is to compress at the arbitrary first kind thermal drivers described in 1-6 item-absorb Formula heat pump, increases the second generator, second throttle, the second solution pump and the second solution heat exchanger, is had by absorber dilute Solution line connects with generator through solution pump and solution heat exchanger and is adjusted to absorber and has weak solution pipeline through solution pump and molten Liquid heat exchanger and the connection of the second generator, the second generator has concentrated solution pipeline to hand over through the second solution pump and the second solution heat again Parallel operation connects with generator, generator has concentrated solution pipeline connect with absorber through solution heat exchanger and is adjusted to generator and has Concentrated solution pipeline connects with absorber with solution heat exchanger through the second solution heat exchanger, and generator is had refrigerant steam channel Connect with condenser and be adjusted to the second generator after generator has refrigerant steam channel to connect with the second generator and have cryogen liquid again Pipeline connects with condenser through second throttle, and the second generator also has refrigerant steam channel to connect with condenser, forms first Class thermal drivers compressing-absorbing type heat pump.
10. first kind thermal drivers compressing-absorbing type heat pump, is at the described arbitrary first kind thermal drivers compressing-absorbing type of 1-6 item Heat pump, increases the second generator, the second absorber, the second solution pump and the second solution heat exchanger, is had by absorber dilute molten Liquid pipeline connects with generator through solution pump and solution heat exchanger and is adjusted to absorber and has 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 second solution pump and the second solution heat exchange Device connects with generator, generator has concentrated solution pipeline connect with absorber through solution heat exchanger and is adjusted to generator and has dense Solution line connects through the second solution heat exchanger and the second generator, and the second generator has concentrated solution pipeline to hand over through solution heat again Parallel operation connects with absorber, and the second generator also has refrigerant steam channel to connect with the second absorber, and the second generator also has height Warm passage and ft connection, the second absorber also has heated medium passage and ft connection, forms first kind heat and drives Dynamic pressure contracting-absorption heat pump.
11. first kind thermal drivers compressing-absorbing type heat pumps, are at the 10th described arbitrary first kind thermal drivers compressing-absorbing type Heat pump, increases the 3rd generator, second throttle, the 3rd solution pump and the 3rd solution heat exchanger, and the second absorber is set up Weak solution pipeline is through the 3rd solution pump and the 3rd solution heat exchanger and the connection of the 3rd generator, and the 3rd generator also has concentrated solution Pipeline connects through the 3rd solution heat exchanger and the second generator, and generator has refrigerant steam channel connect adjustment with condenser After having refrigerant steam channel to connect with the 3rd generator for generator, the 3rd generator has cryogen liquid pipeline again through second throttle Connecting with condenser, the 3rd generator also has refrigerant steam channel to connect with condenser, forms first kind thermal drivers compression-absorption Formula heat pump.
12. first kind thermal drivers compressing-absorbing type heat pumps, are at the 10th described arbitrary first kind thermal drivers compressing-absorbing type Heat pump, increases the 3rd generator, second throttle and the 3rd solution heat exchanger, the second absorber has weak solution pipeline warp Second solution pump and the second solution heat exchanger connect with generator and are adjusted to the second absorber and have weak solution pipeline through the second solution Pump, the second solution heat exchanger and the 3rd solution heat exchanger connect with generator, generator have concentrated solution pipeline through 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 to connect, by generator through the second solution heat exchanger and the second generator again There is refrigerant steam channel to connect with condenser and be adjusted to after generator has refrigerant steam channel to connect with the 3rd generator the 3rd Raw device has cryogen liquid pipeline to connect with condenser through second throttle again, and the 3rd generator also has refrigerant steam channel and condenser Connection, forms first kind thermal drivers compressing-absorbing type heat pump.
13. first kind thermal drivers compressing-absorbing type heat pumps, are at the 10th described arbitrary first kind thermal drivers compressing-absorbing type Heat pump, increases the 3rd generator, second throttle, the 3rd solution pump and the 3rd solution heat exchanger, is had by the second absorber Weak solution pipeline connects with generator through the second solution pump and the second solution heat exchanger and is adjusted to the second absorber and has weak solution pipe Road the second solution pump and the second solution heat exchanger and the connection of the 3rd generator, the 3rd generator has concentrated solution pipeline again through the Three solution pumps and the 3rd solution heat exchanger connect with generator, generator have concentrated solution pipeline through the second solution heat exchanger Connect with the second generator be adjusted to generator have concentrated solution pipeline through the 3rd solution heat exchanger and the second solution heat exchanger with Second generator connection, generator is had refrigerant steam channel connect with condenser be adjusted to generator have refrigerant steam channel and After 3rd generator connection, the 3rd generator has cryogen liquid pipeline to connect with condenser through second throttle again, the 3rd generator Also have refrigerant steam channel to connect with condenser, form first kind thermal drivers compressing-absorbing type heat pump.
14. first kind thermal drivers compressing-absorbing type heat pumps, are in 1-6,10 described arbitrary first kind thermal drivers compressions In-absorption heat pump, increase newly-increased generator, newly-increased absorber, new solubilization liquid pump and newly-increased solution heat exchanger, will occur Device has refrigerant steam channel to connect with condenser to be adjusted to generator and have refrigerant steam channel to connect with newly-increased absorber, newly-increased inhales Receiving device also has weak solution pipeline to connect with newly-increased generator with newly-increased solution heat exchanger through new solubilization liquid pump, and newly-increased generator is also Having concentrated solution pipeline to connect with newly-increased absorber through newly-increased solution heat exchanger, newly-increased generator also has refrigerant steam channel with cold Condenser connects, and newly-increased generator also has high temperature thermal medium passage and ft connection, newly-increased absorber to also have heated medium passage With ft connection, form first kind thermal drivers compressing-absorbing type heat pump.
15. first kind thermal drivers compressing-absorbing type heat pumps, are in 7-9 item described arbitrary first kind thermal drivers compression-absorption In formula heat pump, the second generator sets up high temperature thermal medium passage and ft connection, forms first kind thermal drivers compressing-absorbing type heat Pump.
16. first kind thermal drivers compressing-absorbing type heat pumps, are in 11-13 item described arbitrary first kind thermal drivers compression-suction In receipts formula heat pump, the 3rd generator sets up high temperature thermal medium passage and ft connection, forms first kind thermal drivers compressing-absorbing type Heat pump.
17. first kind thermal drivers compressing-absorbing type heat pumps, are in 1-16 item described arbitrary first kind thermal drivers compression-absorption In formula heat pump, increasing engine, engine connects compressor and transmits power to compressor, forms additional external power drive First kind thermal drivers compressing-absorbing type heat pump.
18. first kind thermal drivers compressing-absorbing type heat pumps, are in 1-16 item described arbitrary first kind thermal drivers compression-absorption In formula heat pump, increasing working machine, decompressor connects working machine and transmits power to working machine, and being formed to add externally provides power The first kind thermal drivers compressing-absorbing type heat pump of load.
Accompanying drawing illustrates:
Fig. 1 is based on the 1st kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 2 is based on the 2nd kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 3 is based on the 3rd kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 4 is based on the 4th kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 5 is based on the 5th kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 6 is based on the 6th kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 7 is based on the 7th kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 8 is based on the 8th kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 9 is based on the 9th kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 10 is based on the 10th kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 11 is based on the 11st kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 12 is based on the 12nd kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 13 is based on the 13rd kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 14 is based on the 14th kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 15 is based on the 15th kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 16 is based on the 16th kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
In figure, 1-absorber, 2-generator, 3-condenser, 4-vaporizer, 5-choke valve, 6-solution pump, 7-is molten Liquid heat exchanger, 8-compressor, 9-decompressor, 10-the second decompressor, 11-high-temperature heat exchanger, 12-second presses Contracting machine, 13-the second high-temperature heat exchanger, 14-the 3rd decompressor, 15-regenerator, 16-the second generator, 17- Two choke valves, 18-the second solution pump, 19-the second solution heat exchanger, 20-the second absorber, 21-the 3rd generator, 22-the 3rd solution pump, 23-the 3rd solution heat exchanger, 24-engine, 25-working machine；A-increases generator newly, and B-is new Increasing absorber, C-new solubilization liquid pump, D-increases solution heat exchanger newly.
