CN106152599B - 4th class thermal drivers compressing-absorbing type heat pump - Google Patents
4th class thermal drivers compressing-absorbing type heat pump Download PDFInfo
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- CN106152599B CN106152599B CN201610415624.9A CN201610415624A CN106152599B CN 106152599 B CN106152599 B CN 106152599B CN 201610415624 A CN201610415624 A CN 201610415624A CN 106152599 B CN106152599 B CN 106152599B
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B25/00—Machines, plants or systems, using a combination of modes of operation covered by two or more of the groups F25B1/00 - F25B23/00
- F25B25/02—Compression-sorption machines, plants, or systems
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Abstract
The present invention provides the 4th class thermal drivers compressing-absorbing type heat pump, belongs to power, refrigeration and technical field of heat pumps.Absorber is connected to through solution pump and solution heat exchanger with generator, generator is connected to through solution heat exchanger with absorber, generator has refrigerant steam channel to be connected to condenser, and condenser is connected to through throttle valve with evaporator, and evaporator has refrigerant steam channel to be connected to absorber;Outside has low-temperature heat medium channel to be communicated with compressor, compressor has low-temperature heat medium channel to be connected to through condenser with expanding machine, expanding machine has low-temperature heat medium channel to be connected to through evaporator with the second expanding machine, second expanding machine has low-temperature heat medium channel to be connected to outside, generator has high temperature thermal medium channel, absorber and condenser to have heated medium channel to be connected to outside, expanding machine and the second expanding machine connect compressor simultaneously transmit power, form the 4th class thermal drivers compressing-absorbing type heat pump.
Description
Technical field:
The invention belongs to power, refrigeration and technical field of heat pumps.
Background technique:
Cold demand, heat demand and power demand, for human lives with production in it is common;In reality, people are often needed
Refrigeration, heat supply are realized using high temperature heat or is converted into power, it is also desirable to the power that freezes or utilize is carried out using power
And low temperature heat energy is combined to carry out heat supply.During stating purpose in realization, various considerations or condition limit will be faced
System --- type, grade and the quantity of the energy, type, grade and the quantity of user demand, environment temperature, the class of working media
Type, process, structure and manufacturing cost of equipment etc..
Using absorption heat pump technology as thermal energy (temperature difference) utilization technology of representative, is driven using high warm load and realize heat supply
Or refrigeration;Property by working media (solution and refrigerant medium) is influenced, and low temperature thermic load can not often be applied to absorption
In heat pump flowsheet, cause its application field and application range by larger limitation;Also it is cold that absorption heat pump technology can not be played
The big advantage of agent steam latent heat.
Using the compression heat pump technology of the grade difference between mechanical energy and thermal energy, there is certain flexibility, but permitted
In more situations, such compression heat pump is difficult to realize the reasonable utilization to thermal energy;There are also common deficiencies for two kinds of heat pump techniques
Place --- in heating or it can not freeze while realize conversion of the thermal energy to mechanical energy.
In order to play the technical advantage of absorption heat pump, overcome the application limitation of low temperature thermic load, take into account power drive or
Power demand is externally provided, the present invention is proposed comprising compressor, expanding machine, the second expanding machine, condenser and evaporator composition
The temperature difference utilizes link, the temperature difference between high temperature heat source and heated medium is used, and between high temperature heat source and environment
The temperature difference carries out substep utilization, the 4th class thermal drivers compressing-absorbing type heat pump with comprehensive advantage.
Summary of the invention:
Present invention is primarily intended to provide serial 4th class thermal drivers compressing-absorbing type heat pump, specific summary of the invention point
Item is described below:
1. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporator, throttling
Valve, solution pump, solution heat exchanger, compressor, expanding machine and the second expanding machine are formed;Absorber has weak solution pipeline through molten
Liquid pump and solution heat exchanger are connected to generator, and there are also concentrated solution pipelines through solution heat exchanger and absorber company for generator
Logical, there are also refrigerant steam channels be connected to condenser for generator, and there are also cryogen liquid pipelines through throttle valve and evaporator company for condenser
Logical, there are also refrigerant steam channels to be connected to absorber for evaporator, and outside has low-temperature heat medium channel to be communicated with compressor, compressor
There are also low-temperature heat medium channels to be connected to through condenser with expanding machine, and there are also low-temperature heat medium channels through evaporator and second for expanding machine
Expanding machine connection, there are also low-temperature heat medium channels to be connected to external for the second expanding machine, generator there are also high temperature thermal medium channel and
Outside connection, absorber and condenser also have heated medium channel to be connected to outside respectively, and expanding machine and the second expanding machine connect
It connects compressor and transmits power, form the 4th class thermal drivers compressing-absorbing type heat pump;Wherein or expanding machine and the second expanding machine
Connect compressor and solution pump simultaneously transmit power.
2. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporator, throttling
Valve, solution pump, solution heat exchanger, compressor, expanding machine, the second expanding machine and third expanding machine are formed;Absorber has dilute
Solution line is connected to through solution pump and solution heat exchanger with generator, and there are also concentrated solution pipelines through solution heat exchanger for generator
It is connected to absorber, there are also refrigerant steam channels to be connected to condenser for generator, and there are also cryogen liquid pipelines through throttle valve for condenser
It is connected to evaporator, there are also refrigerant steam channels to be connected to absorber for evaporator, and there are low-temperature heat medium channel and compressor in outside
Connection, there are also low-temperature heat medium channels to be connected to through condenser with third expanding machine for compressor, and there are also Low Temperature Thermal Jie for third expanding machine
Matter channel is connected to through condenser with expanding machine, and there are also low-temperature heat medium channels to be connected to through evaporator with the second expanding machine for expanding machine,
There are also low-temperature heat medium channels be connected to outside for second expanding machine, and there are also high temperature thermal medium channels to be connected to external for generator, suction
Receive device and condenser also has heated medium channel to be connected to outside respectively, and expanding machine, the second expanding machine and third expanding machine connect
It connects compressor and transmits power, form the 4th class thermal drivers compressing-absorbing type heat pump;Wherein or expanding machine, the second expanding machine and
Third expanding machine connect compressor and solution pump simultaneously transmit power.
3. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporator, throttling
Valve, solution pump, solution heat exchanger, compressor, expanding machine, the second expanding machine and regenerator are formed;Absorber has weak solution
Pipeline is connected to through solution pump and solution heat exchanger with generator, and there are also concentrated solution pipelines through solution heat exchanger and to inhale for generator
Device connection is received, there are also refrigerant steam channels be connected to condenser for generator, and there are also cryogen liquid pipelines through throttle valve and steaming for condenser
Device connection is sent out, there are also refrigerant steam channels to be connected to absorber for evaporator, and outside has low-temperature heat medium channel to be communicated with compressor,
There are also low-temperature heat medium channels to be connected to through regenerator and condenser with expanding machine for compressor, and there are also low-temperature heat medium channels for expanding machine
Be connected to through regenerator and evaporator with the second expanding machine, the second expanding machine there are also low-temperature heat medium channel with outside be connected to, generation
Device there are also high temperature thermal medium channel with outside be connected to, absorber and condenser also have heated medium channel to connect with outside respectively
Logical, expanding machine and the second expanding machine connect compressor simultaneously transmit power, form the 4th class thermal drivers compressing-absorbing type heat pump;Its
In or expanding machine and the second expanding machine connect compressor and solution pump and transmit power.
4. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporator, throttling
Valve, solution pump, solution heat exchanger, compressor, expanding machine, the second expanding machine and regenerator are formed;Absorber has weak solution
Pipeline is connected to through solution pump and solution heat exchanger with generator, and there are also concentrated solution pipelines through solution heat exchanger and to inhale for generator
Device connection is received, there are also refrigerant steam channels be connected to condenser for generator, and there are also cryogen liquid pipelines through throttle valve and steaming for condenser
Send out device connection, there are also refrigerant steam channels be connected to absorber for evaporator, outside have low-temperature heat medium channel through regenerator with press
The connection of contracting machine, there are also low-temperature heat medium channels to be connected to through condenser with expanding machine for compressor, and there are also low-temperature heat mediums to lead to for expanding machine
Road is connected to through evaporator and regenerator with the second expanding machine, the second expanding machine there are also low-temperature heat medium channel with outside be connected to, hair
There are also high temperature thermal medium channels to be connected to external for raw device, and absorber and condenser also have heated medium channel to connect with outside respectively
Logical, expanding machine and the second expanding machine connect compressor simultaneously transmit power, form the 4th class thermal drivers compressing-absorbing type heat pump;Its
In or expanding machine and the second expanding machine connect compressor and solution pump and transmit power.
5. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporator, throttling
Valve, solution pump, solution heat exchanger, compressor, expanding machine, the second expanding machine and high-temperature heat exchanger are formed;Absorber has
Weak solution pipeline is connected to through solution pump and solution heat exchanger with generator, and there are also concentrated solution pipelines through solution heat exchange for generator
Device is connected to absorber, and there are also refrigerant steam channels to be connected to condenser for generator, and there are also cryogen liquid pipelines through throttling for condenser
Valve is connected to evaporator, and there are also refrigerant steam channels to be connected to absorber for evaporator, and there are low-temperature heat medium channel and compression in outside
Machine connection, there are also low-temperature heat medium channels to be connected to through condenser and high-temperature heat exchanger with expanding machine for compressor, and expanding machine is also
Low-temperature heat medium channel is connected to through evaporator with the second expanding machine, and there are also low-temperature heat medium channels to connect with outside for the second expanding machine
Logical, generator and high-temperature heat exchanger also have high temperature thermal medium channel to be connected to outside respectively, and absorber and condenser are also distinguished
There is heated medium channel be connected to outside, expanding machine and the second expanding machine connect compressor simultaneously transmit power, the 4th class of formation
Thermal drivers compressing-absorbing type heat pump;Wherein or expanding machine and the second expanding machine connect compressor and solution pump and transmit power.
6. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporator, throttling
Valve, solution pump, solution heat exchanger, compressor, expanding machine, the second expanding machine and heat regenerator are formed;Absorber has dilute molten
Liquid pipeline is connected to through solution pump and solution heat exchanger with generator, generator there are also concentrated solution pipeline through solution heat exchanger with
Absorber connection, there are also refrigerant steam channels to be connected to condenser for generator, and there are also cryogen liquid pipelines through cold and heat recovery for condenser
Device and throttle valve are connected to evaporator, and there are also refrigerant steam channels to be connected to absorber for evaporator, and outside has low-temperature heat medium logical
Road is communicated with compressor, and there are also low-temperature heat medium channels to be connected to through heat regenerator and condenser with expanding machine for compressor, expanding machine
There are also low-temperature heat medium channels to be connected to through evaporator with the second expanding machine, and there are also low-temperature heat medium channels and outside for the second expanding machine
Connection, there are also high temperature thermal medium channels to be connected to external for generator, and absorber and condenser also have heated medium channel respectively
Be connected to outside, expanding machine and the second expanding machine connect compressor simultaneously transmit power, the 4th class thermal drivers compressing-absorbing type of formation
Heat pump;Wherein or expanding machine and the second expanding machine connect compressor and solution pump and transmit power.
7. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporator, throttling
Valve, solution pump, solution heat exchanger, compressor, expanding machine, the second expanding machine, regenerator and heat regenerator are formed;Absorber
There is weak solution pipeline to be connected to through solution pump and solution heat exchanger with generator, there are also concentrated solution pipelines to hand over through solution heat for generator
Parallel operation is connected to absorber, and there are also refrigerant steam channels to be connected to condenser for generator, and there are also cryogen liquid pipelines through cold for condenser
Heat regenerator and throttle valve are connected to evaporator, and there are also refrigerant steam channels to be connected to absorber for evaporator, and there is Low Temperature Thermal in outside
Medium channel is communicated with compressor, and there are also low-temperature heat medium channels through regenerator, heat regenerator and condenser and expansion for compressor
Machine connection, there are also low-temperature heat medium channels to be connected to through regenerator and evaporator with the second expanding machine for expanding machine, and the second expanding machine is also
There is low-temperature heat medium channel be connected to outside, there are also high temperature thermal medium channels to be connected to external for generator, absorber and condenser
Also there is heated medium channel be connected to outside respectively, expanding machine and the second expanding machine connect compressor simultaneously transmit power, formation
4th class thermal drivers compressing-absorbing type heat pump;Wherein or expanding machine and the second expanding machine connect compressor and solution pump and transmit
Power.
8. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporator, throttling
Valve, solution pump, solution heat exchanger, compressor, expanding machine, the second expanding machine, regenerator and heat regenerator are formed;Absorber
There is weak solution pipeline to be connected to through solution pump and solution heat exchanger with generator, there are also concentrated solution pipelines to hand over through solution heat for generator
Parallel operation is connected to absorber, and there are also refrigerant steam channels to be connected to condenser for generator, and there are also cryogen liquid pipelines through cold for condenser
Heat regenerator and throttle valve are connected to evaporator, and there are also refrigerant steam channels to be connected to absorber for evaporator, and there is Low Temperature Thermal in outside
Medium channel is communicated with compressor through regenerator, and there are also low-temperature heat medium channels through heat regenerator and condenser and expansion for compressor
Machine connection, there are also low-temperature heat medium channels to be connected to through evaporator and regenerator with the second expanding machine for expanding machine, and the second expanding machine is also
There is low-temperature heat medium channel be connected to outside, there are also high temperature thermal medium channels to be connected to external for generator, absorber and condenser
Also there is heated medium channel be connected to outside respectively, expanding machine and the second expanding machine connect compressor simultaneously transmit power, formation
4th class thermal drivers compressing-absorbing type heat pump;Wherein or expanding machine and the second expanding machine connect compressor and solution pump and transmit
Power.
9. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporator, throttling
Valve, solution pump, solution heat exchanger, compressor, expanding machine, the second expanding machine, high-temperature heat exchanger and heat regenerator are formed;
Absorber has weak solution pipeline to be connected to through solution pump and solution heat exchanger with generator, and there are also concentrated solution pipelines through molten for generator
Liquid heat exchanger is connected to absorber, and there are also refrigerant steam channels to be connected to condenser for generator, and there are also cryogen liquid pipes for condenser
Road is connected to through cold and heat recovery device and throttle valve with evaporator, and there are also refrigerant steam channels to be connected to absorber for evaporator, and outside has
Low-temperature heat medium channel is communicated with compressor, and there are also low-temperature heat medium channels through heat regenerator, condenser and Gao Wenre for compressor
Exchanger is connected to expanding machine, and there are also low-temperature heat medium channels to be connected to through evaporator with the second expanding machine for expanding machine, the second expansion
There are also low-temperature heat medium channels be connected to outside for machine, generator and high-temperature heat exchanger also have respectively high temperature thermal medium channel with outside
Portion's connection, absorber and condenser also have heated medium channel to be connected to outside respectively, expanding machine and the connection of the second expanding machine
Compressor simultaneously transmits power, forms the 4th class thermal drivers compressing-absorbing type heat pump;Wherein or expanding machine and the second expanding machine connect
It connects compressor and solution pump and transmits power.
It is any 4th class thermal drivers compression-described in 1-9 10. the 4th class thermal drivers compressing-absorbing type heat pump
Absorption heat pump increases the second generator, second throttle, the second solution pump and the second solution heat exchanger, absorber and adds
Weak solution pipeline is connected to through the second solution pump and the second solution heat exchanger with the second generator, and there are also concentrated solutions for the second generator
Pipeline is connected to through the second solution heat exchanger with absorber, is had refrigerant steam channel to be connected to condenser in generator and is adjusted to send out
After raw device has refrigerant steam channel to be connected to the second generator the second generator have cryogen liquid pipeline through second throttle again and
Condenser connection, there are also refrigerant steam channels to be connected to condenser for the second generator, the 4th class thermal drivers compressing-absorbing type of formation
Heat pump.
It is any 4th class thermal drivers compression-described in 1-9 11. the 4th class thermal drivers compressing-absorbing type heat pump
Absorption heat pump increases the second generator, second throttle and the second solution heat exchanger, and absorber is had weak solution pipeline warp
Solution pump and solution heat exchanger are connected to generator to be adjusted to absorber and has weak solution pipeline through solution pump, solution heat exchanger
It is connected to the second solution heat exchanger with generator, there is concentrated solution pipeline to be connected to through solution heat exchanger with absorber in generator
Being adjusted to generator has concentrated solution pipeline to be connected to through the second solution heat exchanger with the second generator, and the second generator has dense molten again
Liquid pipeline is connected to through solution heat exchanger with absorber, is had refrigerant steam channel to be connected to condenser in generator and is adjusted to occur
After device has refrigerant steam channel to be connected to the second generator the second generator have again cryogen liquid pipeline through second throttle with it is cold
Condenser connection, there are also refrigerant steam channels be connected to condenser for the second generator, and the 4th class thermal drivers compressing-absorbing type of formation is warm
Pump.
It is any 4th class thermal drivers compression-described in 1-9 12. the 4th class thermal drivers compressing-absorbing type heat pump
Absorption heat pump increases the second generator, second throttle, the second solution pump and the second solution heat exchanger, absorber is had
Weak solution pipeline, which is connected to through solution pump and solution heat exchanger with generator, to be adjusted to absorber and has weak solution pipeline through solution pump
It is connected to solution heat exchanger with the second generator, the second generator has concentrated solution pipeline through the second solution pump and the second solution again
Heat exchanger is connected to generator, is had concentrated solution pipeline to be connected to through solution heat exchanger with absorber in generator and is adjusted to occur
Device has concentrated solution pipeline to be connected to through the second solution heat exchanger and solution heat exchanger with absorber, and generator is had refrigerant vapour
Channel is connected to condenser be adjusted to generator and there is refrigerant steam channel to be connected to the second generator after the second generator have again
Cryogen liquid pipeline is connected to through second throttle with condenser, and there are also refrigerant steam channels to be connected to condenser for the second generator, shape
At the 4th class thermal drivers compressing-absorbing type heat pump.
It is any 4th class thermal drivers compression-described in 1-9 13. the 4th class thermal drivers compressing-absorbing type heat pump
Absorption heat pump increases the second generator, the second absorber, the second solution pump and the second solution heat exchanger, absorber is had
Weak solution pipeline, which is connected to through solution pump and solution heat exchanger with generator, to be adjusted to absorber and has weak solution pipeline through solution pump
It is connected to solution heat exchanger with the second absorber, the second absorber has weak solution pipeline through the second solution pump and the second solution again
Heat exchanger is connected to generator, is had concentrated solution pipeline to be connected to through solution heat exchanger with absorber in generator and is adjusted to occur
Device has concentrated solution pipeline to be connected to through the second solution heat exchanger with the second generator, and the second generator has concentrated solution pipeline through molten again
Liquid heat exchanger is connected to absorber, and there are also refrigerant steam channels to be connected to the second absorber for the second generator, the second generator
There are also high temperature thermal medium channels be connected to outside, and there are also heated medium channels to be connected to external for the second absorber, formation the 4th
Class thermal drivers compressing-absorbing type heat pump.
It is any 4th class thermal drivers compression-described in the 13rd 14. the 4th class thermal drivers compressing-absorbing type heat pump
Absorption heat pump increases third generator, second throttle, third solution pump and third solution heat exchanger, the second absorber
It adds weak solution pipeline and is connected to through third solution pump and third solution heat exchanger with third generator, there are also dense for third generator
Solution line is connected to through third solution heat exchanger with the second generator, has refrigerant steam channel to be connected to condenser in generator
Third generator has cryogen liquid pipeline through second again after being adjusted to generator and having refrigerant steam channel to be connected to third generator
Throttle valve is connected to condenser, and there are also refrigerant steam channels to be connected to condenser for third generator, forms the 4th class thermal drivers pressure
Contracting-absorption heat pump.
It is any 4th class thermal drivers compression-described in the 13rd 15. the 4th class thermal drivers compressing-absorbing type heat pump
Absorption heat pump increases third generator, second throttle and third solution heat exchanger, the second absorber is had weak solution pipe
The second solution pump of road and the second solution heat exchanger are connected to generator to be adjusted to the second absorber and has weak solution pipeline through
Two solution pumps, the second solution heat exchanger and third solution heat exchanger are connected to generator, and generator is had concentrated solution pipeline
It is connected to through the second solution heat exchanger with the second generator and is adjusted to generator and has concentrated solution pipeline through third solution heat exchanger
It being connected to third generator, third generator has concentrated solution pipeline to be connected to through the second solution heat exchanger with the second generator again,
There is refrigerant steam channel to be connected to condenser in generator to be adjusted to generator and there is refrigerant steam channel to be connected to third generator
Third generator has cryogen liquid pipeline to be connected to through second throttle with condenser again later, and there are also refrigerant vapours to lead to for third generator
Road is connected to condenser, forms the 4th class thermal drivers compressing-absorbing type heat pump.
It is any 4th class thermal drivers compression-described in the 13rd 16. the 4th class thermal drivers compressing-absorbing type heat pump
Absorption heat pump increases third generator, second throttle, third solution pump and third solution heat exchanger, and second is absorbed
Device have weak solution pipeline be connected to through the second solution pump and the second solution heat exchanger with generator be adjusted to the second absorber have it is dilute
Solution line is connected to through the second solution pump and the second solution heat exchanger with third generator, and third generator has concentrated solution pipe again
Road is connected to through third solution pump and third solution heat exchanger with generator, has concentrated solution pipeline through the second solution heat in generator
Exchanger be connected to the second generator be adjusted to generator have concentrated solution pipeline through third solution heat exchanger and the second solution heat
Exchanger is connected to the second generator, is had refrigerant steam channel to be connected to condenser in generator and is adjusted to generator and has cryogen steaming
Third generator has cryogen liquid pipeline to be connected to through second throttle with condenser again after vapour channel is connected to third generator, the
There are also refrigerant steam channels to be connected to condenser for three generators, forms the 4th class thermal drivers compressing-absorbing type heat pump.
It is any 4th class thermal drivers pressure described in 10-12 17. the 4th class thermal drivers compressing-absorbing type heat pump
Second throttle is cancelled in contracting-absorption heat pump, increases heater, has cryogen liquid pipeline through second throttle in the second generator
It is connected to condenser and is adjusted to the second generator and there is cryogen liquid pipeline to be connected to through heater with condenser, heater is also heated
Medium channel is connected to outside, forms the 4th class thermal drivers compressing-absorbing type heat pump.
It is any 4th class thermal drivers pressure described in 14-16 18. the 4th class thermal drivers compressing-absorbing type heat pump
Second throttle is cancelled in contracting-absorption heat pump, increases heater, has cryogen liquid pipeline through second throttle in third generator
It is connected to condenser and is adjusted to third generator and there is cryogen liquid pipeline to be connected to through heater with condenser, heater is also heated
Medium channel is connected to outside, forms the 4th class thermal drivers compressing-absorbing type heat pump.
It is any 4th class thermal drivers compression-described in 1-9 19. the 4th class thermal drivers compressing-absorbing type heat pump
In absorption heat pump, increase the second generator, the second absorber, the second solution pump and the second solution heat exchanger, by generator
There is refrigerant steam channel to be connected to condenser to be adjusted to generator and there is refrigerant steam channel to be connected to the second absorber, second absorbs
There are also weak solution pipelines to be connected to through the second solution pump and the second solution heat exchanger with the second generator for device, and the second generator is also
Concentrated solution pipeline is connected to through the second solution heat exchanger with the second absorber, and there are also refrigerant steam channels and condensation for the second generator
Device connection, there are also high temperature thermal medium channels to be connected to external for the second generator, the second absorber there are also heated medium channel and
Outside connection, forms the 4th class thermal drivers compressing-absorbing type heat pump.
20. the 4th class thermal drivers compressing-absorbing type heat pump is any 4th class thermal drivers described in 10-12,17
Compressing-absorbing type heat pump, the second generator are added high temperature thermal medium channel and are connected to outside, and the 4th class thermal drivers compression-is formed
Absorption heat pump.
21. the 4th class thermal drivers compressing-absorbing type heat pump is any 4th class thermal drivers described in 14-16,18
Compressing-absorbing type heat pump, third generator are added high temperature thermal medium channel and are connected to outside, and the 4th class thermal drivers compression-is formed
Absorption heat pump.
It is any 4th class thermal drivers pressure described in 1-21 22. the 4th class thermal drivers compressing-absorbing type heat pump
In contracting-absorption heat pump, increase engine, engine connect compressor simultaneously transmits power to compressor, it is dynamic to form additional external
4th class thermal drivers compressing-absorbing type heat pump of power drive.
