CN106440497A - First-type thermally driven compression-absorption heat pump - Google Patents
First-type thermally driven compression-absorption heat pump Download PDFInfo
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- CN106440497A CN106440497A CN201610820920.7A CN201610820920A CN106440497A CN 106440497 A CN106440497 A CN 106440497A CN 201610820920 A CN201610820920 A CN 201610820920A CN 106440497 A CN106440497 A CN 106440497A
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- generator
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- absorber
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Classifications
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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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- 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
- F25B1/00—Compression machines, plants or systems with non-reversible cycle
- F25B1/10—Compression machines, plants or systems with non-reversible cycle with multi-stage compression
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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
- F25B41/00—Fluid-circulation arrangements
- F25B41/30—Expansion means; Dispositions thereof
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- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Sorption Type Refrigeration Machines (AREA)
Abstract
The invention provides a first-type thermally driven compression-absorption heat pump, and belongs to the technical field of power, refrigeration and heat pumps. An absorber communicates with a generator via a solution pump and a solution heat exchanger; the generator communicates with the absorber via the solution heat exchanger; the generator successively communicates with a compressor and a condenser by refrigerant steam channels; the condenser communicates with an evaporator via a throttling valve; the evaporator communicates with the absorber by a refrigerant steam channel; the outside successively communicates with a second compressor and a combustion chamber by air channels; the combustion chamber communicates with the outside by a fuel channel and communicates with a gas turbine by a gas channel; the gas turbine communicates with the outside through a gas channel via the generator; the outside successively communicates with a third compressor, the evaporator and an expander by low-temperature heat medium channels; the absorber and the condenser communicate with the outside by heated medium pipelines; and the gas turbine and the expander are connected with the compressor, the second compressor and the third compressor and transmit power, so that the first-type thermally driven compression-absorption heat pump is formed.
Description
Technical field:
The invention belongs to power, refrigeration and technical field of heat pumps.
Background technology:
Cold demand, heat demand and power demand, central with production common by human lives;In reality, people often need
To realize refrigeration, heat supply using high temperature heat or be converted into power it is also desirable to being freezed using power or being utilized power
And carry out heat supply with reference to low temperature heat energy.During stating purpose in realization, many conditions will be faced and limit the energy
Type, grade and quantity, the type of user's request, grade and quantity, the type of working media, the flow process of equipment, structure and
Manufacturing cost, the security that equipment runs, acceptable degree of environment temperature and environment etc..
Heat energy (temperature difference) with absorption heat pump technology as representative utilizes technology, is driven using high warm load and realizes heat supply
Or refrigeration;Property by working media (solution and refrigerant medium) is affected, the high warm load of excessive temperature or excessively low temperature
Low temperature thermic load often cannot reasonably be applied in absorption heat pump flow process, lead to its application and range of application to be subject to
Larger restriction.Compression heat pump technology has preferable flexibility in terms of thermodynamic property, but the core of compression heat pump
Part is moving component, and this brings many unfavorable such as, and the noise producing in compression type heat pump operation makes us being difficult to stand;For
This, need use and the quantity considering to reduce big moving component (mainly compressor and decompressor).
In order to play compression heat pump and the respective technical advantage of absorption heat pump, adapt to air and other gaseous state Low Temperature Thermal
Resource, and take into account power drive or power demand is externally provided, the present invention proposes by compressor, the second compressor, combustion chamber, combustion
Gas-turbine, the 3rd compressor, evaporimeter and decompressor composition the temperature difference utilize system, and by absorber, generator, compressor,
Condenser, evaporimeter, choke valve, solution pump and the solution heat exchanger composition temperature difference utilize system, lift condensation using compressor
Parameter, carries out effectively utilizes or the temperature difference between high temperature heat source and environment is carried out to the temperature difference between high temperature heat source and heated medium
Effectively utilizes, have the first kind thermal drivers compressing-absorbing type heat pump of comprehensive advantage.
Content of the invention:
Present invention is primarily intended to serial first kind thermal drivers compressing-absorbing type heat pump will be provided, concrete content of the invention divides
Item is described below:
1. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporimeter, throttling
Valve, solution pump, solution heat exchanger, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor and decompressor institute
Composition;Absorber has weak solution pipeline to connect with generator with solution heat exchanger through solution pump, and generator also has concentrated solution pipe
Road is connected with absorber through solution heat exchanger, and generator also has refrigerant steam channel to connect with compressor, and compressor is also cold
Agent steam channel is connected with condenser, and condenser also has cryogen liquid pipeline to connect with evaporimeter through choke valve, and evaporimeter is also cold
Agent steam channel is connected with absorber, and outside has air duct to connect with the second compressor, and the second compressor also has compressed air
Passage and combustion chamber, combustion chamber also has fuel channel and ft connection, and combustion chamber also has blast tube with gas turbine even
Logical, after gas turbine also has blast tube to connect with generator, generator has blast tube and ft connection again, and outside also has
Low-temperature heat medium passage is connected with the 3rd compressor, and the 3rd compressor also has low-temperature heat medium passage through evaporimeter with decompressor even
Logical, decompressor also have low-temperature heat medium passage and ft connection, absorber and condenser also have respectively heated medium pipeline with
Ft connection, gas turbine and decompressor connect compressor, the second compressor and the 3rd compressor and transmit power, form first
Class thermal drivers compressing-absorbing type heat pump.
2. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporimeter, throttling
Valve, solution pump, solution heat exchanger, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor, decompressor and
4th compressor is formed;Absorber has weak solution pipeline to connect with generator with solution heat exchanger through solution pump, generator
Concentrated solution pipeline is also had to connect with absorber through solution heat exchanger, generator also has refrigerant steam channel to connect with compressor,
Compressor also has refrigerant steam channel to connect with condenser, and condenser also has cryogen liquid pipeline to connect with evaporimeter through choke valve,
Evaporimeter also has refrigerant steam channel to connect with absorber, and outside has air duct to connect with the second compressor, the second compressor
Also have compressed air channel and combustion chamber, combustion chamber also has fuel channel and ft connection, and combustion chamber also has blast tube
Connect with gas turbine, after gas turbine also has blast tube to connect with generator, generator has blast tube to connect with outside again
Logical, outside also have low-temperature heat medium passage to connect with the 3rd compressor, and the 3rd compressor also has low-temperature heat medium passage through evaporation
Device is connected with the 4th compressor, and the 4th compressor also has low-temperature heat medium passage to connect with decompressor through evaporimeter, and decompressor is also
Low-temperature heat medium passage and ft connection, absorber and condenser is had also to have heated medium pipeline and ft connection respectively, combustion
Gas-turbine and decompressor connect compressor, the second compressor, the 3rd compressor and the 4th compressor and transmit power, form first
Class thermal drivers compressing-absorbing type heat pump.
3. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporimeter, throttling
Valve, solution pump, solution heat exchanger, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor, decompressor and
Regenerator is formed;Absorber has weak solution pipeline to connect with generator with solution heat exchanger through solution pump, and generator also has
Concentrated solution pipeline is connected with absorber through solution heat exchanger, and generator also has refrigerant steam channel to connect with compressor, compression
Machine also has refrigerant steam channel to connect with condenser, and condenser also has cryogen liquid pipeline to connect with evaporimeter through choke valve, evaporation
Device also has refrigerant steam channel to connect with absorber, and outside has air duct to connect with the second compressor, and the second compressor also has
Compressed air channel and combustion chamber, combustion chamber also has fuel channel and ft connection, and combustion chamber also has blast tube and combustion
Gas-turbine connects, and after gas turbine also has blast tube to connect with generator, generator has blast tube and ft connection again,
Outside also have low-temperature heat medium passage to connect with the 3rd compressor through regenerator, and the 3rd compressor also has low-temperature heat medium passage warp
Evaporimeter is connected with decompressor with regenerator, and decompressor also has low-temperature heat medium passage and ft connection, absorber and condenser
Heated medium pipeline and ft connection, gas turbine and decompressor is also had to connect compressor, the second compressor and the 3rd respectively
Compressor simultaneously transmits power, forms first kind thermal drivers compressing-absorbing type heat pump.
4. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporimeter, throttling
Valve, solution pump, solution heat exchanger, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor, decompressor and
Low temperature heat exchanger is formed;Absorber has weak solution pipeline to connect with generator with solution heat exchanger through solution pump, occurs
Device also has concentrated solution pipeline to connect with absorber through solution heat exchanger, and generator also has refrigerant steam channel with compressor even
Logical, compressor also has refrigerant steam channel to connect with condenser, and condenser also has cryogen liquid pipeline through choke valve with evaporimeter even
Logical, evaporimeter also has refrigerant steam channel to connect with absorber, and outside has air duct to connect with the second compressor, the second compression
Machine also has compressed air channel and combustion chamber, and combustion chamber also has fuel channel and ft connection, and combustion chamber also has combustion gas to lead to
Road is connected with gas turbine, and after gas turbine also has blast tube to connect with generator, generator has blast tube and outside again
Connection, the 3rd compressor has circulatory mediator passage to connect with decompressor through evaporimeter, and decompressor also has circulatory mediator passage through low
Temperature heat exchanger is connected with the 3rd compressor, and absorber and condenser also have heated medium pipeline and ft connection respectively, low
Temperature heat exchanger also has low-temperature heat medium passage and ft connection, gas turbine and decompressor to connect compressor, the second compressor
With the 3rd compressor and transmit power, form first kind thermal drivers compressing-absorbing type heat pump.
5. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporimeter, throttling
Valve, solution pump, solution heat exchanger, compressor, the second compressor, combustion chamber, gas turbine and the 3rd compressor are formed;Inhale
Receiving device has weak solution pipeline to connect with generator with solution heat exchanger through solution pump, and generator also has concentrated solution pipeline through solution
Heat exchanger is connected with absorber, and generator also has refrigerant steam channel to connect with compressor, and compressor also has refrigerant vapour to lead to
Road is connected with condenser, and condenser also has cryogen liquid pipeline to connect with evaporimeter through choke valve, and evaporimeter also has refrigerant vapour to lead to
Road is connected with absorber, and outside has air duct to connect with the second compressor, and the second compressor also has compressed air channel and combustion
Burn room connection, combustion chamber also has fuel channel and ft connection, and combustion chamber also has blast tube to connect with gas turbine, combustion gas wheel
After machine also has blast tube to connect with generator, generator has blast tube and ft connection again, and outside also have low-temperature heat medium
Passage is connected with the 3rd compressor, and the 3rd compressor also has low-temperature heat medium passage through evaporimeter and ft connection, absorber and
Condenser also has heated medium pipeline and ft connection respectively, and gas turbine connects compressor, the second compressor and the 3rd pressure
Contracting machine simultaneously transmits power, forms first kind thermal drivers compressing-absorbing type heat pump.
6. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporimeter, throttling
Valve, solution pump, solution heat exchanger, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor, Low Temperature Thermal are handed over
Parallel operation and cryogenic throttle valve are formed;Absorber has weak solution pipeline to connect with generator with solution heat exchanger through solution pump,
Generator also has concentrated solution pipeline to connect with absorber through solution heat exchanger, and generator also has refrigerant steam channel and compressor
Connection, compressor also has refrigerant steam channel to connect with condenser, and condenser also has cryogen liquid pipeline through choke valve and evaporimeter
Connection, evaporimeter also has refrigerant steam channel to connect with absorber, and outside has air duct to connect with the second compressor, the second pressure
Contracting machine also has compressed air channel and combustion chamber, and combustion chamber also has fuel channel and ft connection, and combustion chamber also has combustion gas
Passage is connected with gas turbine, and after gas turbine also has blast tube to connect with generator, generator has blast tube again with outward
Portion connects, and the 3rd compressor has circulatory mediator passage to connect with low temperature heat exchanger with cryogenic throttle valve through evaporimeter, Low Temperature Thermal
Exchanger also has circulatory mediator passage to connect with the 3rd compressor, absorber and condenser also have respectively heated medium pipeline with
Ft connection, low temperature heat exchanger also has low temperature heat exchanger passage and ft connection, and gas turbine connects compressor, the second pressure
Contracting machine and the 3rd compressor simultaneously transmit power, form first kind thermal drivers compressing-absorbing type heat pump.
7. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporimeter, throttling
Valve, solution pump, solution heat exchanger, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor, the 4th compression
Machine, low temperature heat exchanger and cryogenic throttle valve are formed;Absorber have weak solution pipeline through solution pump and solution heat exchanger with
Generator connects, and generator also has concentrated solution pipeline to connect with absorber through solution heat exchanger, and generator also has refrigerant vapour
Passage is connected with compressor, and compressor also has refrigerant steam channel to connect with condenser, and condenser also has cryogen liquid pipeline warp knuckle
Stream valve is connected with evaporimeter, and evaporimeter also has refrigerant steam channel to connect with absorber, and there are air duct and the second compression in outside
Machine connects, and the second compressor also has compressed air channel and combustion chamber, and combustion chamber also has fuel channel and ft connection, combustion
Burning room also has blast tube to connect with gas turbine, and after gas turbine also has blast tube to connect with generator, generator has again
Blast tube and ft connection, the 3rd compressor has circulatory mediator passage to connect with the 4th compressor through evaporimeter, the 4th compression
Machine also has circulatory mediator passage to connect with low temperature heat exchanger with cryogenic throttle valve through evaporimeter, and low temperature heat exchanger also has circulation
Medium channel is connected with the 3rd compressor, and absorber and condenser also have heated medium pipeline and ft connection, low temperature respectively
Heat exchanger also has low temperature heat exchanger passage and ft connection, and gas turbine connects compressor, the second compressor, the 3rd compression
Machine and the 4th compressor simultaneously transmit power, form first kind thermal drivers compressing-absorbing type heat pump.
8. first kind thermal drivers compressing-absorbing type heat pump, is arbitrary first kind thermal drivers compression-suction described in 1-7 item
In receipts formula heat pump, cancel the outside fuel channel with combustion chamber, increase new compressor, outside increases fuel gas passage
Connect with new compressor, new compressor also has compressed gaseous fuel channel and combustion chamber, gas turbine connects newly-increased
Compressor simultaneously transmits power, forms first kind thermal drivers compressing-absorbing type heat pump.