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.
First kind thermal drivers compressing-absorbing type heat pump shown in Fig. 1 is achieved in that
(1), in structure, it is mainly handed over by absorber, generator, condenser, vaporizer, choke valve, solution pump, solution heat Parallel operation, compressor, decompressor, the second decompressor and high-temperature heat exchanger are formed；Absorber 1 has weak solution pipeline through molten Liquid pump 6 connects with generator 2 with solution heat exchanger 7, generator 2 also have concentrated solution pipeline through solution heat exchanger 7 with Absorber 1 connects, and generator 2 also refrigerant steam channel connects with condenser 3, and condenser 3 also has cryogen liquid pipeline warp Choke valve 5 connects with vaporizer 4, and vaporizer 4 also refrigerant steam channel connects with absorber 1, and outside has Low Temperature Thermal to be situated between Matter passage connects with compressor 8, and compressor 8 also low-temperature heat medium passage connects with decompressor 9 through high-temperature heat exchanger 11, Decompressor 9 also low-temperature heat medium passage connects with the second decompressor 10 through vaporizer 4, and the second decompressor 10 also has low temperature Hot media channel and ft connection, generator 2 and high-temperature heat exchanger 11 have high temperature thermal medium passage and ft connection the most respectively, Absorber 1 and condenser 3 have heated medium passage and ft connection, decompressor 9 and the second decompressor 10 to connect the most respectively Compressor 8 also transmits power.
(2), in flow process, the weak solution of absorber 1 enters generator 2, high temperature thermal medium through solution pump 6 and solution heat exchanger 7 Flow through generator 2, heating enters its interior solution release refrigerant vapour and provides to condenser 3, the concentrated solution warp of generator 2 Solution heat exchanger 7 enters absorber 1, absorbs refrigerant vapour heat release in heated medium；The refrigerant vapour of condenser 3 is put Heat becomes cryogen liquid in heated medium, and the cryogen liquid stream of condenser 3 enters vaporizer 4 through choke valve 5 throttling, vaporizer 4 Cryogen liquid absorbs heat into refrigerant vapour and provides to absorber 1；Outer low temperature thermal medium enters compressor 8 boosting and heats up, and flows through High-temperature heat exchanger 11 also absorbs heat, and enters decompressor 9 blood pressure lowering work done afterwards；The low-temperature heat medium of decompressor 9 discharge flows through steaming Send out device 4 heat release, enter the second decompressor 10 blood pressure lowering work done afterwards and externally discharge；Decompressor 9 and the second decompressor 10 The merit of output is supplied to compressor 8 and is used as power, and forms first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Fig. 2 is achieved in that
(1), in structure, it is mainly handed over by absorber, generator, condenser, vaporizer, choke valve, solution pump, solution heat Parallel operation, compressor, decompressor, the second decompressor, high-temperature heat exchanger, the second compressor and the second high-temperature heat exchanger institute Composition；Absorber 1 has weak solution pipeline to connect with generator 2 with solution heat exchanger 7 through solution pump 6, and generator 2 is also Having concentrated solution pipeline to connect with absorber 1 through solution heat exchanger 7, generator 2 also has refrigerant steam channel and condenser 3 Connection, condenser 3 also cryogen liquid pipeline connects with vaporizer 4 through choke valve 5, and vaporizer 4 also has refrigerant steam channel Connecting with absorber 1, outside has low-temperature heat medium passage to connect with compressor 8, and compressor 8 also has low-temperature heat medium passage Connecting with the second compressor 12 through high-temperature heat exchanger 11, the second compressor 12 also has low-temperature heat medium passage through the second high temperature Heat exchanger 13 connects with decompressor 9, and decompressor 9 also has low-temperature heat medium passage through vaporizer 4 and the second decompressor 10 Connection, the second decompressor 10 also has low-temperature heat medium passage and ft connection, generator 2, high-temperature heat exchanger 11 and second High-temperature heat exchanger 13 has high temperature thermal medium passage and ft connection, absorber 1 and condenser 3 to have the most respectively to be added the most respectively Hot media channel and ft connection, decompressor 9 and the second decompressor 10 connect compressor 8 and the second compressor 12 and transmit Power.
(2), in flow process, the weak solution of absorber 1 enters generator 2, high temperature thermal medium through solution pump 6 and solution heat exchanger 7 Flow through generator 2, heating enters its interior solution release refrigerant vapour and provides to condenser 3, the concentrated solution warp of generator 2 Solution heat exchanger 7 enters absorber 1, absorbs refrigerant vapour heat release in heated medium；The refrigerant vapour of condenser 3 is put Heat becomes cryogen liquid in heated medium, and the cryogen liquid stream of condenser 3 enters vaporizer 4 through choke valve 5 throttling, vaporizer 4 Cryogen liquid absorbs heat into refrigerant vapour and provides to absorber 1；Outer low temperature thermal medium enters compressor 8 boosting and heats up, and flows through High-temperature heat exchanger 11 also absorbs heat, and enters the second compressor 12 boosting afterwards and heats up；The Low Temperature Thermal of the second compressor 12 discharge Medium flows through the second high-temperature heat exchanger 13 and absorbs heat, and enters decompressor 9 blood pressure lowering work done afterwards；The low temperature of decompressor 9 discharge Thermal medium flows through vaporizer 4 heat release, enters the second decompressor 10 blood pressure lowering work done afterwards and externally discharges；Decompressor 9 and The merit of two decompressor 10 outputs is supplied to compressor 8 and the second compressor 12 is used as power, and forms first kind thermal drivers compression-suction Receipts formula heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Fig. 3 is achieved in that
(1), in structure, it is mainly handed over by absorber, generator, condenser, vaporizer, choke valve, solution pump, solution heat Parallel operation, compressor, decompressor, the second decompressor, high-temperature heat exchanger, the second high-temperature heat exchanger and the 3rd decompressor institute Composition；Absorber 1 has weak solution pipeline to connect with generator 2 with solution heat exchanger 7 through solution pump 6, and generator 2 is also Having concentrated solution pipeline to connect with absorber 1 through solution heat exchanger 7, generator 2 also has refrigerant steam channel and condenser 3 Connection, condenser 3 also cryogen liquid pipeline connects with vaporizer 4 through choke valve 5, and vaporizer 4 also has refrigerant steam channel Connecting with absorber 1, outside has low-temperature heat medium passage to connect with compressor 8, and compressor 8 also has low-temperature heat medium passage Connecting with the 3rd decompressor 14 through high-temperature heat exchanger 11, the 3rd decompressor 14 also has low-temperature heat medium passage through the second high temperature Heat exchanger 13 connects with decompressor 9, and decompressor 9 also has low-temperature heat medium passage through vaporizer 4 and the second decompressor 10 Connection, the second decompressor 10 also has low-temperature heat medium passage and ft connection, generator 2, high-temperature heat exchanger 11 and second High-temperature heat exchanger 13 has high temperature thermal medium passage and ft connection, absorber 1 and condenser 3 to have the most respectively to be added the most respectively Hot media channel and ft connection, decompressor the 9, second decompressor 10 and the 3rd decompressor 14 connect compressor 8 and transmit dynamic Power.