It is any 4th class thermal drivers compression type heat described in 1-21 23. the 4th class thermal drivers compression heat pump
In pump, increase working machine, expanding machine connects working machine and transmits power to working machine, and formation is additional externally to provide living load
4th class thermal drivers compressing-absorbing type heat pump.
24. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporator, throttling
Valve, solution pump, solution heat exchanger, compressor, expanding machine, the second expanding machine and heat regenerator are formed;Absorber has dilute molten
Liquid pipeline is connected to through solution pump and solution heat exchanger with generator, generator there are also concentrated solution pipeline through solution heat exchanger with
Absorber connection, there are also refrigerant steam channels to be connected to condenser for generator, and there are also cryogen liquid pipelines through heat regenerator for condenser
It is connected to throttle valve with evaporator, there are also refrigerant steam channels to be connected to absorber for evaporator, and there is low-temperature heat medium channel in outside
It is communicated with compressor, there are also low-temperature heat medium channels to be connected to through heat regenerator with expanding machine for compressor, and there are also Low Temperature Thermals for expanding machine
Medium channel is connected to through evaporator with the second expanding machine, the second expanding machine there are also low-temperature heat medium channel with outside be connected to, generation
Device there are also high temperature thermal medium channel with outside be connected to, absorber and condenser also have heated medium channel to connect with outside respectively
Logical, expanding machine and the second expanding machine connect compressor simultaneously transmit power, form the 4th class thermal drivers compressing-absorbing type heat pump;Its
In or expanding machine and the second expanding machine connect compressor and solution pump and transmit power.
For ease of understanding, explanation is provided --- taking the example shown in figure 1, high warm load cools down and is added in generator 2
To utilize, the high warm load after cooling, which enters after condenser 3, is divided into that two-way --- the first via is supplied to heated medium, the
Two tunnels enter the temperature difference being made of compressor 8, expanding machine 9, the second expanding machine 10, condenser 3 and evaporator 4 and utilize link, drop
It is mildly utilized, the compressing-absorbing type heat pump being cooled to so as to form high temperature driven thermic load under heated medium temperature
Process, referred to as the 4th class drive compressing-absorbing type heat pump.
Detailed description of the invention:
Fig. 1 be according to the present invention provided by the 4th the 1st kind of principled thermal system of class thermal drivers compressing-absorbing type heat pump
Figure.
Fig. 2 be according to the present invention provided by the 4th the 2nd kind of principled thermal system of class thermal drivers compressing-absorbing type heat pump
Figure.
Fig. 3 be according to the present invention provided by the 4th the 3rd kind of principled thermal system of class thermal drivers compressing-absorbing type heat pump
Figure.
Fig. 4 be according to the present invention provided by the 4th the 4th kind of principled thermal system of class thermal drivers compressing-absorbing type heat pump
Figure.
Fig. 5 be according to the present invention provided by the 4th the 5th kind of principled thermal system of class thermal drivers compressing-absorbing type heat pump
Figure.
Fig. 6 be according to the present invention provided by the 4th the 6th kind of principled thermal system of class thermal drivers compressing-absorbing type heat pump
Figure.
Fig. 7 be according to the present invention provided by the 4th the 7th kind of principled thermal system of class thermal drivers compressing-absorbing type heat pump
Figure.
Fig. 8 be according to the present invention provided by the 4th the 8th kind of principled thermal system of class thermal drivers compressing-absorbing type heat pump
Figure.
Fig. 9 be according to the present invention provided by the 4th the 9th kind of principled thermal system of class thermal drivers compressing-absorbing type heat pump
Figure.
Figure 10 be according to the present invention provided by the 4th the 10th kind of principle heating power system of class thermal drivers compressing-absorbing type heat pump
System figure.
Figure 11 be according to the present invention provided by the 4th the 11st kind of principle heating power system of class thermal drivers compressing-absorbing type heat pump
System figure.
Figure 12 be according to the present invention provided by the 4th the 12nd kind of principle heating power system of class thermal drivers compressing-absorbing type heat pump
System figure.
Figure 13 be according to the present invention provided by the 4th the 13rd kind of principle heating power system of class thermal drivers compressing-absorbing type heat pump
System figure.
Figure 14 be according to the present invention provided by the 4th the 14th kind of principle heating power system of class thermal drivers compressing-absorbing type heat pump
System figure.
Figure 15 be according to the present invention provided by the 4th the 15th kind of principle heating power system of class thermal drivers compressing-absorbing type heat pump
System figure.
Figure 16 be according to the present invention provided by the 4th the 16th kind of principle heating power system of class thermal drivers compressing-absorbing type heat pump
System figure.
Figure 17 be according to the present invention provided by the 4th the 17th kind of principle heating power system of class thermal drivers compressing-absorbing type heat pump
System figure.
Figure 18 be according to the present invention provided by the 4th the 18th kind of principle heating power system of class thermal drivers compressing-absorbing type heat pump
System figure.
Figure 19 be according to the present invention provided by the 4th the 19th kind of principle heating power system of class thermal drivers compressing-absorbing type heat pump
System figure.
In figure, 1- absorber, 2- generator, 3- condenser, 4- evaporator, 5- throttle valve, 6- solution pump, the friendship of 7- solution heat
Parallel operation, 8- compressor, 9- expanding machine, the second expanding machine of 10-, 11- third expanding machine, 12- regenerator, 13- high-temperature heat exchanger,
14- heat regenerator, the second generator of 15-, 16- increase throttle valve, the second solution pump of 17-, the second solution heat exchanger of 18-, 19- newly
Second absorber, 20- third generator, 21- third solution pump, 22- third solution heat exchanger, 23- heater.
Specific embodiment:
First it is noted that in the statement of structure and process, do not repeat in inessential situation;To apparent
Process do not state.Carry out the present invention is described in detail with example with reference to the accompanying drawing.
4th class 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, evaporator, throttle valve, solution pump, solution heat
Parallel operation, compressor, expanding machine and the second expanding machine are formed;Absorber 1 has weak solution pipeline through solution pump 6 and solution heat exchange
Device 7 is connected to generator 2, and generator 2 is connected to through solution heat exchanger 7 with absorber 1 there are also concentrated solution pipeline, and generator 2 is also
There is refrigerant steam channel to be connected to condenser 3, condenser 3 is connected to through throttle valve 5 with evaporator 4 there are also cryogen liquid pipeline, is evaporated
Device 4 is connected to there are also refrigerant steam channel with absorber 1, and outside has low-temperature heat medium channel to be connected to compressor 8, and compressor 8 is also
There is low-temperature heat medium channel to be connected to through condenser 3 with expanding machine 9, there are also low-temperature heat medium channels through evaporator 4 and for expanding machine 9
The connection of two expanding machines 10, the second also low-temperature heat medium channel of expanding machine 10 are connected to outside, and there are also high temperature thermal mediums for generator 2
Channel is connected to outside, and absorber 1 and condenser 3 also have heated medium channel to be connected to outside respectively, expanding machine 9 and second
10 connect compressor 8 of expanding machine simultaneously transmits power.
(2) in process, the weak solution of absorber 1 enters generator 2 through solution pump 6 and solution heat exchanger 7, and high warm is situated between
The solution that mass flow enters in it through generator 2, heating discharges refrigerant vapour and provides to condenser 3, the concentrated solution warp of generator 2
Solution heat exchanger 7 enters absorber 1, absorbs refrigerant vapour and heat release in heated medium;The refrigerant vapour of condenser 3 is distinguished
At cryogen liquid after heated medium and low-temperature heat medium, the cryogen liquid of condenser 3 throttles through throttle valve 5 enters evaporation for heat release
Device 4, heat absorption are provided at refrigerant vapour and to absorber 1;Outer low temperature thermal medium enters the boosting heating of compressor 8, flows through condensation
Device 3 simultaneously absorbs heat, and enters expanding machine 9 later and is depressured work done;The low-temperature heat medium that expanding machine 9 discharges flows through evaporator 4 and heat release, it
After flow through the decompression of the second expanding machine 10 and work done and externally discharge, the function of expanding machine 9 and the output of the second expanding machine 10 is supplied to compression
Machine 8 is used as power, and forms the 4th class thermal drivers compressing-absorbing type heat pump.
4th class 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, evaporator, throttle valve, solution pump, solution heat
Parallel operation, compressor, expanding machine, the second expanding machine and third expanding machine are formed;Absorber 1 has weak solution pipeline through solution pump 6
It is connected to solution heat exchanger 7 with generator 2, there are also concentrated solution pipelines through solution heat exchanger 7 and the company of absorber 1 for generator 2
Logical, generator 2 is connected to there are also refrigerant steam channel with condenser 3, and there are also cryogen liquid pipelines through throttle valve 5 and evaporation for condenser 3
Device 4 is connected to, and evaporator 4 is connected to there are also refrigerant steam channel with absorber 1, and outside has low-temperature heat medium channel and compressor 8 to connect
Logical, compressor 8 is connected to through condenser 3 with third expanding machine 11 there are also low-temperature heat medium channel, and there are also low temperature for third expanding machine 11
Hot media channel is connected to through condenser 3 with expanding machine 9, and there are also low-temperature heat medium channels through evaporator 4 and the second expansion for expanding machine 9
Machine 10 is connected to, and there are also low-temperature heat medium channels be connected to external for the second expanding machine 10, the also high temperature thermal medium channel of generator 2 and
Outside connection, absorber 1 and condenser 3 also have heated medium channel to be connected to outside respectively, expanding machine 9, the second expanding machine
10 and 11 connect compressor 8 of third expanding machine and transmit power.
(2) in process, the weak solution of absorber 1 enters generator 2 through solution pump 6 and solution heat exchanger 7, and high warm is situated between
The solution that mass flow enters in it through generator 2, heating discharges refrigerant vapour and provides to condenser 3, the concentrated solution warp of generator 2
Solution heat exchanger 7 enters absorber 1, absorbs refrigerant vapour and heat release in heated medium;The refrigerant vapour of condenser 3 is distinguished
At cryogen liquid after heated medium and low-temperature heat medium, the cryogen liquid of condenser 3 throttles through throttle valve 5 enters evaporation for heat release
Device 4, heat absorption are provided at refrigerant vapour and to absorber 1;Outer low temperature thermal medium enters the boosting heating of compressor 8, flows through condensation
Device 3 simultaneously absorbs heat, and enters third expanding machine 11 later and is depressured work done;The low-temperature heat medium that third expanding machine 11 discharges flows through condenser
It 3 and absorbs heat, enters expanding machine 9 later and be depressured work done;The low-temperature heat medium that expanding machine 9 discharges flows through evaporator 4 and heat release, later
It flows through the decompression work done of the second expanding machine 10 and externally discharges, the function that expanding machine 9, the second expanding machine 10 and third expanding machine 11 export
It is supplied to compressor 8 to be used as power, forms the 4th class thermal drivers compressing-absorbing type heat pump.
4th class 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, evaporator, throttle valve, solution pump, solution heat
Parallel operation, compressor, expanding machine, the second expanding machine and regenerator are formed;Absorber 1 has weak solution pipeline through solution pump 6 and molten
Liquid heat exchanger 7 is connected to generator 2, and generator 2 is connected to through solution heat exchanger 7 with absorber 1 there are also concentrated solution pipeline, is sent out
Raw device 2 is connected to there are also refrigerant steam channel with condenser 3, and there are also cryogen liquid pipelines through throttle valve 5 and the company of evaporator 4 for condenser 3
Logical, evaporator 4 is connected to there are also refrigerant steam channel with absorber 1, and outside has low-temperature heat medium channel to be connected to compressor 8, pressure
Contracting machine 8 is connected to through regenerator 12 and condenser 3 with expanding machine 9 there are also low-temperature heat medium channel, and there are also low-temperature heat mediums for expanding machine 9
Channel is connected to through regenerator 12 and evaporator 4 with the second expanding machine 10, and the second expanding machine 10 is there are also low-temperature heat medium channel and outside
Portion's connection, the also high temperature thermal medium channel of generator 2 are connected to outside, and absorber 1 and condenser 3 also have heated medium respectively
Channel is connected to outside, and expanding machine 9 and 10 connect compressor 8 of the second expanding machine simultaneously transmit power.