9. first kind thermal drivers compressing-absorbing type heat pump, is arbitrary first kind thermal drivers compression-suction described in 1-8 item
In receipts formula heat pump, increase heater, after gas turbine is had blast tube to connect with generator, generator has blast tube again
Being adjusted to heater after gas turbine has blast tube to be sequentially communicated generator and heater with ft connection has combustion gas to lead to again
Road and ft connection, heater also has heated medium passage and ft connection, forms first kind thermal drivers compressing-absorbing type heat
Pump.
10. first kind thermal drivers compressing-absorbing type heat pump, be arbitrary first kind thermal drivers compression described in 1-8 item-
In absorption heat pump, increase heater, after gas turbine is had blast tube to connect with generator, generator has combustion gas to lead to again
Road and ft connection are adjusted to gas turbine has blast tube to be sequentially communicated the finisher of generator, heater and evaporimeter again
Have blast tube and ft connection, heater also has heated medium passage and ft connection, formed the compression of first kind thermal drivers-
Absorption heat pump.
11. first kind thermal drivers compressing-absorbing type heat pumps, be arbitrary first kind thermal drivers compression described in 1-8 item-
In absorption heat pump, increase the second generator, second throttle, the second solution pump and the second solution heat exchanger, absorber increases
If weak solution pipeline is connected with the second generator through the second solution pump and the second solution heat exchanger, the second generator also has dense molten
Liquid pipeline is connected with absorber through the second solution heat exchanger, generator is had refrigerant steam channel to connect with compressor and is adjusted to
After generator has refrigerant steam channel to connect with the second generator, the second generator has cryogen liquid pipeline again through second throttle
Connect with condenser, the second generator also has refrigerant steam channel to connect with compressor, form first kind thermal drivers compression-absorption
Formula heat pump.
12. first kind thermal drivers compressing-absorbing type heat pumps, be arbitrary first kind thermal drivers compression described in 1-8 item-
In absorption heat pump, increase the second generator, second throttle and the second solution heat exchanger, absorber is had weak solution pipeline
Connect with generator through solution pump and solution heat exchanger and be adjusted to absorber and have weak solution pipeline through solution pump, solution heat exchange
Device and the second solution heat exchanger are connected with generator, and generator is had concentrated solution pipeline through solution heat exchanger with absorber even
Logical be adjusted to generator and have concentrated solution pipeline to connect with the second generator through the second solution heat exchanger, the second generator has dense again
Solution line is connected with absorber through solution heat exchanger, by generator have refrigerant steam channel connect with compressor be adjusted to send out
Raw device have refrigerant steam channel to connect with the second generator after the second generator have cryogen liquid pipeline through second throttle again and
Condenser connects, and the second generator also has refrigerant steam channel to connect with compressor, forms first kind thermal drivers compressing-absorbing type
Heat pump.
13. first kind thermal drivers compressing-absorbing type heat pumps, be arbitrary first kind thermal drivers compression described in 1-8 item-
In absorption heat pump, increase the second generator, second throttle, the second solution pump and the second solution heat exchanger, by absorber
There is weak solution pipeline to connect with generator through solution pump and solution heat exchanger to be adjusted to absorber and have weak solution pipeline through solution
Pump is connected with the second generator with solution heat exchanger, and the second generator has concentrated solution pipeline molten through the second solution pump and second again
Liquid heat exchanger is connected with generator, by generator have concentrated solution pipeline connect with absorber through solution heat exchanger be adjusted to send out
Raw device has concentrated solution pipeline to connect with absorber with solution heat exchanger through the second solution heat exchanger, and generator is had cryogen to steam
Vapour passage is connected with compressor and is adjusted to after generator has refrigerant steam channel to connect with the second generator the second generator again
Cryogen liquid pipeline is had to connect with condenser through second throttle, the second generator also has refrigerant steam channel to connect with compressor,
Form first kind thermal drivers compressing-absorbing type heat pump.
14. first kind thermal drivers compressing-absorbing type heat pumps, be arbitrary first kind thermal drivers compression described in 1-8 item-
In absorption heat pump, increase the second generator, second throttle, the second solution pump and the second solution heat exchanger, absorber increases
If weak solution pipeline is connected with the second generator through the second solution pump and the second solution heat exchanger, the second generator also has dense molten
Liquid pipeline is connected with absorber through the second solution heat exchanger, compressor is had refrigerant steam channel to connect with condenser and is adjusted to
After compressor has refrigerant steam channel to connect with the second generator, the second generator has cryogen liquid pipeline again through second throttle
Connect with condenser, the second generator also has refrigerant steam channel to connect with condenser, form first kind thermal drivers compression-absorption
Formula heat pump.