(2), in flow process, the weak solution of absorber 1 enters generator 2, high temperature thermal medium through solution pump 6 and solution heat exchanger 7 Flow through generator 2, heating enters its interior solution release refrigerant vapour and provides to condenser 3, the concentrated solution warp of generator 2 Solution heat exchanger 7 enters absorber 1, absorbs refrigerant vapour heat release in heated medium；The refrigerant vapour of condenser 3 is put Heat becomes cryogen liquid in heated medium, and the cryogen liquid stream of condenser 3 enters vaporizer 4 through choke valve 5 throttling, vaporizer 4 Cryogen liquid absorbs heat into refrigerant vapour and provides to absorber 1；Outer low temperature thermal medium enters compressor 8 boosting and heats up, and flows through High-temperature heat exchanger 11 also absorbs heat, and enters the 3rd decompressor 14 blood pressure lowering work done afterwards；The Low Temperature Thermal of the 3rd decompressor 14 discharge Medium flows through the second high-temperature heat exchanger 13 and absorbs heat, and enters decompressor 9 blood pressure lowering work done afterwards；The low temperature of decompressor 9 discharge Thermal medium flows through vaporizer 4 heat release, enters decompressor 10 blood pressure lowering work done afterwards and externally discharges；Decompressor 9, second is swollen The merit of swollen machine 10 and the output of the 3rd decompressor 14 is supplied to compressor 8 and is used as power, and forms first kind thermal drivers compressing-absorbing type Heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Fig. 4 is achieved in that
(1), in structure, it is mainly handed over by absorber, generator, condenser, vaporizer, choke valve, solution pump, solution heat Parallel operation, compressor, decompressor, the second decompressor, high-temperature heat exchanger and the second compressor are formed；Absorber 1 has dilute Solution line connects with generator 2 with solution heat exchanger 7 through solution pump 6, and generator 2 also has concentrated solution pipeline through solution Heat exchanger 7 connects with absorber 1, and generator 2 also refrigerant steam channel connects with condenser 3, and condenser 3 also has Cryogen liquid pipeline connects with vaporizer 4 through choke valve 5, and vaporizer 4 also refrigerant steam channel connects with absorber 1, outward Portion has low-temperature heat medium passage to connect with compressor 8, compressor 8 also have low-temperature heat medium passage through high-temperature heat exchanger 11 with Decompressor 9 connects, and decompressor 9 also low-temperature heat medium passage connects with the second compressor 12 through vaporizer 4, the second compression Machine 12 also low-temperature heat medium passage connects with the second decompressor 10 through vaporizer 4, and the second decompressor 10 also has Low Temperature Thermal to be situated between Matter passage and ft connection, generator 2 and high-temperature heat exchanger 11 have high temperature thermal medium passage and ft connection the most respectively, inhale Receive device 1 and condenser 3 has heated medium passage and ft connection, decompressor 9 and the second decompressor 10 to connect pressure the most respectively Contracting machine 8 and the second compressor 12 also transmit power.
(2), in flow process, the weak solution of absorber 1 enters generator 2, high temperature thermal medium through solution pump 6 and solution heat exchanger 7 Flow through generator 2, heating enters its interior solution release refrigerant vapour and provides to condenser 3, the concentrated solution warp of generator 2 Solution heat exchanger 7 enters absorber 1, absorbs refrigerant vapour heat release in heated medium；The refrigerant vapour of condenser 3 is put Heat becomes cryogen liquid in heated medium, and the cryogen liquid stream of condenser 3 enters vaporizer 4 through choke valve 5 throttling, vaporizer 4 Cryogen liquid absorbs heat into refrigerant vapour and provides to absorber 1；Outer low temperature thermal medium enters compressor 8 boosting and heats up, and flows through High-temperature heat exchanger 11 also absorbs heat, and enters decompressor 9 blood pressure lowering work done afterwards；The low-temperature heat medium of decompressor 9 discharge flows through steaming Send out device 4 heat release, enter the second compressor 12 boosting afterwards and heat up；The low-temperature heat medium of the second compressor 12 discharge flows through Vaporizer 4 heat release, enter the second decompressor 10 blood pressure lowering work done afterwards and externally discharge；Decompressor 9 and the second decompressor 10 The merit of output is supplied to compressor 8 and the second compressor 12 is used as power, and forms first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Fig. 5 is achieved in that
(1), in structure, it is mainly handed over by absorber, generator, condenser, vaporizer, choke valve, solution pump, solution heat Parallel operation, compressor, decompressor, the second decompressor, high-temperature heat exchanger and regenerator are formed；Absorber 1 has weak solution Pipeline connects with generator 2 with solution heat exchanger 7 through solution pump 6, and generator 2 also has concentrated solution pipeline to hand over through solution heat Parallel operation 7 connects with absorber 1, and generator 2 also refrigerant steam channel connects with condenser 3, and condenser 3 also has cryogen Liquid pipeline connects with vaporizer 4 through choke valve 5, and vaporizer 4 also refrigerant steam channel connects with absorber 1, and outside has Low-temperature heat medium passage connects with compressor 8, and compressor 8 also has low-temperature heat medium passage to exchange through regenerator 15 and high-temperature hot Device 11 connects with decompressor 9, and decompressor 9 also has low-temperature heat medium passage to expand through regenerator 15 and vaporizer 4 and second Machine 10 connects, and the second decompressor 10 also has low-temperature heat medium passage and ft connection, generator 2 and high-temperature heat exchanger 11 High temperature thermal medium passage and ft connection, absorber 1 and condenser 3 is had to have heated medium passage the most respectively with outer the most respectively Portion connects, and decompressor 9 and the second decompressor 10 connect compressor 8 and transmit power.
(2), in flow process, the weak solution of absorber 1 enters generator 2, high temperature thermal medium through solution pump 6 and solution heat exchanger 7 Flow through generator 2, heating enters its interior solution release refrigerant vapour and provides to condenser 3, the concentrated solution warp of generator 2 Solution heat exchanger 7 enters absorber 1, absorbs refrigerant vapour heat release in heated medium；The refrigerant vapour of condenser 3 is put Heat becomes cryogen liquid in heated medium, and the cryogen liquid stream of condenser 3 enters vaporizer 4 through choke valve 5 throttling, vaporizer 4 Cryogen liquid absorbs heat into refrigerant vapour and provides to absorber 1；Outer low temperature thermal medium enters compressor 8 boosting and heats up, successively Flow through regenerator 15 and high-temperature heat exchanger 11 and progressively absorb heat, entering decompressor 9 blood pressure lowering work done afterwards；Decompressor 9 row The low-temperature heat medium put flows through regenerator 15 and vaporizer 4 progressively heat release successively, enters the second decompressor 10 blood pressure lowering afterwards Work done is also externally discharged；The merit of decompressor 9 and the output of the second decompressor 10 is supplied to compressor 8 and is used as power, and forms the first kind Thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Fig. 6 is achieved in that
(1), in structure, it is mainly handed over by absorber, generator, condenser, vaporizer, choke valve, solution pump, solution heat Parallel operation, compressor, decompressor, the second decompressor, high-temperature heat exchanger and regenerator are formed；Absorber 1 has weak solution Pipeline connects with generator 2 with solution heat exchanger 7 through solution pump 6, and generator 2 also has concentrated solution pipeline to hand over through solution heat Parallel operation 7 connects with absorber 1, and generator 2 also refrigerant steam channel connects with condenser 3, and condenser 3 also has cryogen Liquid pipeline connects with vaporizer 4 through choke valve 5, and vaporizer 4 also refrigerant steam channel connects with absorber 1, and outside has Low-temperature heat medium passage connects with compressor 8 through regenerator 15, and compressor 8 also has low-temperature heat medium passage to exchange through high-temperature hot Device 11 connects with decompressor 9, and decompressor 9 also has low-temperature heat medium passage to expand through vaporizer 4 and regenerator 15 and second Machine 10 connects, and the second decompressor 10 also has low-temperature heat medium passage and ft connection, generator 2 and high-temperature heat exchanger 11 High temperature thermal medium passage and ft connection, absorber 1 and condenser 3 is had to have heated medium passage the most respectively with outer the most respectively Portion connects, and decompressor 9 and the second decompressor 10 connect compressor 8 and transmit power.