(2) in process, the weak solution of absorber 1 enters generator 2 through solution pump 6 and solution heat exchanger 7, and high warm is situated between
The solution that mass flow enters in it through generator 2, heating discharges refrigerant vapour and provides to condenser 3, the concentrated solution warp of generator 2
Solution heat exchanger 7 enters absorber 1, absorbs refrigerant vapour and heat release in heated medium;The refrigerant vapour of condenser 3 is distinguished
At cryogen liquid after heated medium and low-temperature heat medium, the cryogen liquid of condenser 3 throttles through throttle valve 5 enters evaporation for heat release
Device 4, heat absorption are provided at refrigerant vapour and to absorber 1;Outer low temperature thermal medium enters the boosting heating of compressor 8, followed by
Regenerator 12 and condenser 3 simultaneously gradually absorb heat, and enter expanding machine 9 later and are depressured work done;Expanding machine 9 discharge low-temperature heat medium according to
It is secondary to flow through regenerator 12 and evaporator 4 and gradually heat release, the decompression work done of the second expanding machine 10 is flowed through later and is externally discharged, and is expanded
Machine 9 and the function of the second expanding machine 10 output are supplied to compressor 8 and are used as power, and form the 4th class thermal drivers compressing-absorbing type heat pump.
4th class 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, evaporator, throttle valve, solution pump, solution heat
Parallel operation, compressor, expanding machine, the second expanding machine and regenerator are formed;Absorber 1 has weak solution pipeline through solution pump 6 and molten
Liquid heat exchanger 7 is connected to generator 2, and generator 2 is connected to through solution heat exchanger 7 with absorber 1 there are also concentrated solution pipeline, is sent out
Raw device 2 is connected to there are also refrigerant steam channel with condenser 3, and there are also cryogen liquid pipelines through throttle valve 5 and the company of evaporator 4 for condenser 3
Logical, evaporator 4 is connected to there are also refrigerant steam channel with absorber 1, and outside has low-temperature heat medium channel through regenerator 12 and compression
Machine 8 is connected to, and compressor 8 is connected to through condenser 3 with expanding machine 9 there are also low-temperature heat medium channel, and there are also low-temperature heat mediums for expanding machine 9
Channel is connected to through evaporator 4 and regenerator 12 with the second expanding machine 10, and the second expanding machine 10 is there are also low-temperature heat medium channel and outside
Portion's connection, the also high temperature thermal medium channel of generator 2 are connected to outside, and absorber 1 and condenser 3 also have heated medium respectively
Channel is connected to outside, and expanding machine 9 and 10 connect compressor 8 of the second expanding machine simultaneously transmit power.
(2) in process, the weak solution of absorber 1 enters generator 2 through solution pump 6 and solution heat exchanger 7, and high warm is situated between
The solution that mass flow enters in it through generator 2, heating discharges refrigerant vapour and provides to condenser 3, the concentrated solution warp of generator 2
Solution heat exchanger 7 enters absorber 1, absorbs refrigerant vapour and heat release in heated medium;The refrigerant vapour of condenser 3 is distinguished
At cryogen liquid after heated medium and low-temperature heat medium, the cryogen liquid of condenser 3 throttles through throttle valve 5 enters evaporation for heat release
Device 4, heat absorption are provided at refrigerant vapour and to absorber 1;Outer low temperature thermal medium flows through regenerator 12 and absorbs heat, and enters pressure later
The boosting heating of contracting machine 8;The low-temperature heat medium that compressor 8 discharges flows through condenser 3 and absorbs heat, and enters the decompression of expanding machine 9 later and makees
Function;It is swollen to flow through second followed by evaporator 4 and regenerator 12 and gradually heat release later for the low-temperature heat medium that expanding machine 9 discharges
Swollen machine 10 is depressured work done and externally discharges, and the function of expanding machine 9 and the output of the second expanding machine 10 is supplied to compressor 8 and is used as power, shape
At the 4th class thermal drivers compressing-absorbing type heat pump.
4th class 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, evaporator, throttle valve, solution pump, solution heat
Parallel operation, compressor, expanding machine, the second expanding machine and high-temperature heat exchanger are formed;Absorber 1 has weak solution pipeline through solution pump
6 and solution heat exchanger 7 be connected to generator 2, there are also concentrated solution pipelines to connect through solution heat exchanger 7 and absorber 1 for generator 2
Logical, generator 2 is connected to there are also refrigerant steam channel with condenser 3, and there are also cryogen liquid pipelines through throttle valve 5 and evaporation for condenser 3
Device 4 is connected to, and evaporator 4 is connected to there are also refrigerant steam channel with absorber 1, and outside has low-temperature heat medium channel and compressor 8 to connect
Logical, compressor 8 is connected to through condenser 3 and high-temperature heat exchanger 13 with expanding machine 9 there are also low-temperature heat medium channel, and expanding machine 9 is also
There is low-temperature heat medium channel to be connected to through evaporator 4 with the second expanding machine 10, the second expanding machine 10 there are also low-temperature heat medium channel with
Outside connection, generator 2 and high-temperature heat exchanger 13 also have high temperature thermal medium channel to be connected to external respectively, absorber 1 and cold
Condenser 3 also has heated medium channel to be connected to outside respectively, and expanding machine 9 and 10 connect compressor 8 of the second expanding machine are simultaneously transmitted
Power.
(2) in process, the weak solution of absorber 1 enters generator 2 through solution pump 6 and solution heat exchanger 7, and high warm is situated between
The solution that mass flow enters in it through generator 2, heating discharges refrigerant vapour and provides to condenser 3, the concentrated solution warp of generator 2
Solution heat exchanger 7 enters absorber 1, absorbs refrigerant vapour and heat release in heated medium;The refrigerant vapour of condenser 3 is distinguished
At cryogen liquid after heated medium and low-temperature heat medium, the cryogen liquid of condenser 3 throttles through throttle valve 5 enters evaporation for heat release
Device 4, heat absorption are provided at refrigerant vapour and to absorber 1;Outer low temperature thermal medium flows through the boosting heating of compressor 8, followed by
Condenser 3 and high-temperature heat exchanger 13 simultaneously gradually absorb heat, and enter expanding machine 9 later and are depressured work done;The Low Temperature Thermal that expanding machine 9 discharges
Medium flows through evaporator 4 and heat release, flows through the decompression work done of the second expanding machine 10 later and externally discharges, expanding machine 9 and second is swollen
The function that swollen machine 10 exports is supplied to compressor 8 and is used as power, and forms the 4th class thermal drivers compressing-absorbing type heat pump.
4th class 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, evaporator, throttle valve, solution pump, solution heat
Parallel operation, compressor, expanding machine, the second expanding machine and heat regenerator are formed;Absorber 1 has weak solution pipeline through 6 He of solution pump
Solution heat exchanger 7 is connected to generator 2, and generator 2 is connected to through solution heat exchanger 7 with absorber 1 there are also concentrated solution pipeline,
Generator 2 is connected to there are also refrigerant steam channel with condenser 3, and there are also cryogen liquid pipelines through cold and heat recovery device 14 and section for condenser 3
Stream valve 5 is connected to evaporator 4, and evaporator 4 is connected to there are also refrigerant steam channel with absorber 1, and there is low-temperature heat medium channel in outside
It is connected to compressor 8, compressor 8 is connected to through heat regenerator 14 and condenser 3 with expanding machine 9 there are also low-temperature heat medium channel, swollen
Swollen machine 9 is connected to through evaporator 4 with the second expanding machine 10 there are also low-temperature heat medium channel, and there are also low-temperature heat mediums for the second expanding machine 10
Channel be connected to outside, and there are also high temperature thermal medium channels to be connected to external for generator 2, absorber 1 and condenser 3 also have respectively by
Heating medium passage is connected to outside, and expanding machine 9 and 10 connect compressor 8 of the second expanding machine simultaneously transmit power.
(2) in process, the weak solution of absorber 1 enters generator 2 through solution pump 6 and solution heat exchanger 7, and high warm is situated between
The solution that mass flow enters in it through generator 2, heating discharges refrigerant vapour and provides to condenser 3, the concentrated solution warp of generator 2
Solution heat exchanger 7 enters absorber 1, absorbs refrigerant vapour and heat release in heated medium;The refrigerant vapour of condenser 3 is distinguished
Heat release after heated medium and low-temperature heat medium at cryogen liquid, the cryogen liquid stream of condenser 3 through heat regenerator 14 and heat release,
Enter evaporator 4 through 5 reducing pressure by regulating flow of throttle valve later, absorb heat into refrigerant vapour and is provided to absorber 1;Outer low temperature thermal medium
It boosts and heats up into compressor 8, absorb heat followed by heat regenerator 14 and condenser 3 and gradually, enter expanding machine 9 later and be depressured
Work done;The low-temperature heat medium that expanding machine 9 discharges flows through evaporator 4 and heat release, flows through the second expanding machine 10 decompression work done later simultaneously
The function of externally discharge, expanding machine 9 and the output of the second expanding machine 10 is supplied to compressor 8 and is used as power, and forms the 4th class thermal drivers pressure
Contracting-absorption heat pump.
4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 7 is achieved in that
(1) in structure, it is mainly handed over by absorber, generator, condenser, evaporator, throttle valve, solution pump, solution heat
Parallel operation, compressor, expanding machine, the second expanding machine, regenerator and heat regenerator are formed;Absorber 1 has weak solution pipeline through molten
Liquid pump 6 and solution heat exchanger 7 are connected to generator 2, and there are also concentrated solution pipelines through solution heat exchanger 7 and to absorb for generator 2
Device 1 is connected to, and generator 2 is connected to there are also refrigerant steam channel with condenser 3, and there are also cryogen liquid pipelines through cold and heat recovery for condenser 3
Device 14 and throttle valve 5 are connected to evaporator 4, and evaporator 4 is connected to there are also refrigerant steam channel with absorber 1, and there is Low Temperature Thermal in outside
Medium channel is connected to compressor 8, and there are also low-temperature heat medium channels through regenerator 12, heat regenerator 14 and condenser 3 for compressor 8
It being connected to expanding machine 9, expanding machine 9 is connected to through regenerator 12 and evaporator 4 with the second expanding machine 10 there are also low-temperature heat medium channel,
The second also low-temperature heat medium channel of expanding machine 10 is connected to outside, and the also high temperature thermal medium channel of generator 2 is connected to outside,
Absorber 1 and condenser 3 also have heated medium channel to be connected to outside respectively, expanding machine 9 and the second expanding machine 10 connection pressure
Contracting machine 8 simultaneously transmits power.
(2) in process, the weak solution of absorber 1 enters generator 2 through solution pump 6 and solution heat exchanger 7, and high warm is situated between
The solution that mass flow enters in it through generator 2, heating discharges refrigerant vapour and provides to condenser 3, the concentrated solution warp of generator 2
Solution heat exchanger 7 enters absorber 1, absorbs refrigerant vapour and heat release in heated medium;The refrigerant vapour of condenser 3 is distinguished
Heat release after heated medium and low-temperature heat medium at cryogen liquid, the cryogen liquid stream of condenser 3 through heat regenerator 14 and heat release,
Enter evaporator 4 through the throttling of throttle valve 5 later, absorb heat into refrigerant vapour and is provided to absorber 1;Outer low temperature thermal medium enters
The boosting heating of compressor 8, absorbs heat followed by regenerator 12, heat regenerator 14 and condenser 3 and gradually, enters expanding machine later
9 decompression works done;The low-temperature heat medium that expanding machine 9 discharges flows through later followed by regenerator 12 and evaporator 4 and gradually heat release
The decompression work done of second expanding machine 10 is simultaneously externally discharged, and the function of expanding machine 9 and the output of the second expanding machine 10 is supplied to 8 actuation of compressor
Power forms the 4th class thermal drivers compressing-absorbing type heat pump.
4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 8 is achieved in that
(1) in structure, it is mainly handed over by absorber, generator, condenser, evaporator, throttle valve, solution pump, solution heat
Parallel operation, compressor, expanding machine, the second expanding machine, regenerator and heat regenerator are formed;Absorber 1 has weak solution pipeline through molten
Liquid pump 6 and solution heat exchanger 7 are connected to generator 2, and there are also concentrated solution pipelines through solution heat exchanger 7 and to absorb for generator 2
Device 1 is connected to, and generator 2 is connected to there are also refrigerant steam channel with condenser 3, and there are also cryogen liquid pipelines through cold and heat recovery for condenser 3
Device 14 and throttle valve 5 are connected to evaporator 4, and evaporator 4 is connected to there are also refrigerant steam channel with absorber 1, and there is Low Temperature Thermal in outside
Medium channel is connected to through regenerator 12 with compressor 8, and there are also low-temperature heat medium channels through heat regenerator 14 and condenser for compressor 8
3 are connected to expanding machine 9, and there are also low-temperature heat medium channels through evaporator 4 and regenerator 12 and the second expanding machine 10 company for expanding machine 9
Logical, the second also low-temperature heat medium channel of expanding machine 10 is connected to outside, and generator 2 connects there are also high temperature thermal medium channel with outside
Logical, absorber 1 and condenser 3 also have heated medium channel to be connected to outside respectively, expanding machine 9 and the connection of the second expanding machine 10
Compressor 8 simultaneously transmits power.