15. first kind thermal drivers compressing-absorbing type heat pumps, be arbitrary first kind thermal drivers compression described in 1-8 item-
In absorption heat pump, increase the second generator, second throttle and the second solution heat exchanger, absorber is had weak solution pipeline
Connect with generator through solution pump and solution heat exchanger and be adjusted to absorber and have weak solution pipeline through solution pump, solution heat exchange
Device and the second solution heat exchanger are connected with generator, and generator is had concentrated solution pipeline through solution heat exchanger with absorber even
Logical be adjusted to generator and have concentrated solution pipeline to connect with the second generator through the second solution heat exchanger, the second generator has dense again
Solution line is connected with absorber through solution heat exchanger, compressor is had refrigerant steam channel to connect with condenser and is adjusted to pressure
Contracting machine have refrigerant steam channel to connect with the second generator after the second generator have again cryogen liquid pipeline through second throttle with
Condenser connects, and the second generator also has refrigerant steam channel to connect with condenser, forms first kind thermal drivers compressing-absorbing type
Heat pump.
16. first kind thermal drivers compressing-absorbing type heat pumps, be arbitrary first kind thermal drivers compression described in 1-8 item-
In absorption heat pump, increase the second generator, second throttle, the second solution pump and the second solution heat exchanger, by absorber
There is weak solution pipeline to connect with generator through solution pump and solution heat exchanger to be adjusted to absorber and have weak solution pipeline through solution
Pump is connected with the second generator with solution heat exchanger, and the second generator has concentrated solution pipeline molten through the second solution pump and second again
Liquid heat exchanger is connected with generator, by generator have concentrated solution pipeline connect with absorber through solution heat exchanger be adjusted to send out
Raw device has concentrated solution pipeline to connect with absorber with solution heat exchanger through the second solution heat exchanger, and compressor is had cryogen to steam
Vapour passage is connected with condenser and is adjusted to after compressor has refrigerant steam channel to connect with the second generator the second generator again
Cryogen liquid pipeline is had to connect with condenser through second throttle, the second generator also has refrigerant steam channel to connect with condenser,
Form first kind thermal drivers compressing-absorbing type heat pump.
17. first kind thermal drivers compressing-absorbing type heat pumps, be the described arbitrary first kind thermal drivers compression of 11-16 item-
In absorption heat pump, increase heater, after gas turbine is had blast tube to connect with generator, generator has combustion gas to lead to again
Road and ft connection are adjusted to heater after gas turbine has blast tube to be sequentially communicated generator and heater combustion gas again
Passage and ft connection, heater also has heated medium passage and ft connection, forms first kind thermal drivers compressing-absorbing type
Heat pump.
18. first kind thermal drivers compressing-absorbing type heat pumps, be the described arbitrary first kind thermal drivers compression of 11-16 item-
In absorption heat pump, increase heater, after gas turbine is had blast tube to connect with generator, generator has combustion gas to lead to again
Road and ft connection are adjusted to gas turbine has blast tube to be sequentially communicated the finisher of generator, heater and evaporimeter again
Have blast tube and ft connection, heater also has heated medium passage and ft connection, formed the compression of first kind thermal drivers-
Absorption heat pump.
19. first kind thermal drivers compressing-absorbing type heat pumps, be the described arbitrary first kind thermal drivers compression of 11-16 item-
In absorption heat pump, after gas turbine is had blast tube to connect with generator, generator has blast tube and ft connection again
Being adjusted to the second generator after gas turbine has blast tube to be sequentially communicated generator and the second generator has blast tube again
With ft connection, form first kind thermal drivers compressing-absorbing type heat pump.
20. first kind thermal drivers compressing-absorbing type heat pumps, be the described arbitrary first kind thermal drivers compression of 11-16 item-
In absorption heat pump, increase heater, after gas turbine is had blast tube to connect with generator, generator has combustion gas to lead to again
Road and ft connection are adjusted to gas turbine has blast tube to be sequentially communicated heat supply after generator, the second generator and heater
Device has blast tube and ft connection again, and heater also has heated medium passage and ft connection, forms first kind thermal drivers
Compressing-absorbing type heat pump.
21. first kind thermal drivers compressing-absorbing type heat pumps, be the described arbitrary first kind thermal drivers compression of 11-16 item-
In absorption heat pump, increase heater, after gas turbine is had blast tube to connect with generator, generator has combustion gas to lead to again
Road and ft connection are adjusted to gas turbine has blast tube to be sequentially communicated generator, the second generator, heater and evaporimeter
Finisher have blast tube and ft connection again, heater also has heated medium passage and ft connection, forms first
Class thermal drivers compressing-absorbing type heat pump.
22. first kind thermal drivers compressing-absorbing type heat pumps, be arbitrary first kind thermal drivers compression described in 1-8 item-
In absorption heat pump, increase the second generator, the second absorber, the second solution pump and the second solution heat exchanger, by evaporimeter
There is refrigerant steam channel to connect with absorber to be adjusted to evaporimeter and have refrigerant steam channel to connect with the second absorber, the second absorption
Device also has weak solution pipeline to connect with the second generator through the second solution pump and the second solution heat exchanger, and the second generator also has
Concentrated solution pipeline is connected with the second absorber through the second solution heat exchanger, and the second generator also has refrigerant steam channel and absorption
Device connects, and after gas turbine is had blast tube to connect with generator, generator has blast tube to be adjusted to ft connection again
After gas turbine has blast tube to be sequentially communicated generator and the second generator, the second generator has blast tube and outside again
Connection, the second absorber also has heated medium passage and ft connection, forms first kind thermal drivers compressing-absorbing type heat pump.