(2), in flow process, the weak solution of absorber 1 enters generator 2, high temperature thermal medium through solution pump 6 and solution heat exchanger 7 Flow through generator 2, heating enters its interior solution release refrigerant vapour and provides to condenser 3, the concentrated solution warp of generator 2 Solution heat exchanger 7 enters absorber 1, absorbs refrigerant vapour heat release in heated medium；The refrigerant vapour of condenser 3 is put Heat becomes cryogen liquid in heated medium, and the cryogen liquid stream of condenser 3 enters vaporizer 4 through choke valve 5 throttling, vaporizer 4 Cryogen liquid absorbs heat into refrigerant vapour and provides to absorber 1；Outer low temperature thermal medium flows through regenerator 15 and absorbs heat, laggard Enter compressor 8 boosting to heat up；The low-temperature heat medium of compressor 8 discharge flows through high-temperature heat exchanger 11 and absorbs heat, and enters afterwards Decompressor 9 blood pressure lowering work done；The low-temperature heat medium of decompressor 9 discharge flows through vaporizer 4 and regenerator 15 progressively heat release successively, Enter the second decompressor 10 blood pressure lowering work done afterwards and externally discharge；The merit of decompressor 9 and the output of the second decompressor 10 is supplied to Compressor 8 is used as power, and forms first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Fig. 7 is achieved in that
(1) in structure, in the compressing-absorbing type heat pump of first kind thermal drivers shown in Fig. 1, the second generator, the second throttling are increased Valve, the second solution pump and the second solution heat exchanger, it is molten through the second solution pump 18 and second that absorber 1 sets up weak solution pipeline Liquid heat exchanger 19 connects with the second generator 16, and the second generator 16 also has concentrated solution pipeline through the second solution heat exchanger 19 connect with absorber 1, generator 2 has refrigerant steam channel connect with condenser 3 and is adjusted to generator 2 and has cryogen to steam After vapour passage and the connection of the second generator 16, the second generator 16 has cryogen liquid pipeline again through second throttle 17 and condenser 3 connections, the second generator 16 also refrigerant steam channel connects with condenser 4.
(2), in flow process, the refrigerant vapour that generator 2 produces is supplied to the second generator 16 and makees to drive thermal medium, absorber 1 Part weak solution enters the second generator 16 through the second solution pump 18 and the second solution heat exchanger 19, and refrigerant vapour flows through Two generators 16, heating enter its interior solution release refrigerant vapour and also provide to condenser 3, the second generator 16 dense molten Liquid enters absorber 1 through the second solution heat exchanger 19, flows through after the refrigerant vapour heat release of the second generator 16 becomes cryogen liquid Enter condenser 3 through second throttle 17 throttling, form first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Fig. 8 is achieved in that
(1) in structure, in the compressing-absorbing type heat pump of first kind thermal drivers shown in Fig. 1, the second generator, the second throttling are increased Valve and the second solution heat exchanger, have weak solution pipeline through solution pump 6 and solution heat exchanger 7 and generator 2 by absorber 1 Connection be adjusted to absorber 1 have weak solution pipeline through solution pump 6, solution heat exchanger 7 and the second solution heat exchanger 19 with Generator 2 connects, and generator 2 has concentrated solution pipeline connect with absorber 1 through solution heat exchanger 7 and is adjusted to generator 2 Having concentrated solution pipeline to connect with the second generator 16 through the second solution heat exchanger 19, the second generator 16 has concentrated solution pipe again Road connects with absorber 1 through solution heat exchanger 7, generator 2 has refrigerant steam channel connect with condenser 3 and is adjusted to After generator 2 has refrigerant steam channel to connect with the second generator 16, the second generator 16 has cryogen liquid pipeline again through second Choke valve 17 connects with condenser 3, and the second generator 16 also refrigerant steam channel connects with condenser 3.
(2), in flow process, the refrigerant vapour that generator 2 produces is supplied to the second generator 16 and makees to drive thermal medium, absorber 1 Weak solution enters generator 2 through solution pump 6, solution heat exchanger 7 and the second solution heat exchanger 19, generator 2 dense Solution enters the second generator 16 through the second solution heat exchanger 19, and refrigerant vapour flows through the second generator 16, heating enters Its interior solution release refrigerant vapour also provides to condenser 3, and the concentrated solution of the second generator 16 is entered through solution heat exchanger 7 Enter absorber 1, flow through after the refrigerant vapour heat release of the second generator 16 becomes cryogen liquid and enter cold through second throttle 17 throttling Condenser 3, forms first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Fig. 9 is achieved in that
(1) in structure, in the compressing-absorbing type heat pump of first kind thermal drivers shown in Fig. 1, the second generator, the second throttling are increased Valve, the second solution pump and the second solution heat exchanger, have weak solution pipeline through solution pump 6 and solution heat exchange by absorber 1 Device 7 connects with generator 2 and is adjusted to absorber 1 and has weak solution pipeline through solution pump 6 and solution heat exchanger 7 and second Raw device 16 connects, the second generator 16 have again concentrated solution pipeline through the second solution pump 18 and the second solution heat exchanger 19 with Generator 2 connects, and generator 2 has concentrated solution pipeline connect with absorber 1 through solution heat exchanger 7 and is adjusted to generator 2 There is concentrated solution pipeline to connect with absorber 1 with solution heat exchanger 7 through the second solution heat exchanger 19, generator 2 is had cold Agent steam channel connects with condenser 3 and is adjusted to after generator 2 has refrigerant steam channel to connect with the second generator 16 second Generator 16 has cryogen liquid pipeline to connect with condenser 3 through second throttle 17 again, and the second generator 16 also has refrigerant vapour Passage connects with condenser 3.
(2), in flow process, the refrigerant vapour that generator 2 produces is supplied to the second generator 16 and makees to drive thermal medium, absorber 1 Weak solution enters the second generator 16 through solution pump 6 and solution heat exchanger 7, and refrigerant vapour flows through the second generator 16, adds Heat enters its interior solution release refrigerant vapour and provides to condenser 3, and the concentrated solution of the second generator 16 is through the second solution pump 18 and second solution heat exchanger 19 enter generator 2, the concentrated solution of generator 2 is through the second solution heat exchanger 19 and molten Liquid heat exchanger 7 enters absorber 1, flows through the refrigerant vapour heat release of the second generator 16 and becomes after cryogen liquid through second section stream Valve 17 throttling enters condenser 3, forms first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Figure 10 is achieved in that
(1) in structure, in the compressing-absorbing type heat pump of first kind thermal drivers shown in Fig. 1, the second generator, the second absorption are increased Device, the second solution pump and the second solution heat exchanger, have weak solution pipeline through solution pump 6 and solution heat exchange by absorber 1 Device 7 connects with generator 2 and is adjusted to absorber 1 and has weak solution pipeline to inhale through solution pump 6 and solution heat exchanger 7 and second Receive device 20 to connect, the second absorber 20 have again weak solution pipeline through the second solution pump 18 and the second solution heat exchanger 19 with Generator 2 connects, and generator 2 has concentrated solution pipeline connect with absorber 1 through solution heat exchanger 7 and is adjusted to generator 2 Having concentrated solution pipeline to connect with the second generator 16 through the second solution heat exchanger 19, the second generator 16 has concentrated solution pipe again Road connects with absorber 1 through solution heat exchanger 7, and the second generator 16 also has refrigerant steam channel and the second absorber 20 Connection, the second generator 16 also has high temperature thermal medium passage and ft connection, the second absorber 20 to also have heated medium to lead to Road and ft connection.