(2) in process, the weak solution of absorber 1 enters generator 2 through solution pump 6 and solution heat exchanger 7, and high warm is situated between
The solution that mass flow enters in it through generator 2, heating discharges refrigerant vapour and provides to condenser 3, the concentrated solution warp of generator 2
Solution heat exchanger 7 enters absorber 1, absorbs refrigerant vapour and heat release in heated medium;The refrigerant vapour of condenser 3 is distinguished
Heat release after heated medium and low-temperature heat medium at cryogen liquid, the cryogen liquid stream of condenser 3 through heat regenerator 14 and heat release,
Enter evaporator 4 through the throttling of throttle valve 5 later, absorb heat into refrigerant vapour and is provided to absorber 1;Outer low temperature thermal medium flows through
Regenerator 12 simultaneously absorbs heat, and enters the boosting heating of compressor 8 later;The low-temperature heat medium that compressor 8 discharges is followed by recuperation of heat
Device 14 and condenser 3 simultaneously gradually absorb heat, and enter expanding machine 9 later and are depressured work done;The low-temperature heat medium that expanding machine 9 discharges successively flows
Through evaporator 4 and regenerator 12 and gradually heat release, the decompression work done of the second expanding machine 10 is flowed through later and is externally discharged, expanding machine 9
Compressor 8 is supplied to the function of the second expanding machine 10 output to be used as power, and forms the 4th class thermal drivers compressing-absorbing type heat pump.
4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 9 is achieved in that
(1) in structure, it is mainly handed over by absorber, generator, condenser, evaporator, throttle valve, solution pump, solution heat
Parallel operation, compressor, expanding machine, the second expanding machine, high-temperature heat exchanger and heat regenerator are formed;Absorber 1 has weak solution pipe
Road is connected to through solution pump 6 and solution heat exchanger 7 with generator 2, and there are also concentrated solution pipelines through solution heat exchanger 7 for generator 2
It is connected to absorber 1, generator 2 is connected to there are also refrigerant steam channel with condenser 3, and there are also cryogen liquid pipelines through cold for condenser 3
Heat regenerator 14 and throttle valve 5 are connected to evaporator 4, and evaporator 4 is connected to there are also refrigerant steam channel with absorber 1, and outside has
Low-temperature heat medium channel is connected to compressor 8, and there are also low-temperature heat medium channels through heat regenerator 14, condenser 3 and height for compressor 8
Temperature heat exchanger 13 is connected to expanding machine 9, and there are also low-temperature heat medium channels through evaporator 4 and the second expanding machine 10 company for expanding machine 9
Logical, the second also low-temperature heat medium channel of expanding machine 10 is connected to outside, and generator 2 and high-temperature heat exchanger 13 also have height respectively
Warm channel is connected to outside, and absorber 1 and condenser 3 also have heated medium channel to be connected to outside respectively, is expanded
Machine 9 and 10 connect compressor 8 of the second expanding machine simultaneously transmit power.
(2) in process, the weak solution of absorber 1 enters generator 2 through solution pump 6 and solution heat exchanger 7, and high warm is situated between
The solution that mass flow enters in it through generator 2, heating discharges refrigerant vapour and provides to condenser 3, the concentrated solution warp of generator 2
Solution heat exchanger 7 enters absorber 1, absorbs refrigerant vapour and heat release in heated medium;The refrigerant vapour of condenser 3 is distinguished
Heat release after heated medium and low-temperature heat medium at cryogen liquid, the cryogen liquid stream of condenser 3 through heat regenerator 14 and heat release,
Enter evaporator 4 through the throttling of throttle valve 5 later, absorb heat into refrigerant vapour and is provided to absorber 1;Outer low temperature thermal medium flows through
The boosting heating of compressor 8, absorbs heat followed by heat regenerator 14, condenser 3 and high-temperature heat exchanger 13 and gradually, enters later
Expanding machine 9 is depressured work done;The low-temperature heat medium that expanding machine 9 discharges flows through evaporator 4 and heat release, flows through the second expanding machine 10 later
Decompression work done is simultaneously externally discharged, and the function of expanding machine 9 and the output of the second expanding machine 10 is supplied to compressor 8 and is used as power, and forms the 4th
Class thermal drivers compressing-absorbing type heat pump.
4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 10 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 1, increase the second generator, second
Throttle valve, the second solution pump and the second solution heat exchanger, absorber 1 add weak solution pipeline through the second solution pump 17 and second
Solution heat exchanger 18 is connected to the second generator 15, and there are also concentrated solution pipelines through the second solution heat exchanger for the second generator 15
18 are connected to absorber 1, have refrigerant steam channel to be connected to condenser 3 in generator 2 and are adjusted to generator 2 and have refrigerant vapour to lead to
Second generator 15 has cryogen liquid pipeline to connect through second throttle 16 and condenser 3 again after road is connected to the second generator 15
Logical, the second generator 15 is connected to there are also refrigerant steam channel with condenser 4.
(2) in process, the refrigerant vapour that generator 2 generates is supplied to the second generator 15 and makees driving thermal medium, absorber 1
Part weak solution enter the second generator 15 through the second solution pump 17 and the second solution heat exchanger 18, refrigerant vapour flows through the
The solution that two generators 15, heating enter in it discharges refrigerant vapour and provides to condenser 3, the concentrated solution of the second generator 15
Enter absorber 1 through the second solution heat exchanger 18;The refrigerant vapour heat release of the second generator 15 is flowed through into cryogen liquid, after pass through
The throttling of second throttle 16 enters condenser 3, forms the 4th class thermal drivers compressing-absorbing type heat pump.
4th class thermal drivers compressing-absorbing type heat pump shown in Figure 11 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 1, increase the second generator, second
Absorber 1 is had weak solution pipeline through solution pump 6 and solution heat exchanger 7 and occurred by throttle valve and the second solution heat exchanger
The connection of device 2 be adjusted to absorber 1 have weak solution pipeline through solution pump 6, solution heat exchanger 7 and the second solution heat exchanger 18 with
Generator 2 is connected to, and is had concentrated solution pipeline to be connected to absorber 1 through solution heat exchanger 7 in generator 2 and is adjusted to generator 2 and has
Concentrated solution pipeline is connected to through the second solution heat exchanger 18 with the second generator 15, and the second generator 15 has concentrated solution pipeline warp again
Solution heat exchanger 7 is connected to absorber 1, is had refrigerant steam channel to be connected to condenser 3 in generator 2 and is adjusted to generator 2
Second generator 15 has cryogen liquid pipeline through second throttle 16 again after having refrigerant steam channel to be connected to the second generator 15
It is connected to condenser 3, the second generator 15 is connected to there are also refrigerant steam channel with condenser 3.
(2) in process, the refrigerant vapour that generator 2 generates is supplied to the second generator 15 and makees driving thermal medium, absorber 1
Weak solution through solution pump 6, solution heat exchanger 7 and the second solution heat exchanger 18 enter generator 2, generator 2 it is dense molten
Liquid enters the second generator 15 through the second solution heat exchanger 18, and refrigerant vapour flows through the second generator 15, heating enters in it
Solution release refrigerant vapour and provided to condenser 3, the concentrated solution of the second generator 15 enters through solution heat exchanger 7 to be absorbed
Device 1;The refrigerant vapour heat release of the second generator 15 is flowed through into cryogen liquid, after through the throttling of second throttle 16 enter condenser 3,
Form the 4th class thermal drivers compressing-absorbing type heat pump.
4th class thermal drivers compressing-absorbing type heat pump shown in Figure 12 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 1, increase the second generator, second
Absorber 1 is had weak solution pipeline to hand over through solution pump 6 and solution heat by throttle valve, the second solution pump and the second solution heat exchanger
Parallel operation 7 be connected to generator 2 be adjusted to absorber 1 have weak solution pipeline through solution pump 6 and solution heat exchanger 7 and second occur
Device 15 is connected to, and the second generator 15 has concentrated solution pipeline through the second solution pump 17 and the second solution heat exchanger 18 and generator again
Generator 2 is had concentrated solution pipeline to be connected to absorber 1 through solution heat exchanger 7 and is adjusted to generator 2 and has concentrated solution by 2 connections
Pipeline is connected to through the second solution heat exchanger 18 and solution heat exchanger 7 with absorber 1, and generator 2 is had refrigerant steam channel
Second generator 15 is connected to after being adjusted to generator 2 and having refrigerant steam channel to be connected to the second generator 15 with condenser 3 again
There is cryogen liquid pipeline to be connected to through second throttle 16 with condenser 3, there are also refrigerant steam channel and condensers 3 for the second generator 15
Connection.
(2) in process, the refrigerant vapour that generator 2 generates is supplied to the second generator 15 and makees driving thermal medium, absorber 1
Weak solution enter the second generator 15 through solution pump 6 and solution heat exchanger 7, refrigerant vapour flow through the second generator 15 plus
Heat enters the solution release refrigerant vapour in it and to the offer of condenser 3, and the concentrated solution of the second generator 15 is through the second solution pump
17 and second solution heat exchanger 18 enter generator 2, the concentrated solution of generator 2 is through the second solution heat exchanger 18 and solution heat
Exchanger 7 enters absorber 1;The refrigerant vapour heat release of the second generator 15 is flowed through into cryogen liquid, after through second throttle 16
Throttling enters condenser 3, forms the 4th class thermal drivers compressing-absorbing type heat pump.
4th class thermal drivers compressing-absorbing type heat pump shown in Figure 13 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 1, increase the second generator, second
Absorber 1 is had weak solution pipeline to hand over through solution pump 6 and solution heat by absorber, the second solution pump and the second solution heat exchanger
Parallel operation 7 be connected to generator 2 be adjusted to absorber 1 have weak solution pipeline through solution pump 6 and solution heat exchanger 7 and second absorb
Device 19 is connected to, and the second absorber 19 has weak solution pipeline through the second solution pump 17 and the second solution heat exchanger 18 and generator again
Generator 2 is had concentrated solution pipeline to be connected to absorber 1 through solution heat exchanger 7 and is adjusted to generator 2 and has concentrated solution by 2 connections
Pipeline is connected to through the second solution heat exchanger 18 with the second generator 15, and the second generator 15 has concentrated solution pipeline through solution heat again
Exchanger 7 is connected to absorber 1, and the second generator 15 is connected to there are also refrigerant steam channel with the second absorber 19, and second occurs
The also high temperature thermal medium channel of device 15 is connected to outside, and the second also heated medium channel of absorber 19 is connected to outside.
(2) in process, the weak solution of absorber 1 enters the second absorber 19 through solution pump 6 and solution heat exchanger 7, inhales
It receives refrigerant vapour and heat release is in heated medium, the weak solution of the second absorber 19 is handed over through the second solution pump 17 and the second solution heat
Parallel operation 18 enters generator 2, and the concentrated solution of generator 2 enters the second generator 15, Gao Wenre through the second solution heat exchanger 18
The solution that medium flows through generator 2, heating enters in it discharges refrigerant vapour and provides to the second absorber 19, the second generator
15 concentrated solution enters absorber 1 through solution heat exchanger 7, forms the 4th class thermal drivers compressing-absorbing type heat pump.
4th class thermal drivers compressing-absorbing type heat pump shown in Figure 14 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Figure 13, increase third generator, second
Throttle valve, third solution pump and third solution heat exchanger, the second absorber 19 add weak solution pipeline through third solution pump 21
It is connected to third solution heat exchanger 22 with third generator 20, there are also concentrated solution pipelines through third solution heat for third generator 20
Exchanger 22 is connected to the second generator 15, is had refrigerant steam channel to be connected to condenser 3 in generator 2 and is adjusted to generator 2
Third generator 20 has cryogen liquid pipeline through second throttle 16 again after having refrigerant steam channel to be connected to third generator 20
It is connected to condenser 3, third generator 20 is connected to there are also refrigerant steam channel with condenser 3.