23. first kind thermal drivers compressing-absorbing type heat pumps, be arbitrary first kind thermal drivers compression described in 1-8 item-
In absorption heat pump, increase the second generator, the second absorber, the second solution pump, solution choke valve, the second solution choke valve and
Point steam chest, by absorber have weak solution pipeline connect with generator through solution pump and solution heat exchanger be adjusted to absorber have dilute
Solution line is connected with the second absorber with solution heat exchanger through solution pump, and the second absorber also has weak solution pipeline through solution
Choke valve is connected with the second generator, and the second generator has concentrated solution pipeline to connect with generator through the second solution pump again, will send out
Raw device has concentrated solution pipeline to connect with absorber through solution heat exchanger to be adjusted to generator and have concentrated solution pipeline through the second solution
Choke valve and the second absorber are connected with a point steam chest, and a point steam chest has concentrated solution pipeline through solution heat exchanger with absorber even again
Logical, generator there is is refrigerant steam channel connect with compressor and is adjusted to generator and has refrigerant steam channel and the second absorber company
Logical, the second generator and a point steam chest also have refrigerant steam channel to connect with compressor respectively, by gas turbine have blast tube and
After generator connection, generator has blast tube and ft connection to be adjusted to gas turbine and have blast tube to be sequentially communicated again and sends out
After raw device and the second generator, the second generator has blast tube and ft connection again, forms first kind thermal drivers compression-suction
Receipts formula heat pump.
24. first kind thermal drivers compressing-absorbing type heat pumps, mainly by absorber, generator, condenser, evaporimeter, throttling
Valve, solution pump, solution heat exchanger, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor, decompressor and
High temperature regenerator is formed;Absorber has weak solution pipeline to connect with generator with solution heat exchanger through solution pump, generator
Concentrated solution pipeline is also had to connect with absorber through solution heat exchanger, generator also has refrigerant steam channel to connect with compressor,
Compressor also has refrigerant steam channel to connect with condenser, and condenser also has cryogen liquid pipeline to connect with evaporimeter through choke valve,
Evaporimeter also has refrigerant steam channel to connect with absorber, and outside has air duct to connect with the second compressor, the second compressor
Also has compressed air channel through high temperature regenerator and combustion chamber, combustion chamber also has fuel channel and ft connection, combustion chamber
Blast tube is also had to connect with gas turbine, after gas turbine also has blast tube to be sequentially communicated high temperature regenerator and generator
Generator has blast tube and ft connection again, and outside also have low-temperature heat medium passage to connect with the 3rd compressor, the 3rd compression
Machine also has low-temperature heat medium passage to connect with decompressor through evaporimeter, and decompressor also has low-temperature heat medium passage and ft connection,
Absorber and condenser also have respectively heated medium pipeline and ft connection, gas turbine and decompressor connect compressor, the
Two compressors and the 3rd compressor simultaneously transmit power, form first kind thermal drivers compressing-absorbing type heat pump.
25. first kind thermal drivers compressing-absorbing type heat pumps, mainly by absorber, generator, condenser, evaporimeter, throttling
Valve, solution pump, solution heat exchanger, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor, decompressor,
Four compressors and high temperature regenerator are formed;Absorber has weak solution pipeline to connect with generator through solution pump and solution heat exchanger
Logical, generator also has concentrated solution pipeline to connect with absorber through solution heat exchanger, and generator also has refrigerant steam channel and pressure
Contracting machine connects, and compressor also has refrigerant steam channel to connect with condenser, and condenser also has cryogen liquid pipeline through choke valve and steaming
Send out device connection, evaporimeter also has refrigerant steam channel to connect with absorber, and outside has air duct to connect with the second compressor, the
Two compressors also have compressed air channel through high temperature regenerator and combustion chamber, and combustion chamber also has fuel channel to connect with outside
Logical, combustion chamber also has blast tube to connect with gas turbine, gas turbine also have blast tube be sequentially communicated high temperature regenerator with
After generator, generator has blast tube and ft connection again, and outside also have low-temperature heat medium passage and the 3rd compressor even
Logical, the 3rd compressor also has low-temperature heat medium passage to connect with the 4th compressor through evaporimeter, and the 4th compressor also has Low Temperature Thermal
Medium channel is connected with decompressor through evaporimeter, and decompressor also has low-temperature heat medium passage and ft connection, absorber and condensation
Device also has heated medium pipeline and ft connection respectively, gas turbine and decompressor connect compressor, the second compressor, the 3rd
Compressor and the 4th compressor simultaneously transmit power, form first kind thermal drivers compressing-absorbing type heat pump.