(2), in flow process, the weak solution of absorber 1 enters the second absorber 20 through solution pump 6 and solution heat exchanger 7, absorbs Refrigerant vapour heat release are handed over through the second solution pump 18 and the second solution heat in heated medium, the weak solution of the second absorber 20 Parallel operation 19 enters generator 2, and the concentrated solution of generator 2 enters the second generator 16 through the second solution heat exchanger 19, high Warm flows through the second generator 16, heating enters its interior solution release refrigerant vapour and provides to the second absorber 20, The concentrated solution of the second generator 16 enters absorber 1 through solution heat exchanger 7, forms first kind thermal drivers compressing-absorbing type heat Pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Figure 11 is achieved in that
(1) in structure, in the compressing-absorbing type heat pump of first kind thermal drivers shown in Figure 10, the 3rd generator, second section are increased Stream valve, the 3rd solution pump and the 3rd solution heat exchanger, the second absorber 20 sets up weak solution pipeline through the 3rd solution pump 22 Connecting with the 3rd generator 21 with the 3rd solution heat exchanger 23, the 3rd generator 21 also has concentrated solution pipeline through the 3rd solution Heat exchanger 23 connects with the second generator 16, generator 2 is had refrigerant steam channel connect with condenser 3 be adjusted to send out After raw device 2 has refrigerant steam channel to connect with the 3rd generator 21, the 3rd generator 21 has cryogen liquid pipeline again through second section Stream valve 17 connects with condenser 3, and the 3rd generator 21 also refrigerant steam channel connects with condenser 3.
(2), in flow process, the refrigerant vapour that generator 2 produces is supplied to the 3rd generator 21 and makees to drive thermal medium, the second absorber The part weak solution of 20 enters the 3rd generator 21, refrigerant vapour stream through the 3rd solution pump 22 and the 3rd solution heat exchanger 23 Enter its interior solution release refrigerant vapour through the 3rd generator 21, heating and provide to condenser 3, the 3rd generator 21 Concentrated solution enters the second generator 16 through the 3rd solution heat exchanger 23, and the refrigerant vapour heat release flowing through the 3rd generator 21 becomes Enter condenser 3 through second throttle 17 throttling after cryogen liquid, form first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Figure 12 is achieved in that
(1) in structure, in the compressing-absorbing type heat pump of first kind thermal drivers shown in Figure 10, the 3rd generator, second section are increased Stream valve and the 3rd solution heat exchanger, have weak solution pipeline through the second solution pump 18 and the second solution heat by the second absorber 20 Exchanger 19 connects with generator 2 and is adjusted to the second absorber 20 and has weak solution pipeline through second solution pump the 18, second solution Heat exchanger 19 connects with generator 2 with the 3rd solution heat exchanger 23, has concentrated solution pipeline molten through second in generator 2 Liquid heat exchanger 19 connects with the second generator 16 and is adjusted to generator 2 and has concentrated solution pipeline through the 3rd solution heat exchanger 23 Connecting with the 3rd generator 21, the 3rd generator 21 has concentrated solution pipeline to occur through the second solution heat exchanger 19 and second again Device 16 connects, generator 2 is had refrigerant steam channel connect with condenser 3 be adjusted to generator 2 have refrigerant steam channel with After 3rd generator 21 connection, the 3rd generator 21 has cryogen liquid pipeline to connect with condenser 3 through second throttle 17 again, 3rd generator 21 also refrigerant steam channel connects with condenser 3.
(2), in flow process, the refrigerant vapour that external high temperature thermal medium and generator 2 produce is supplied to the 3rd generator 21 and makees to drive heat Medium, the weak solution of the second absorber 20 is through the second solution pump the 18, second solution heat exchanger 19 and the 3rd solution heat exchange Device 23 enters generator 2, and the concentrated solution of generator 2 enters the 3rd generator 21, cryogen through the 3rd solution heat exchanger 23 Steam and high temperature thermal medium flow separately through the 3rd generator 21, heating enters its interior solution and discharges refrigerant vapour and to condenser 3 provide, and the concentrated solution of the 3rd generator 21 enters the second generator 16 through the second solution heat exchanger 19, flows through the 3rd The refrigerant vapour heat release of raw device 21 enters condenser 3 through second throttle 17 throttling after becoming cryogen liquid, forms first kind heat and drives Dynamic pressure contracting-absorption heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Figure 13 is achieved in that
(1) in structure, in the compressing-absorbing type heat pump of first kind thermal drivers shown in Figure 10, the 3rd generator, second section are increased Stream valve, the 3rd solution pump and the 3rd solution heat exchanger, have weak solution pipeline through the second solution pump 18 by the second absorber 20 Connect with generator 2 with the second solution heat exchanger 19 and be adjusted to the second absorber 20 and have weak solution pipeline through the second solution pump 18 connect with the 3rd generator 21 with the second solution heat exchanger 19, and the 3rd generator 21 has concentrated solution pipeline molten through the 3rd again Liquid pump 22 connects with generator 2 with the 3rd solution heat exchanger 23, generator 2 has concentrated solution pipeline through the second solution heat Exchanger 19 connects with the second generator 16 and is adjusted to generator 2 and has concentrated solution pipeline through the 3rd solution heat exchanger 23 and Two solution heat exchangers 19 connect with the second generator 16, have refrigerant steam channel to connect tune with condenser 3 in generator 2 Whole have refrigerant steam channel to connect with the 3rd generator 21 for generator 2 after the 3rd generator 21 have cryogen liquid pipeline warp again Second throttle 17 connects with condenser 3, and the 3rd generator 21 also refrigerant steam channel connects with condenser 3.
(2), in flow process, the refrigerant vapour that generator 2 produces is supplied to the 3rd generator 21 and makees to drive thermal medium, the second absorber The weak solution of 20 enters the 3rd generator 21 through the second solution pump 18 and the second solution heat exchanger 19, and refrigerant vapour flows through Three generators 21, heating enter its interior solution release refrigerant vapour and also provide to condenser 3, the 3rd generator 21 dense molten Liquid enters generator 2 through the 3rd solution pump 22 and the 3rd solution heat exchanger 23, and the concentrated solution of generator 2 is through the 3rd solution heat Exchanger 23 and the second solution heat exchanger 19 enter the second generator 16, flow through the refrigerant vapour heat release of the 3rd generator 21 Enter condenser 3 through second throttle 17 throttling after becoming cryogen liquid, form first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Figure 14 is achieved in that
(1) in structure, in the compressing-absorbing type heat pump of first kind thermal drivers shown in Fig. 1, newly-increased generator, newly-increased absorption are increased Device, new solubilization liquid pump and newly-increased solution heat exchanger, have refrigerant steam channel to connect with condenser (3) in generator (2) Being adjusted to generator (2) has refrigerant steam channel to connect with newly-increased absorber (B), and newly-increased absorber (B) also has weak solution Pipeline connects with newly-increased generator (A) with newly-increased solution heat exchanger (D) through new solubilization liquid pump (C), newly-increased generator (A) Also having concentrated solution pipeline to connect with newly-increased absorber (B) through newly-increased solution heat exchanger (D), newly-increased generator (A) also has Refrigerant steam channel connects with condenser (3), and newly-increased generator (A) also has high temperature thermal medium passage and ft connection, newly Increase absorber (B) and also have heated medium passage and ft connection.