(2) in process, the refrigerant vapour that generator 2 generates is supplied to third generator 20 and makees driving thermal medium, and second inhales
The part weak solution for receiving device 19 enters third generator 20, refrigerant vapour through third solution pump 21 and third solution heat exchanger 22
Third generator 20, heating are flowed through into the solution release refrigerant vapour in it and is provided to condenser 3, third generator 20
Concentrated solution enters the second generator 15 through third solution heat exchanger 22;Flow through the refrigerant vapour heat release Cheng Leng of third generator 20
Agent liquid, after through second throttle 16 throttling enter condenser 3, formed the 4th class thermal drivers compressing-absorbing type heat pump.
4th class thermal drivers compressing-absorbing type heat pump shown in figure 15 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Figure 13, increase third generator, second
Second absorber 19 is had weak solution pipeline through the second solution pump 17 and the second solution heat by throttle valve and third solution heat exchanger
Exchanger 18 be connected to generator 2 be adjusted to the second absorber 19 have weak solution pipeline through the second solution pump 17, the second solution heat
Exchanger 18 and third solution heat exchanger 22 are connected to generator 2, have concentrated solution pipeline to hand over through the second solution heat in generator 2
Parallel operation 18 is connected to the second generator 15 to be adjusted to generator 2 and has concentrated solution pipeline to send out through third solution heat exchanger 22 and third
Raw device 20 is connected to, and third generator 20 has concentrated solution pipeline to be connected to through the second solution heat exchanger 18 with the second generator 15 again,
There is refrigerant steam channel to be connected to condenser 3 in generator 2 to be adjusted to generator 2 and have refrigerant steam channel and third generator 20
Third generator 20 has cryogen liquid pipeline to be connected to through second throttle 16 with condenser 3 again after connection, and third generator 20 is also
There is refrigerant steam channel to be connected to condenser 3, the also high temperature thermal medium channel of third generator 20 is connected to outside.
(2) in process, the refrigerant vapour that external high temperature thermal medium and generator 2 generate is supplied to third generator 20 and drives
The weak solution of dynamic thermal medium, the second absorber 19 is handed over through the second solution pump 17, the second solution heat exchanger 18 and third solution heat
Parallel operation 22 enters generator 2, and the concentrated solution of generator 2 enters third generator 20 through third solution heat exchanger 22, and cryogen steams
Vapour and high temperature thermal medium flow separately through third generator 20, heating enters the solution release refrigerant vapour in it and to condenser 3
It provides, the concentrated solution of third generator 20 enters the second generator 15 through the second solution heat exchanger 18;Flow through third generator
20 refrigerant vapour heat release at cryogen liquid, after through the throttling of second throttle 16 enter condenser 3, form the 4th class thermal drivers pressure
Contracting-absorption heat pump.
4th class thermal drivers compressing-absorbing type heat pump shown in Figure 16 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Figure 13, increase third generator, second
Second absorber 19 is had weak solution pipeline through the second solution pump 17 by throttle valve, third solution pump and third solution heat exchanger
It is connected to the second solution heat exchanger 18 with generator 2 and is adjusted to the second absorber 19 and has weak solution pipeline through the second solution pump 17
It is connected to the second solution heat exchanger 18 with third generator 20, third generator 20 has concentrated solution pipeline through third solution pump again
21 and third solution heat exchanger 22 be connected to generator 2, have concentrated solution pipeline through the second solution heat exchanger 18 in generator 2
It is connected to the second generator 15 and is adjusted to generator 2 and there is concentrated solution pipeline to hand over through third solution heat exchanger 22 and the second solution heat
Parallel operation 18 is connected to the second generator 15, is had refrigerant steam channel to be connected to condenser 3 in generator 2 and is adjusted to generator 2 and has
After refrigerant steam channel is connected to third generator 20 third generator 20 have again cryogen liquid pipeline through second throttle 16 with
Condenser 3 is connected to, and third generator 20 is connected to there are also refrigerant steam channel with condenser 3.
(2) in process, the refrigerant vapour that generator 2 generates is supplied to third generator 20 and makees driving thermal medium, and second inhales
The weak solution for receiving device 19 enters third generator 20 through the second solution pump 17 and the second solution heat exchanger 18, and refrigerant vapour flows through
Third generator 20, heating enter its in solution release refrigerant vapour and to condenser 3 provide, third generator 20 it is dense molten
Liquid enters generator 2 through third solution pump 21 and third solution heat exchanger 22, and the concentrated solution of generator 2 is handed over through third solution heat
Parallel operation 22 and the second solution heat exchanger 18 enter the second generator 15;Flow through the refrigerant vapour heat release Cheng Leng of third generator 20
Agent liquid, after through second throttle 16 throttling enter condenser 3, formed the 4th class thermal drivers compressing-absorbing type heat pump.
4th class thermal drivers compressing-absorbing type heat pump shown in Figure 17 is achieved in that
In the 4th class thermal drivers compressing-absorbing type heat pump shown in Figure 11, cancel second throttle, increases heater, it will
Second generator 15 has cryogen liquid pipeline to be connected to through second throttle 16 with condenser 3 to be adjusted to the second generator 15 and have cryogen liquid
Pipeline is connected to through heater 23 with condenser 3, and the also heated medium channel of heater 23 is connected to outside;Refrigerant vapour flows through
Second generator, 15 heat release flows through heater 23 and heat release in heated medium, enters condenser 3 later, formed at cryogen liquid
4th class thermal drivers compressing-absorbing type heat pump.
4th class thermal drivers compressing-absorbing type heat pump shown in Figure 18 is achieved in that
(1) in structure, in the 4th class thermal drivers compressing-absorbing type heat pump shown in Fig. 1, increase the second generator, second
Generator 2 is had refrigerant steam channel to be connected to adjustment with condenser 3 by absorber, the second solution pump and the second solution heat exchanger
There is refrigerant steam channel to be connected to the second absorber 19 for generator 2, there are also weak solution pipeline is molten through second for the second absorber 19
Liquid pump 17 and the second solution heat exchanger 18 are connected to the second generator 15, and there are also concentrated solution pipelines through second for the second generator 15
Solution heat exchanger 18 is connected to the second absorber 19, and the second generator 15 is connected to there are also refrigerant steam channel with condenser 3, the
The two also high temperature thermal medium channels of generators 15 are connected to outside, and the second absorber 19 connects there are also heated medium channel with outside
It is logical.
(2) in process, the refrigerant vapour that generator 2 generates enters the second absorber 19, the weak solution of the second absorber 19
Enter the second generator 15 through the second solution pump 17 and the second solution heat exchanger 18, high temperature thermal medium flows through the second generator
15, heating enters the solution release refrigerant vapour in it and to the offer of condenser 3, and the concentrated solution of the second generator 15 is molten through second
Liquid heat exchanger 18 enters the second absorber 19, absorbs refrigerant vapour and heat release is in heated medium, forms the 4th class thermal drivers
Compressing-absorbing type heat pump.
5th class absorption heat pump shown in Figure 19 is achieved in that
(1) in structure, it is mainly handed over by absorber, generator, condenser, evaporator, throttle valve, solution pump, solution heat
Parallel operation, compressor, expanding machine, the second expanding machine and heat regenerator are formed;Absorber 1 has weak solution pipeline through 6 He of solution pump
Solution heat exchanger 7 is connected to generator 2, and generator 2 is connected to through solution heat exchanger 7 with absorber 1 there are also concentrated solution pipeline,
Generator 2 is connected to there are also refrigerant steam channel with condenser 3, and there are also cryogen liquid pipelines through heat regenerator 14 and throttling for condenser 3
Valve 5 is connected to evaporator 4, and evaporator 4 is connected to there are also refrigerant steam channel with absorber 1, outside have low-temperature heat medium channel and
Compressor 8 is connected to, and compressor 8 is connected to through heat regenerator 14 with expanding machine 9 there are also low-temperature heat medium channel, and there are also low for expanding machine 9
Warm channel is connected to through evaporator 4 with the second expanding machine 10, and there are also low-temperature heat medium channels and outside for the second expanding machine 10
Connection, the also high temperature thermal medium channel of generator 2 are connected to outside, and absorber 1 and condenser 3 also have heated medium logical respectively
Road is connected to outside, and expanding machine 9 and 10 connect compressor 8 of the second expanding machine simultaneously transmit power.
(2) in process, the weak solution of absorber 1 enters generator 2 through solution pump 6 and solution heat exchanger 7, and high warm is situated between
The solution that mass flow enters in it through generator 2, heating discharges refrigerant vapour and provides to condenser 3, the concentrated solution warp of generator 2
Solution heat exchanger 7 enters absorber 1, absorbs refrigerant vapour and heat release in heated medium;The refrigerant vapour heat release of condenser 3
At cryogen liquid after low-temperature heat medium, the cryogen liquid stream of condenser 3 is through heat regenerator 14 and heat release, later through 5 section of throttle valve
Stream enters evaporator 4, heat absorption is provided at refrigerant vapour and to absorber 1;Outer low temperature thermal medium enters the boosting of compressor 8 and rises
Temperature flows through heat regenerator 14 and absorbs heat, and enters expanding machine 9 later and is depressured work done;The low-temperature heat medium that expanding machine 9 discharges flows through steaming
Device 4 and heat release are sent out, flow through the decompression work done of the second expanding machine 10 later and is externally discharged, expanding machine 9 and the output of the second expanding machine 10
Function be supplied to compressor 8 and be used as power, form the 4th class thermal drivers compressing-absorbing type heat pump.
The effect that the technology of the present invention may be implemented --- the 4th class thermal drivers compressing-absorbing type heat proposed by the invention
Pump, has the following effects that and advantage:
(1) new approaches and new technology that the temperature difference utilizes are proposed.
(2) thermal energy (temperature difference) drives, and realizes heat supply/refrigeration, or may be selected while externally providing power.
(3) absorption heat pump process is combined with compression heat pump process, reduces the compression ratio of compressor.
(4) process is reasonable, and performance index is variable and thermodynamic parameter variation is corresponding, can be realized filling for thermal energy (temperature difference)
Divide and efficiently utilizes.
(5) when necessary, heat supply/refrigeration is realized by external impetus, mode is flexible, and adaptability is good.
(6) effective use for realizing low temperature heat energy, avoids conflicting between low-temperature heat medium parameter and cryogen fluidity energy, more
The deficiency of absorption heat pump technology is mended.
(7) acquisition and release that latent heat realizes thermic load are relied primarily on, the deficiency of gas compression formula heat pump techniques is overcome.
(8) a variety of specific technical solutions are provided, numerous different actual states is coped with, there is the wider scope of application.
(9) heat pump techniques are extended, the type of compressing-absorbing type heat pump is enriched, are conducive to that thermal energy height is better achieved
Effect utilizes.
Claims (24)
1. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporator, throttle valve, molten
Liquid pump, solution heat exchanger, compressor, expanding machine and the second expanding machine are formed;Absorber (1) has weak solution pipeline through solution
Pump (6) and solution heat exchanger (7) are connected to generator (2), and there are also concentrated solution pipelines through solution heat exchanger for generator (2)
(7) it is connected to absorber (1), generator (2) is connected to there are also refrigerant steam channel with condenser (3), and there are also cryogens for condenser (3)
Liquid pipeline is connected to through throttle valve (5) with evaporator (4), and evaporator (4) is connected to there are also refrigerant steam channel with absorber (1), outside
Portion has low-temperature heat medium channel to be connected to compressor (8), compressor (8) there are also low-temperature heat medium channel through condenser (3) with it is swollen
Swollen machine (9) connection, expanding machine (9) are connected to through evaporator (4) with the second expanding machine (10) there are also low-temperature heat medium channel, and second is swollen
Swollen machine (10) also low-temperature heat medium channel is connected to outside, and generator (2) also high temperature thermal medium channel is connected to outside, is inhaled
Receive device (1) and condenser (3) also has heated medium channel to be connected to outside respectively, expanding machine (9) and the second expanding machine (10)
Connect compressor (8) simultaneously transmits power, forms the 4th class thermal drivers compressing-absorbing type heat pump;Wherein or expanding machine (9) and
Two expanding machines (10) connect compressor (8) and solution pump (6) simultaneously transmit power.
2. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporator, throttle valve, molten
Liquid pump, solution heat exchanger, compressor, expanding machine, the second expanding machine and third expanding machine are formed;Absorber (1) has dilute molten
Liquid pipeline is connected to through solution pump (6) and solution heat exchanger (7) with generator (2), and there are also concentrated solution pipelines through molten for generator (2)
Liquid heat exchanger (7) is connected to absorber (1), and generator (2) is connected to there are also refrigerant steam channel with condenser (3), condenser
(3) it is connected to through throttle valve (5) with evaporator (4) there are also cryogen liquid pipeline, there are also refrigerant steam channel and absorbers for evaporator (4)
(1) it is connected to, outside has low-temperature heat medium channel to be connected to compressor (8), and there are also low-temperature heat medium channels through condensing for compressor (8)
Device (3) is connected to third expanding machine (11), and there are also low-temperature heat medium channels through condenser (3) and expanding machine for third expanding machine (11)
(9) it is connected to, expanding machine (9) is connected to through evaporator (4) with the second expanding machine (10) there are also low-temperature heat medium channel, the second expanding machine
(10) there are also low-temperature heat medium channels is connected to outside, and generator (2) also high temperature thermal medium channel is connected to outside, absorber
(1) and condenser (3) also has heated medium channel to be connected to outside respectively, expanding machine (9), the second expanding machine (10) and third
Expanding machine (11) connect compressor (8) simultaneously transmits power, forms the 4th class thermal drivers compressing-absorbing type heat pump;Wherein, it or expands
Machine (9), the second expanding machine (10) and third expanding machine (11) connect compressor (8) and solution pump (6) simultaneously transmit power.
3. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporator, throttle valve, molten
Liquid pump, solution heat exchanger, compressor, expanding machine, the second expanding machine and regenerator are formed;Absorber (1) has weak solution pipe
Road is connected to through solution pump (6) and solution heat exchanger (7) with generator (2), and there are also concentrated solution pipelines through solution heat for generator (2)
Exchanger (7) is connected to absorber (1), and generator (2) is connected to there are also refrigerant steam channel with condenser (3), and condenser (3) is also
There is cryogen liquid pipeline to be connected to through throttle valve (5) with evaporator (4), there are also refrigerant steam channels and absorber (1) to connect for evaporator (4)
Logical, outside has low-temperature heat medium channel to be connected to compressor (8), and there are also low-temperature heat medium channels through regenerator for compressor (8)
(12) it is connected to condenser (3) with expanding machine (9), there are also low-temperature heat medium channels through regenerator (12) and evaporation for expanding machine (9)
Device (4) is connected to the second expanding machine (10), and the second expanding machine (10) also low-temperature heat medium channel is connected to outside, generator
(2) there are also high temperature thermal medium channels is connected to external, absorber (1) and condenser (3) also have respectively heated medium channel and
Outside connection, expanding machine (9) and the second expanding machine (10) connect compressor (8) simultaneously transmit power, form the 4th class thermal drivers pressure
Contracting-absorption heat pump;Wherein or expanding machine (9) and the second expanding machine (10) connect compressor (8) and solution pump (6) and transmit
Power.
4. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporator, throttle valve, molten
Liquid pump, solution heat exchanger, compressor, expanding machine, the second expanding machine and regenerator are formed;Absorber (1) has weak solution pipe
Road is connected to through solution pump (6) and solution heat exchanger (7) with generator (2), and there are also concentrated solution pipelines through solution heat for generator (2)
Exchanger (7) is connected to absorber (1), and generator (2) is connected to there are also refrigerant steam channel with condenser (3), and condenser (3) is also
There is cryogen liquid pipeline to be connected to through throttle valve (5) with evaporator (4), there are also refrigerant steam channels and absorber (1) to connect for evaporator (4)
Logical, outside has low-temperature heat medium channel to be connected to through regenerator (12) with compressor (8), and there are also low-temperature heat mediums to lead to for compressor (8)
Road is connected to through condenser (3) with expanding machine (9), and there are also low-temperature heat medium channels through evaporator (4) and regenerator for expanding machine (9)
(12) it is connected to the second expanding machine (10), the second expanding machine (10) also low-temperature heat medium channel is connected to outside, generator (2)
There are also high temperature thermal medium channels to be connected to outside, and absorber (1) and condenser (3) also have heated medium channel and outside respectively
Connection, expanding machine (9) and the second expanding machine (10) connect compressor (8) simultaneously transmit power, form the 4th class thermal drivers compression-suction
Receipts formula heat pump;Wherein or expanding machine (9) and the second expanding machine (10) connect compressor (8) and solution pump (6) and transmit power.
5. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporator, throttle valve, molten
Liquid pump, solution heat exchanger, compressor, expanding machine, the second expanding machine and high-temperature heat exchanger are formed;Absorber (1) has dilute
Solution line is connected to through solution pump (6) and solution heat exchanger (7) with generator (2), and there are also concentrated solution pipelines to pass through for generator (2)
Solution heat exchanger (7) is connected to absorber (1), and generator (2) is connected to there are also refrigerant steam channel with condenser (3), is condensed
Device (3) is connected to through throttle valve (5) with evaporator (4) there are also cryogen liquid pipeline, and evaporator (4) is there are also refrigerant steam channel and absorbs
Device (1) connection, outside have low-temperature heat medium channel to be connected to compressor (8), and there are also low-temperature heat medium channels through cold for compressor (8)
Condenser (3) and high-temperature heat exchanger (13) are connected to expanding machine (9), and there are also low-temperature heat medium channels through evaporator for expanding machine (9)
(4) it is connected to the second expanding machine (10), the second expanding machine (10) also low-temperature heat medium channel is connected to outside, generator (2)
Also there is high temperature thermal medium channel to be connected to outside respectively with high-temperature heat exchanger (13), absorber (1) and condenser (3) are also distinguished
There is heated medium channel to be connected to outside, expanding machine (9) and the second expanding machine (10) connect compressor (8) simultaneously transmit power,
Form the 4th class thermal drivers compressing-absorbing type heat pump;Wherein or expanding machine (9) and the second expanding machine (10) connect compressor (8)
With solution pump (6) and transmit power.
6. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporator, throttle valve, molten
Liquid pump, solution heat exchanger, compressor, expanding machine, the second expanding machine and heat regenerator are formed;Absorber (1) has weak solution
Pipeline is connected to through solution pump (6) and solution heat exchanger (7) with generator (2), and there are also concentrated solution pipelines through solution for generator (2)
Heat exchanger (7) is connected to absorber (1), and generator (2) is connected to there are also refrigerant steam channel with condenser (3), condenser (3)
There are also cryogen liquid pipelines to be connected to through cold and heat recovery device (14) and throttle valve (5) with evaporator (4), and there are also cryogens to steam for evaporator (4)
Vapour channel is connected to absorber (1), and outside has low-temperature heat medium channel to be connected to compressor (8), and there are also Low Temperature Thermals for compressor (8)
Medium channel is connected to through heat regenerator (14) and condenser (3) with expanding machine (9), and there are also low-temperature heat medium channels for expanding machine (9)
It is connected to through evaporator (4) with the second expanding machine (10), the second expanding machine (10) also low-temperature heat medium channel is connected to outside, is sent out
Raw device (2) also high temperature thermal medium channel is connected to outside, and absorber (1) and condenser (3) also have heated medium logical respectively
Road be connected to outside, and expanding machine (9) and the second expanding machine (10) connect compressor (8) simultaneously transmit power, formation the 4th class heat drive
Dynamic pressure contracting-absorption heat pump;Wherein or expanding machine (9) and the second expanding machine (10) connect compressor (8) and solution pump (6) simultaneously
Transmit power.
7. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporator, throttle valve, molten
Liquid pump, solution heat exchanger, compressor, expanding machine, the second expanding machine, regenerator and heat regenerator are formed;Absorber (1) has
Weak solution pipeline is connected to through solution pump (6) and solution heat exchanger (7) with generator (2), and there are also concentrated solution pipelines for generator (2)
It is connected to through solution heat exchanger (7) with absorber (1), generator (2) is connected to there are also refrigerant steam channel with condenser (3), cold
Condenser (3) is connected to through cold and heat recovery device (14) and throttle valve (5) with evaporator (4) there are also cryogen liquid pipeline, and evaporator (4) is also
Refrigerant steam channel is connected to absorber (1), and outside has low-temperature heat medium channel to be connected to compressor (8), and compressor (8) is also
Low-temperature heat medium channel is connected to through regenerator (12), heat regenerator (14) and condenser (3) with expanding machine (9), and expanding machine (9) is also
There is low-temperature heat medium channel to be connected to through regenerator (12) and evaporator (4) with the second expanding machine (10), the second expanding machine (10) is also
There is low-temperature heat medium channel be connected to outside, there are also high temperature thermal medium channels to be connected to external for generator (2), absorber (1) and
Condenser (3) also has heated medium channel to be connected to outside respectively, expanding machine (9) and the second expanding machine (10) connect compressor
(8) and power is transmitted, forms the 4th class thermal drivers compressing-absorbing type heat pump;Wherein or expanding machine (9) and the second expanding machine
(10) connect compressor (8) and solution pump (6) and power is transmitted.
8. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporator, throttle valve, molten
Liquid pump, solution heat exchanger, compressor, expanding machine, the second expanding machine, regenerator and heat regenerator are formed;Absorber (1) has
Weak solution pipeline is connected to through solution pump (6) and solution heat exchanger (7) with generator (2), and there are also concentrated solution pipelines for generator (2)
It is connected to through solution heat exchanger (7) with absorber (1), generator (2) is connected to there are also refrigerant steam channel with condenser (3), cold
Condenser (3) is connected to through cold and heat recovery device (14) and throttle valve (5) with evaporator (4) there are also cryogen liquid pipeline, and evaporator (4) is also
Refrigerant steam channel is connected to absorber (1), and outside has low-temperature heat medium channel to be connected to through regenerator (12) with compressor (8),
Compressor (8) is connected to through heat regenerator (14) and condenser (3) with expanding machine (9) there are also low-temperature heat medium channel, expanding machine (9)
There are also low-temperature heat medium channels to be connected to through evaporator (4) and regenerator (12) with the second expanding machine (10), the second expanding machine (10)
There are also low-temperature heat medium channels to be connected to outside, and generator (2) also high temperature thermal medium channel is connected to outside, absorber (1)
Also there is heated medium channel to be connected to outside respectively with condenser (3), expanding machine (9) and the second expanding machine (10) connection compression
Machine (8) simultaneously transmits power, forms the 4th class thermal drivers compressing-absorbing type heat pump;Wherein or expanding machine (9) and the second expanding machine
(10) connect compressor (8) and solution pump (6) and power is transmitted.
9. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporator, throttle valve, molten
Liquid pump, solution heat exchanger, compressor, expanding machine, the second expanding machine, high-temperature heat exchanger and heat regenerator are formed;It absorbs
Device (1) has weak solution pipeline to be connected to through solution pump (6) and solution heat exchanger (7) with generator (2), and there are also dense for generator (2)
Solution line is connected to through solution heat exchanger (7) with absorber (1), and there are also refrigerant steam channel and condenser (3) for generator (2)
Connection, condenser (3) are connected to through cold and heat recovery device (14) and throttle valve (5) with evaporator (4) there are also cryogen liquid pipeline, evaporator
(4) it is connected to there are also refrigerant steam channel with absorber (1), outside has low-temperature heat medium channel to be connected to compressor (8), compressor
(8) there are also low-temperature heat medium channels connects through heat regenerator (14), condenser (3) and high-temperature heat exchanger (13) and expanding machine (9)
Logical, expanding machine (9) is connected to through evaporator (4) with the second expanding machine (10) there are also low-temperature heat medium channel, the second expanding machine (10)
There are also low-temperature heat medium channels to be connected to outside, and generator (2) and high-temperature heat exchanger (13) also have high temperature thermal medium logical respectively
Road be connected to outside, and absorber (1) and condenser (3) also have heated medium channel to be connected to external respectively, expanding machine (9) and
Second expanding machine (10) connect compressor (8) simultaneously transmits power, forms the 4th class thermal drivers compressing-absorbing type heat pump;Wherein, or
Expanding machine (9) and the second expanding machine (10) connect compressor (8) and solution pump (6) simultaneously transmit power.