26. first kind thermal drivers compressing-absorbing type heat pumps, mainly by absorber, generator, condenser, evaporimeter, throttling
Valve, solution pump, solution heat exchanger, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor, decompressor, return
Hot device and high temperature regenerator are formed;Absorber has weak solution pipeline to connect with generator with solution heat exchanger through solution pump,
Generator also has concentrated solution pipeline to connect with absorber through solution heat exchanger, and generator also has refrigerant steam channel and compressor
Connection, compressor also has refrigerant steam channel to connect with condenser, and condenser also has cryogen liquid pipeline through choke valve and evaporimeter
Connection, evaporimeter also has refrigerant steam channel to connect with absorber, and outside has air duct to connect with the second compressor, the second pressure
Contracting machine also has compressed air channel through high temperature regenerator and combustion chamber, and combustion chamber also has fuel channel and ft connection, combustion
Burning room also has blast tube to connect with gas turbine, and gas turbine also has blast tube to be sequentially communicated high temperature regenerator and generator
Generator has blast tube and ft connection more afterwards, and outside also have low-temperature heat medium passage to connect through regenerator and the 3rd compressor
Logical, the 3rd compressor also has low-temperature heat medium passage to connect with decompressor with regenerator through evaporimeter, and decompressor also has Low Temperature Thermal
Medium channel and ft connection, absorber and condenser also have heated medium pipeline and ft connection respectively, gas turbine and
Decompressor connects compressor, the second compressor and the 3rd compressor and transmits power, forms first kind thermal drivers compressing-absorbing type
Heat pump.
27. first kind thermal drivers compressing-absorbing type heat pumps, mainly by absorber, generator, condenser, evaporimeter, throttling
Valve, solution pump, solution heat exchanger, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor, decompressor, low
Temperature heat exchanger and high temperature regenerator are formed;Absorber has weak solution pipeline through solution pump and solution heat exchanger and generator
Connection, generator also has concentrated solution pipeline to connect with absorber through solution heat exchanger, generator also have refrigerant steam channel and
Compressor connects, and compressor also has refrigerant steam channel to connect with condenser, condenser also have cryogen liquid pipeline through choke valve and
Evaporimeter connects, and evaporimeter also has refrigerant steam channel to connect with absorber, and outside has air duct to connect with the second compressor,
Second compressor also has compressed air channel through high temperature regenerator and combustion chamber, and combustion chamber also has fuel channel to connect with outside
Logical, combustion chamber also has blast tube to connect with gas turbine, gas turbine also have blast tube be sequentially communicated high temperature regenerator with
After generator, generator has blast tube and ft connection again, and the 3rd compressor has circulatory mediator passage through evaporimeter and expansion
Machine connects, and decompressor also has circulatory mediator passage to connect with the 3rd compressor through low temperature heat exchanger, and absorber and condenser are also
There are heated medium pipeline and ft connection respectively, low temperature heat exchanger also has low-temperature heat medium passage and ft connection, combustion gas
Turbine and decompressor connect compressor, the second compressor and the 3rd compressor and transmit power, and formation first kind thermal drivers compression-
Absorption heat pump.
28. first kind thermal drivers compressing-absorbing type heat pumps, mainly by absorber, generator, condenser, evaporimeter, throttling
Valve, solution pump, solution heat exchanger, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor and high temperature backheat
Device is formed;Absorber has weak solution pipeline to connect with generator with solution heat exchanger through solution pump, and generator also has dense molten
Liquid pipeline is connected with absorber through solution heat exchanger, and generator also has refrigerant steam channel to connect with compressor, and compressor is also
Refrigerant steam channel is had to connect with condenser, condenser also has cryogen liquid pipeline to connect with evaporimeter through choke valve, and evaporimeter is also
Refrigerant steam channel is had to connect with absorber, outside has air duct to connect with the second compressor, the second compressor also has compression
Through high temperature regenerator and combustion chamber, combustion chamber also has fuel channel and ft connection to air duct, and combustion chamber also has combustion gas
Passage is connected with gas turbine, gas turbine also have blast tube to be sequentially communicated high temperature regenerator and generator after generator again
There are blast tube and ft connection, outside also have low-temperature heat medium passage to connect with the 3rd compressor, and the 3rd compressor is also low
Through evaporimeter and ft connection, absorber and condenser also have heated medium pipeline and outside to connect to warm passage respectively
Logical, gas turbine connects compressor, the second compressor and the 3rd compressor and transmits power, and formation first kind thermal drivers compression-
Absorption heat pump.