(2), in flow process, the refrigerant vapour that generator 2 produces enters newly-increased absorber B, and the weak solution of newly-increased absorber B is through newly-increased Solution pump C and newly-increased solution heat exchanger D enter newly-increased generator A, high temperature thermal medium flow through newly-increased generator A, heat into Entering its interior solution release refrigerant vapour and provide to condenser 3, the concentrated solution of newly-increased generator A is through new solubilization liquid heat exchange Device D enters newly-increased absorber B, absorbs refrigerant vapour heat release in heated medium, formation first kind thermal drivers compression-absorb Formula heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Figure 15 is achieved in that
In the compressing-absorbing type heat pump of first kind thermal drivers shown in Fig. 1, increasing engine, engine 24 connects compressor 8 And transmit power to compressor 8, form additional external power-actuated first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Figure 16 is achieved in that
In the compressing-absorbing type heat pump of first kind thermal drivers shown in Fig. 1, increasing working machine, decompressor 9 connects working machine 25 And transmit power to working machine 25, form the additional first kind thermal drivers compressing-absorbing type heat pump that living load is externally provided.
The first kind 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) new approaches and new technique that the temperature difference utilizes are proposed.
(2) heat energy (temperature difference) drives, it is achieved heat supply/refrigeration, or externally provides power while of optional.
(3) flow process is reasonable, and performance index is variable and corresponding with thermodynamic parameter change, it is possible to realize filling of heat energy (temperature difference) Divide and efficiently utilize.
(4) if desired, realizing heat supply/refrigeration by external impetus, mode is flexible, and adaptability is good.
(5) heat supply temperature can be improved by a relatively large margin, compensate for the deficiency of absorption heat pump technology, and avoid driving thermal medium ginseng Number and conflicting between solution property.
(6) as heat pump, it is possible to directly utilize surrounding air as low-temperature heat source, and not by temperature limiting；Solve absorption Heat pump is about the source of low-temperature heat source and a temperature limiting difficult problem.
(7) rely primarily on latent heat and realize acquisition and the release of thermic load, overcome the deficiency of gas compression formula heat pump techniques.
(8) multiple concrete technical scheme is provided, it is possible to tackle numerous different actual state, have the wider scope of application.
(9) extend heat pump techniques, enrich the type of compression heat pump, be conducive to being better achieved the efficient utilization of heat energy.

Claims (18)

1. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, vaporizer, choke valve, Solution pump, solution heat exchanger, compressor, decompressor, the second decompressor and high-temperature heat exchanger are formed；Absorber (1) Having weak solution pipeline to connect with generator (2) with solution heat exchanger (7) through solution pump (6), generator (2) is the denseest Solution line connects with absorber (1) through solution heat exchanger (7), and generator (2) also has refrigerant steam channel and condenser (3) connection, condenser (3) also has cryogen liquid pipeline to connect with vaporizer (4) through choke valve (5), and vaporizer (4) is also Having refrigerant steam channel to connect with absorber (1), outside has low-temperature heat medium passage to connect with compressor (8), compressor (8) Also having low-temperature heat medium passage to connect with decompressor (9) through high-temperature heat exchanger (11), decompressor (9) also has Low Temperature Thermal to be situated between Matter passage connects with the second decompressor (10) through vaporizer (4), and the second decompressor (10) also has low-temperature heat medium passage with outer Portion connects, and generator (2) and high-temperature heat exchanger (11) have high temperature thermal medium passage and ft connection, absorber (1) the most respectively Heated medium passage and ft connection, decompressor (9) and the second decompressor (10) is had to connect the most respectively with condenser (3) Compressor (8) also transmits power, forms first kind thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor (9) and second Decompressor (10) connects compressor (8) and solution pump (6) and transmits power.
2. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, vaporizer, choke valve, Solution pump, solution heat exchanger, compressor, decompressor, the second decompressor, high-temperature heat exchanger, the second compressor and second High-temperature heat exchanger is formed；Absorber (1) has weak solution pipeline through solution pump (6) and solution heat exchanger (7) and to occur Device (2) connects, and generator (2) also has concentrated solution pipeline to connect with absorber (1) through solution heat exchanger (7), occurs Device (2) also has refrigerant steam channel to connect with condenser (3), and condenser (3) also has cryogen liquid pipeline through choke valve (5) Connecting with vaporizer (4), vaporizer (4) also has refrigerant steam channel to connect with absorber (1), and there is low-temperature heat medium outside Passage connects with compressor (8), and compressor (8) also has low-temperature heat medium passage through high-temperature heat exchanger (11) and the second pressure Contracting machine (12) connects, and the second compressor (12) also has low-temperature heat medium passage through the second high-temperature heat exchanger (13) and expansion Machine (9) connects, and decompressor (9) also has low-temperature heat medium passage to connect with the second decompressor (10) through vaporizer (4), the Two decompressors (10) also have low-temperature heat medium passage and ft connection, generator (2), high-temperature heat exchanger (11) and second High-temperature heat exchanger (13) has high temperature thermal medium passage and ft connection, absorber (1) and condenser (3) also to divide the most respectively Heated medium passage and ft connection, decompressor (9) and the second decompressor (10) is not had to connect compressor (8) and second Compressor (12) also transmits power, forms first kind thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor (9) and Two decompressors (10) connect compressor (8), the second compressor (12) and solution pump (6) and transmit power.
3. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, vaporizer, choke valve, Solution pump, solution heat exchanger, compressor, decompressor, the second decompressor, high-temperature heat exchanger, the second high-temperature heat exchanger Formed with the 3rd decompressor；Absorber (1) has weak solution pipeline through solution pump (6) and solution heat exchanger (7) and to occur Device (2) connects, and generator (2) also has concentrated solution pipeline to connect with absorber (1) through solution heat exchanger (7), occurs Device (2) also has refrigerant steam channel to connect with condenser (3), and condenser (3) also has cryogen liquid pipeline through choke valve (5) Connecting with vaporizer (4), vaporizer (4) also has refrigerant steam channel to connect with absorber (1), and there is low-temperature heat medium outside Passage connects with compressor (8), and compressor (8) also has low-temperature heat medium passage swollen with the 3rd through high-temperature heat exchanger (11) Swollen machine (14) connects, and the 3rd decompressor (14) also has low-temperature heat medium passage through the second high-temperature heat exchanger (13) and expansion Machine (9) connects, and decompressor (9) also has low-temperature heat medium passage to connect with the second decompressor (10) through vaporizer (4), the Two decompressors (10) also have low-temperature heat medium passage and ft connection, generator (2), high-temperature heat exchanger (11) and second High-temperature heat exchanger (13) has high temperature thermal medium passage and ft connection, absorber (1) and condenser (3) also to divide the most respectively Heated medium passage and ft connection, decompressor (9), the second decompressor (10) and the 3rd decompressor (14) is not had to connect Compressor (8) also transmits power, forms first kind thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor (9), second Decompressor (10) and the 3rd decompressor (14) connect compressor (8) and solution pump (6) and transmit power.
4. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, vaporizer, choke valve, Solution pump, solution heat exchanger, compressor, decompressor, the second decompressor, high-temperature heat exchanger and the second compressor are formed； Absorber (1) has weak solution pipeline to connect with generator (2) with solution heat exchanger (7) through solution pump (6), generator (2) also having concentrated solution pipeline to connect with absorber (1) through solution heat exchanger (7), generator (2) also has refrigerant vapour Passage connects with condenser (3), and condenser (3) also has cryogen liquid pipeline to connect with vaporizer (4) through choke valve (5), Vaporizer (4) also has refrigerant steam channel to connect with absorber (1), and outside has low-temperature heat medium passage with compressor (8) even Logical, compressor (8) also has low-temperature heat medium passage to connect with decompressor (9) through high-temperature heat exchanger (11), decompressor (9) Also having low-temperature heat medium passage to connect with the second compressor (12) through vaporizer (4), the second compressor (12) also has Low Temperature Thermal Medium channel connects with the second decompressor (10) through vaporizer (4), the second decompressor (10) also have low-temperature heat medium passage with Ft connection, generator (2) and high-temperature heat exchanger (11) have high temperature thermal medium passage and ft connection, absorber the most respectively And condenser (3) has heated medium passage and ft connection, decompressor (9) and the second decompressor (10) the most respectively (1) Connect compressor (8) and the second compressor (12) and transmit power, forming first kind thermal drivers compressing-absorbing type heat pump；Its In, or decompressor (9) and the second decompressor (10) connect compressor (8), the second compressor (12) and solution pump (6) And transmit power.
5. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, vaporizer, choke valve, Solution pump, solution heat exchanger, compressor, decompressor, the second decompressor, high-temperature heat exchanger and regenerator are formed；Inhale Receiving device (1) has weak solution pipeline to connect with generator (2) with solution heat exchanger (7) through solution pump (6), generator (2) Also have concentrated solution pipeline connect with absorber (1) through solution heat exchanger (7), generator (2) also refrigerant steam channel and Condenser (3) connects, and condenser (3) also has cryogen liquid pipeline to connect with vaporizer (4) through choke valve (5), vaporizer (4) also having refrigerant steam channel to connect with absorber (1), outside has low-temperature heat medium passage to connect with compressor (8), pressure Contracting machine (8) also has low-temperature heat medium passage to connect with decompressor (9) with high-temperature heat exchanger (11) through regenerator (15), Decompressor (9) also has low-temperature heat medium passage to connect with the second decompressor (10) with vaporizer (4) through regenerator (15), Second decompressor (10) also has low-temperature heat medium passage and ft connection, and generator (2) and high-temperature heat exchanger (11) also divide High temperature thermal medium passage and ft connection, absorber (1) and condenser (3) is not had to have heated medium passage the most respectively with outer Portion connects, and decompressor (9) and the second decompressor (10) connect compressor (8) and transmit power, form first kind thermal drivers Compressing-absorbing type heat pump；Wherein, or decompressor (9) and the second decompressor (10) connect compressor (8) and solution pump (6) And transmit power.
6. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, vaporizer, choke valve, Solution pump, solution heat exchanger, compressor, decompressor, the second decompressor, high-temperature heat exchanger and regenerator are formed；Inhale Receiving device (1) has weak solution pipeline to connect with generator (2) with solution heat exchanger (7) through solution pump (6), generator (2) Also have concentrated solution pipeline connect with absorber (1) through solution heat exchanger (7), generator (2) also refrigerant steam channel and Condenser (3) connects, and condenser (3) also has cryogen liquid pipeline to connect with vaporizer (4) through choke valve (5), vaporizer (4) also having refrigerant steam channel to connect with absorber (1), there is low-temperature heat medium passage outside through regenerator (15) and compression Machine (8) connects, and compressor (8) also has low-temperature heat medium passage to connect with decompressor (9) through high-temperature heat exchanger (11), Decompressor (9) also has low-temperature heat medium passage to connect with the second decompressor (10) with regenerator (15) through vaporizer (4), Second decompressor (10) also has low-temperature heat medium passage and ft connection, and generator (2) and high-temperature heat exchanger (11) also divide High temperature thermal medium passage and ft connection, absorber (1) and condenser (3) is not had to have heated medium passage the most respectively with outer Portion connects, and decompressor (9) and the second decompressor (10) connect compressor (8) and transmit power, form first kind thermal drivers Compressing-absorbing type heat pump；Wherein, or decompressor (9) and the second decompressor (10) connect compressor (8) and solution pump (6) And transmit power.
7. first kind thermal drivers compressing-absorbing type heat pump, is to compress at the arbitrary first kind thermal drivers described in claim 1-6-inhale Receipts formula heat pump, increases the second generator, second throttle, the second solution pump and the second solution heat exchanger, and absorber (1) increases If weak solution pipeline connects with the second generator (16) with the second solution heat exchanger (19) through the second solution pump (18), the Two generators (16) also have concentrated solution pipeline to connect with absorber (1) through the second solution heat exchanger (19), by generator (2) Have refrigerant steam channel to connect with condenser (3) to be adjusted to generator (2) and have refrigerant steam channel and the second generator (16) After connection, the second generator (16) has cryogen liquid pipeline to connect with condenser (3) through second throttle (17) again, second Raw device (16) also has refrigerant steam channel to connect with condenser (4), forms first kind thermal drivers compressing-absorbing type heat pump.
8. first kind thermal drivers compressing-absorbing type heat pump, is to compress at the arbitrary first kind thermal drivers described in claim 1-6-inhale Receipts formula heat pump, increases the second generator, second throttle and the second solution heat exchanger, and absorber (1) is had weak solution pipeline Connect with generator (2) through solution pump (6) and solution heat exchanger (7) and be adjusted to absorber (1) and have weak solution pipeline warp Solution pump (6), solution heat exchanger (7) connect, by generator with generator (2) with the second solution heat exchanger (19) (2) have concentrated solution pipeline to connect with absorber (1) through solution heat exchanger (7) to be adjusted to generator (2) and have concentrated solution pipe Road the second solution heat exchanger (19) connects with the second generator (16), and the second generator (16) has concentrated solution pipeline again Connect with absorber (1) through solution heat exchanger (7), generator (2) has refrigerant steam channel with condenser (3) even Logical it be adjusted to the second generator (16) after generator (2) has refrigerant steam channel to connect with the second generator (16) and have cold again Agent liquid pipeline connects with condenser (3) through second throttle (17), and the second generator (16) also has refrigerant steam channel with cold Condenser (3) connects, and forms first kind thermal drivers compressing-absorbing type heat pump.
9. first kind thermal drivers compressing-absorbing type heat pump, is to compress at the arbitrary first kind thermal drivers described in claim 1-6-inhale Receipts formula heat pump, increases the second generator, second throttle, the second solution pump and the second solution heat exchanger, by absorber (1) Have weak solution pipeline to connect with generator (2) through solution pump (6) and solution heat exchanger (7) to be adjusted to absorber (1) and have Weak solution pipeline connects with the second generator (16) with solution heat exchanger (7) through solution pump (6), the second generator (16) There is concentrated solution pipeline to connect with generator (2) with the second solution heat exchanger (19) through the second solution pump (18) again, will occur Device (2) has concentrated solution pipeline to connect with absorber (1) through solution heat exchanger (7) to be adjusted to generator (2) and have concentrated solution Pipeline connects with absorber (1) with solution heat exchanger (7) through the second solution heat exchanger (19), is had by generator (2) Refrigerant steam channel connects with condenser (3) and is adjusted to generator (2) and has refrigerant steam channel and the second generator (16) even After Tong, the second generator (16) has cryogen liquid pipeline to connect with condenser (3) through second throttle (17) again, and second occurs Device (16) also has refrigerant steam channel to connect with condenser (3), forms first kind thermal drivers compressing-absorbing type heat pump.
10. first kind thermal drivers compressing-absorbing type heat pump, is in arbitrary first kind thermal drivers compression-suction described in claim 1-6 Receipts formula heat pump, increases the second generator, the second absorber, the second solution pump and the second solution heat exchanger, by absorber (1) Have weak solution pipeline to connect with generator (2) through solution pump (6) and solution heat exchanger (7) to be adjusted to absorber (1) and have Weak solution pipeline connects with the second absorber (20) with solution heat exchanger (7) through solution pump (6), the second absorber (20) There is weak solution pipeline to connect with generator (2) with the second solution heat exchanger (19) through the second solution pump (18) again, will occur Device (2) has concentrated solution pipeline to connect with absorber (1) through solution heat exchanger (7) to be adjusted to generator (2) and have concentrated solution Pipeline connects with the second generator (16) through the second solution heat exchanger (19), and the second generator (16) has concentrated solution pipe again Road connects with absorber (1) through solution heat exchanger (7), and the second generator (16) also has refrigerant steam channel to inhale with second Receiving device (20) connection, the second generator (16) also has high temperature thermal medium passage and ft connection, and the second absorber (20) is also There are heated medium passage and ft connection, form first kind thermal drivers compressing-absorbing type heat pump.