10. the 4th class thermal drivers compressing-absorbing type heat pump is any 4th class thermal drivers compression-described in claim 1-9
Absorption 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 is connected to through the second solution pump (17) and the second solution heat exchanger (18) with the second generator (15), the second hair
Raw device (15) are connected to through the second solution heat exchanger (18) with absorber (1) there are also concentrated solution pipeline, and generator (2) is had cryogen
Steam channel is connected to condenser (3) to be adjusted to after generator (2) has refrigerant steam channel to be connected to the second generator (15)
Second generator (15) has cryogen liquid pipeline to be connected to through second throttle (16) with condenser (3) again, and the second generator (15) is also
There is refrigerant steam channel to be connected to condenser, forms the 4th class thermal drivers compressing-absorbing type heat pump.
11. the 4th class thermal drivers compressing-absorbing type heat pump is any 4th class thermal drivers compression-described in claim 1-9
Absorption heat pump increases the second generator, second throttle and the second solution heat exchanger, absorber (1) is had weak solution pipe
Road, which is connected to through solution pump (6) and solution heat exchanger (7) with generator (2), to be adjusted to absorber (1) and has weak solution pipeline through molten
Liquid pump (6), solution heat exchanger (7) and the second solution heat exchanger (18) are connected to generator (2), generator (2) are had dense
Solution line, which is connected to through solution heat exchanger (7) with absorber (1), to be adjusted to generator (2) and has concentrated solution pipeline through the second solution
Heat exchanger (18) is connected to the second generator (15), and the second generator (15) has concentrated solution pipeline through solution heat exchanger again
(7) it is connected to absorber (1), there is refrigerant steam channel to be connected to condenser (3) in generator (2) and be adjusted to generator (2) and have
The second generator (15) has cryogen liquid pipeline through second throttle again after refrigerant steam channel is connected to the second generator (15)
(16) it is connected to condenser (3), the second generator (15) is connected to there are also refrigerant steam channel with condenser (3), forms the 4th class
Thermal drivers compressing-absorbing type heat pump.
12. the 4th class thermal drivers compressing-absorbing type heat pump is any 4th class thermal drivers compression-described in claim 1-9
Absorption 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 be connected to through solution pump (6) and solution heat exchanger (7) with generator (2) be adjusted to absorber (1) have it is dilute molten
Liquid pipeline is connected to through solution pump (6) and solution heat exchanger (7) with the second generator (15), and the second generator (15) has dense molten again
Liquid pipeline is connected to through the second solution pump (17) and the second solution heat exchanger (18) with generator (2), generator (2) is had dense molten
Liquid pipeline be connected to through solution heat exchanger (7) with absorber (1) be adjusted to generator (2) have concentrated solution pipeline through the second solution heat
Exchanger (18) and solution heat exchanger (7) are connected to absorber (1), and generator (2) is had refrigerant steam channel and condenser
(3) the second generator (15) is again after connection is adjusted to generator (2) and has refrigerant steam channel to be connected to the second generator (15)
There is cryogen liquid pipeline to be connected to through second throttle (16) with condenser (3), the second generator (15) there are also refrigerant steam channel with
Condenser (3) connection, forms the 4th class thermal drivers compressing-absorbing type heat pump.
13. the 4th class thermal drivers compressing-absorbing type heat pump is any 4th class thermal drivers compression-described in claim 1-9
Absorption 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 be connected to through solution pump (6) and solution heat exchanger (7) with generator (2) be adjusted to absorber (1) have it is dilute molten
Liquid pipeline is connected to through solution pump (6) and solution heat exchanger (7) with the second absorber (19), and the second absorber (19) has dilute molten again
Liquid pipeline is connected to through the second solution pump (17) and the second solution heat exchanger (18) with generator (2), generator (2) is had dense molten
Liquid pipeline be connected to through solution heat exchanger (7) with absorber (1) be adjusted to generator (2) have concentrated solution pipeline through the second solution heat
Exchanger (18) is connected to the second generator (15), and the second generator (15) has concentrated solution pipeline through solution heat exchanger (7) again
It is connected to absorber (1), the second generator (15) is connected to there are also refrigerant steam channel with the second absorber (19), the second generator
(15) there are also high temperature thermal medium channels is connected to outside, and the second absorber (19) also heated medium channel is connected to outside,
Form the 4th class thermal drivers compressing-absorbing type heat pump.
14. the 4th class thermal drivers compressing-absorbing type heat pump is any 4th class thermal drivers compression-described in claim 13
Absorption heat pump increases third generator, second throttle, third solution pump and third solution heat exchanger, the second absorber
(19) it adds weak solution pipeline and is connected to through third solution pump (21) and third solution heat exchanger (22) with third generator (20),
Third generator (20) is connected to through third solution heat exchanger (22) with the second generator (15) there are also concentrated solution pipeline, will be occurred
Device (2) has refrigerant steam channel to be connected to condenser (3) to be adjusted to generator (2) and have refrigerant steam channel and third generator
(20) third generator (20) has cryogen liquid pipeline to be connected to through second throttle (16) with condenser (3) again after being connected to, third
Generator (20) is connected to there are also refrigerant steam channel with condenser (3), forms the 4th class thermal drivers compressing-absorbing type heat pump.
15. the 4th class thermal drivers compressing-absorbing type heat pump is any 4th class thermal drivers compression-described in claim 13
Absorption heat pump increases third generator, second throttle and third solution heat exchanger, the second absorber (19) is had dilute molten
Liquid pipeline is connected to generator (2) through the second solution pump (17) and the second solution heat exchanger (18) and is adjusted to the second absorber
(19) have weak solution pipeline through the second solution pump (17), the second solution heat exchanger (18) and third solution heat exchanger (22) with
Generator (2) is had concentrated solution pipeline to connect through the second solution heat exchanger (18) and the second generator (15) by generator (2) connection
It is logical to be adjusted to generator (2) and there is concentrated solution pipeline to be connected to through third solution heat exchanger (22) with third generator (20), third
Generator (20) has concentrated solution pipeline to be connected to through the second solution heat exchanger (18) with the second generator (15) again, by generator
(2) there is refrigerant steam channel to be connected to condenser (3) to be adjusted to generator (2) and have refrigerant steam channel and third generator (20)
Third generator (20) has cryogen liquid pipeline to be connected to through second throttle (16) with condenser (3) again after connection, and third occurs
Device (20) is connected to there are also refrigerant steam channel with condenser (3), forms the 4th class thermal drivers compressing-absorbing type heat pump.
16. the 4th class thermal drivers compressing-absorbing type heat pump is any 4th class thermal drivers compression-described in claim 13
Absorption heat pump increases third generator, second throttle, third solution pump and third solution heat exchanger, and second is absorbed
Device (19) has weak solution pipeline to be connected to through the second solution pump (17) and the second solution heat exchanger (18) with generator (2) to be adjusted to
Second absorber (19) has weak solution pipeline through the second solution pump (17) and the second solution heat exchanger (18) and third generator
(20) be connected to, third generator (20) have concentrated solution pipeline through third solution pump (21) and third solution heat exchanger (22) again and
Generator (2) is had concentrated solution pipeline to connect through the second solution heat exchanger (18) and the second generator (15) by generator (2) connection
The logical generator (2) that is adjusted to has concentrated solution pipeline through third solution heat exchanger (22) and the second solution heat exchanger (18) and the
Two generators (15) connection, by generator (2) have refrigerant steam channel be connected to condenser (3) be adjusted to generator (2) have it is cold
Third generator (20) has cryogen liquid pipeline through second throttle again after agent steam channel is connected to third generator (20)
(16) it is connected to condenser (3), third generator (20) is connected to there are also refrigerant steam channel with condenser (3), forms the 4th class
Thermal drivers compressing-absorbing type heat pump.
17. the 4th class thermal drivers compressing-absorbing type heat pump is any 4th class thermal drivers pressure described in claim 10-12
Second throttle is cancelled in contracting-absorption heat pump, increases heater, has cryogen liquid pipeline through the second section in the second generator (15)
Stream valve (16) is connected to condenser (3) to be adjusted to the second generator (15) and has cryogen liquid pipeline through heater (23) and condenser
(3) it is connected to, heater (23) also heated medium channel is connected to outside, forms the 4th class thermal drivers compressing-absorbing type heat
Pump.
18. the 4th class thermal drivers compressing-absorbing type heat pump is any 4th class thermal drivers pressure described in claim 14-16
Second throttle is cancelled in contracting-absorption heat pump, increases heater, has cryogen liquid pipeline through the second section in third generator (20)
Stream valve (16) is connected to condenser (3) to be adjusted to third generator (20) and has cryogen liquid pipeline through heater (23) and condenser
(3) it is connected to, heater (23) also heated medium channel is connected to outside, forms the 4th class thermal drivers compressing-absorbing type heat
Pump.
19. the 4th class thermal drivers compressing-absorbing type heat pump is any 4th class thermal drivers compression-described in claim 1-9
In absorption heat pump, increase the second generator, the second absorber, the second solution pump and the second solution heat exchanger, by generator
(2) there is refrigerant steam channel to be connected to condenser (3) to be adjusted to generator (2) and have refrigerant steam channel and the second absorber (19)
Connection, there are also weak solution pipelines through the second solution pump (17) and the second solution heat exchanger (18) and second for the second absorber (19)
Generator (15) connection, there are also concentrated solution pipelines through the second solution heat exchanger (18) and the second absorber for the second generator (15)
(19) it is connected to, the second generator (15) is connected to there are also refrigerant steam channel with condenser (3), and there are also high temperature for the second generator (15)
Hot media channel is connected to outside, and the second absorber (19) also heated medium channel is connected to outside, forms the 4th class heat
Drive compressing-absorbing type heat pump.
20. the 4th class thermal drivers compressing-absorbing type heat pump is any 4th class thermal drivers described in claim 10-12,17
Compressing-absorbing type heat pump, the second generator (15) are added high temperature thermal medium channel and are connected to outside, and the 4th class thermal drivers pressure is formed
Contracting-absorption heat pump.
21. the 4th class thermal drivers compressing-absorbing type heat pump is any 4th class thermal drivers described in claim 14-16,18
Compressing-absorbing type heat pump, third generator (20) are added high temperature thermal medium channel and are connected to outside, and the 4th class thermal drivers pressure is formed
Contracting-absorption heat pump.
22. the 4th class thermal drivers compressing-absorbing type heat pump is any 4th class thermal drivers pressure described in claim 1-21
In contracting-absorption heat pump, increase engine, engine connect compressor (8) is simultaneously transmitted power to compressor (8), formed additional
4th class thermal drivers compressing-absorbing type heat pump of external impetus driving.
23. the 4th class thermal drivers compression heat pump is any 4th class thermal drivers compression type heat described in claim 1-21
In pump, increase working machine, expanding machine (9) connects working machine and to working machine transmission power, forms the additional power that externally provides and bear
The 4th class thermal drivers compressing-absorbing type heat pump of lotus.
24. the 4th class thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporator, throttle valve,
Solution pump, solution heat exchanger, compressor, expanding machine, the second expanding machine and heat regenerator are formed;Absorber (1) has dilute molten
Liquid pipeline is connected to through solution pump (6) and solution heat exchanger (7) with generator (2), and there are also concentrated solution pipelines through molten for generator (2)
Liquid heat exchanger (7) is connected to absorber (1), and generator (2) is connected to there are also refrigerant steam channel with condenser (3), condenser
(3) it is connected to through heat regenerator (14) and throttle valve (5) with evaporator (4) there are also cryogen liquid pipeline, there are also cryogens to steam for evaporator (4)
Vapour channel is connected to absorber (1), and outside has low-temperature heat medium channel to be connected to compressor (8), and there are also Low Temperature Thermals for compressor (8)
Medium channel is connected to through heat regenerator (14) with expanding machine (9), and there are also low-temperature heat medium channels through evaporator (4) for expanding machine (9)
It is connected to the second expanding machine (10), the second expanding machine (10) also low-temperature heat medium channel is connected to outside, and generator (2) is also
High temperature thermal medium channel is connected to outside, and absorber (1) and condenser (3) also have heated medium channel to connect with outside respectively
Logical, expanding machine (9) and the second expanding machine (10) connect compressor (8) simultaneously transmit power, formation the 4th class thermal drivers compression-absorption
Formula heat pump;Wherein or expanding machine (9) and the second expanding machine (10) connect compressor (8) and solution pump (6) and transmit power.
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