11. first kind thermal drivers compressing-absorbing type heat pumps, are in arbitrary first kind thermal drivers compression-absorption described in claim 10 Formula heat pump, increases the 3rd generator, second throttle, the 3rd solution pump and the 3rd solution heat exchanger, the second absorber (20) Set up weak solution pipeline to connect with the 3rd generator (21) with the 3rd solution heat exchanger (23) through the 3rd solution pump (22), 3rd generator (21) also has concentrated solution pipeline to connect with the second generator (16) through the 3rd solution heat exchanger (23), will Generator (2) have refrigerant steam channel connect with condenser (3) be adjusted to generator (2) have refrigerant steam channel with the 3rd After raw device (21) connection, the 3rd generator (21) has cryogen liquid pipeline through second throttle (17) with condenser (3) even again Logical, the 3rd generator (21) also has refrigerant steam channel to connect with condenser (3), forms first kind thermal drivers compression-absorption Formula heat pump.
12. first kind thermal drivers compressing-absorbing type heat pumps, are in arbitrary first kind thermal drivers compression-absorption described in claim 10 Formula heat pump, increases the 3rd generator, second throttle and the 3rd solution heat exchanger, the second absorber (20) is had weak solution Pipeline connects with generator (2) through the second solution pump (18) and the second solution heat exchanger (19) and is adjusted to the second absorber (20) Weak solution pipeline is had through the second solution pump (18), the second solution heat exchanger (19) and the 3rd solution heat exchanger (23) and to send out Raw device (2) connection, has concentrated solution pipeline through the second solution heat exchanger (19) and the second generator (16) by generator (2) Connection is adjusted to generator (2) has concentrated solution pipeline to connect with the 3rd generator (21) through the 3rd solution heat exchanger (23), 3rd generator (21) has concentrated solution pipeline to connect with the second generator (16) through the second solution heat exchanger (19) again, will Generator (2) have refrigerant steam channel connect with condenser (3) be adjusted to generator (2) have refrigerant steam channel with the 3rd After raw device (21) connection, the 3rd generator (21) has cryogen liquid pipeline through second throttle (17) with condenser (3) even again Logical, the 3rd generator (21) also has refrigerant steam channel to connect with condenser (3), forms first kind thermal drivers compression-absorption Formula heat pump.
13. first kind thermal drivers compressing-absorbing type heat pumps, are in arbitrary first kind thermal drivers compression-absorption described in claim 10 Formula heat pump, increases the 3rd generator, second throttle, the 3rd solution pump and the 3rd solution heat exchanger, by the second absorber (20) There is weak solution pipeline to connect with generator (2) through the second solution pump (18) and the second solution heat exchanger (19) and be adjusted to second Absorber (20) has weak solution pipeline through the second solution pump (18) and the second solution heat exchanger (19) and the 3rd generator (21) Connection, the 3rd generator (21) have concentrated solution pipeline through the 3rd solution pump (22) and the 3rd solution heat exchanger (23) again and Generator (2) connects, and generator (2) has concentrated solution pipeline through the second solution heat exchanger (19) and the second generator (16) Connection is adjusted to generator (2) has concentrated solution pipeline through the 3rd solution heat exchanger (23) and the second solution heat exchanger (19) Connect with the second generator (16), generator (2) has refrigerant steam channel connect with condenser (3) and is adjusted to generator (2) after having refrigerant steam channel to connect with the 3rd generator (21), the 3rd generator (21) has cryogen liquid pipeline again through second Choke valve (17) connects with condenser (3), and the 3rd generator (21) also has refrigerant steam channel to connect with condenser (3), Form first kind thermal drivers compressing-absorbing type heat pump.
14. first kind thermal drivers compressing-absorbing type heat pumps, are in claim 1-6, arbitrary first kind thermal drivers pressure described in 10 In contracting-absorption heat pump, increase newly-increased generator, newly-increased absorber, new solubilization liquid pump and newly-increased solution heat exchanger, will occur Device (2) has refrigerant steam channel to connect with condenser (3) to be adjusted to generator (2) and have refrigerant steam channel and newly-increased absorber (B) connection, newly-increased absorber (B) also has weak solution pipeline through new solubilization liquid pump (C) and newly-increased solution heat exchanger (D) Connecting with newly-increased generator (A), newly-increased generator (A) also has concentrated solution pipeline through newly-increased solution heat exchanger (D) with newly-increased Absorber (B) connects, and newly-increased generator (A) also has refrigerant steam channel to connect with condenser (3), newly-increased generator (A) Also have high temperature thermal medium passage and ft connection, newly-increased absorber (B) to also have heated medium passage and ft connection, form the One class thermal drivers compressing-absorbing type heat pump.
15. first kind thermal drivers compressing-absorbing type heat pumps, are in arbitrary first kind thermal drivers compression-suction described in claim 7-9 In receipts formula heat pump, the second generator (16) sets up high temperature thermal medium passage and ft connection, formed the compression of first kind thermal drivers- Absorption heat pump.
16. first kind thermal drivers compressing-absorbing type heat pumps, are in arbitrary first kind thermal drivers compression-suction described in claim 11-13 In receipts formula heat pump, the 3rd generator (21) sets up high temperature thermal medium passage and ft connection, formed the compression of first kind thermal drivers- Absorption heat pump.
17. first kind thermal drivers compressing-absorbing type heat pumps, are in arbitrary first kind thermal drivers compression-suction described in claim 1-16 In receipts formula heat pump, increasing engine, engine (24) connects compressor (8) and transmits power to compressor (8), is formed Additional external power-actuated first kind thermal drivers compressing-absorbing type heat pump.
18. first kind thermal drivers compressing-absorbing type heat pumps, are in arbitrary first kind thermal drivers compression-suction described in claim 1-16 In receipts formula heat pump, increasing working machine, decompressor (9) connects working machine (25) and transmits power to working machine (25), is formed The additional first kind thermal drivers compressing-absorbing type heat pump that living load is externally provided.
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CN107905857A (en) * 2016-10-12 2018-04-13 李华玉 Stage evaporation combined cycle Steam Power Equipment
CN108131866A (en) * 2016-11-24 2018-06-08 李华玉 First kind thermal drivers compression heat pump

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CN1804511A (en) * 2006-01-23 2006-07-19 李华玉 Compression-absorption combined heat pump heating system
CN103743150A (en) * 2013-12-17 2014-04-23 浙江理工大学 Absorption compression type automatic-overlapping refrigerating system and use method
CN104236160A (en) * 2013-06-13 2014-12-24 彭岫麟 Hybrid system combining cooling device and absorption heat pump

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CN1128856A (en) * 1994-09-27 1996-08-14 巴布考克及威尔考克斯公司 Ammonia absorption circulation used for combined circulation power apparatus
JP2000193341A (en) * 1998-12-25 2000-07-14 Takenaka Komuten Co Ltd Ice making system
CN1804511A (en) * 2006-01-23 2006-07-19 李华玉 Compression-absorption combined heat pump heating system
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CN107905857A (en) * 2016-10-12 2018-04-13 李华玉 Stage evaporation combined cycle Steam Power Equipment
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