29. first kind thermal drivers compressing-absorbing type heat pumps, mainly by absorber, generator, condenser, evaporimeter, throttling
Valve, solution pump, solution heat exchanger, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor, Low Temperature Thermal are handed over
Parallel operation, cryogenic throttle valve and high temperature regenerator are formed;Absorber have weak solution pipeline through solution pump and solution heat exchanger with
Generator connects, and generator also has concentrated solution pipeline to connect with absorber through solution heat exchanger, and generator also has refrigerant vapour
Passage is connected with compressor, and compressor also has refrigerant steam channel to connect with condenser, and condenser also has cryogen liquid pipeline warp knuckle
Stream valve is connected with evaporimeter, and evaporimeter also has refrigerant steam channel to connect with absorber, and there are air duct and the second compression in outside
Machine connects, and the second compressor also has compressed air channel through high temperature regenerator and combustion chamber, and combustion chamber also has fuel channel
With ft connection, combustion chamber also has blast tube to connect with gas turbine, and gas turbine also has blast tube to be sequentially communicated high temperature
After regenerator and generator, generator has blast tube and ft connection again, and the 3rd compressor has circulatory mediator passage through evaporation
Device is connected with low temperature heat exchanger with cryogenic throttle valve, and low temperature heat exchanger also has circulatory mediator passage and the 3rd compressor even
Lead to, absorber and condenser also have heated medium pipeline and ft connection respectively, and low temperature heat exchanger also has low temperature heat exchange
Device passage and ft connection, gas turbine connects compressor, the second compressor and the 3rd compressor and transmits power, forms first
Class thermal drivers compressing-absorbing type heat pump.
30. first kind thermal drivers compressing-absorbing type heat pumps, mainly by absorber, generator, condenser, evaporimeter, throttling
Valve, solution pump, solution heat exchanger, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor, the 4th compression
Machine, low temperature heat exchanger, cryogenic throttle valve and high temperature regenerator are formed;Absorber has weak solution pipeline through solution pump and solution
Heat exchanger is connected with generator, and generator also has concentrated solution pipeline to connect with absorber through solution heat exchanger, and generator is also
Refrigerant steam channel is had to connect with compressor, compressor also has refrigerant steam channel to connect with condenser, and condenser also has cryogen
Liquid pipeline is connected with evaporimeter through choke valve, and evaporimeter also has refrigerant steam channel to connect with absorber, and there is air duct outside
Connect with the second compressor, the second compressor also has compressed air channel through high temperature regenerator and combustion chamber, and combustion chamber is also
Have fuel channel and ft connection, combustion chamber also has blast tube to connect with gas turbine, gas turbine also have blast tube according to
After secondary connection high temperature regenerator and generator, generator has blast tube and ft connection again, and the 3rd compressor has circulatory mediator
Passage is connected with the 4th compressor through evaporimeter, the 4th compressor also have circulatory mediator passage through evaporimeter and cryogenic throttle valve with
Low temperature heat exchanger connects, and low temperature heat exchanger also has circulatory mediator passage to connect with the 3rd compressor, absorber and condenser
Also there are heated medium pipeline and ft connection respectively, low temperature heat exchanger also has low temperature heat exchanger passage and ft connection,
Gas turbine connects compressor, the second compressor, the 3rd compressor and the 4th compressor and transmits power, forms first kind heat and drives
Dynamic pressure contracting-absorption heat pump.
31. first kind thermal drivers compressing-absorbing type heat pumps, be the described arbitrary first kind thermal drivers compression of 24-30 item-
In absorption heat pump, cancel the outside fuel channel with combustion chamber, increase new compressor, the outside fuel gas that increases leads to
Road is connected with new compressor, and new compressor also has compressed gaseous fuel channel and combustion chamber, and gas turbine connects new
Increase compressor and transmit power, form first kind thermal drivers compressing-absorbing type heat pump.
32. first kind thermal drivers compressing-absorbing type heat pumps, be the described arbitrary first kind thermal drivers compression of 24-31 item-
In absorption heat pump, increase heater, gas turbine is had blast tube to send out after being sequentially communicated high temperature regenerator and generator
Raw device have again blast tube and ft connection be adjusted to gas turbine have blast tube be sequentially communicated high temperature regenerator, generator and
After heater, heater has blast tube and ft connection again, and heater also has heated medium passage and ft connection, shape
Become first kind thermal drivers compressing-absorbing type heat pump.
33. first kind thermal drivers compressing-absorbing type heat pumps, be the described arbitrary first kind thermal drivers compression of 24-31 item-
In absorption heat pump, increase heater, gas turbine is had blast tube to send out after being sequentially communicated high temperature regenerator and generator
Raw device have again blast tube and ft connection be adjusted to gas turbine have blast tube be sequentially communicated high temperature regenerator, generator,
The finisher of heater and evaporimeter has blast tube and ft connection again, and heater also has heated medium passage and outside
Connection, forms first kind thermal drivers compressing-absorbing type heat pump.
34. first kind thermal drivers compressing-absorbing type heat pumps, be the described arbitrary first kind thermal drivers compression of 24-31 item-
In absorption heat pump, increase the second generator, second throttle, the second solution pump and the second solution heat exchanger, absorber increases
If weak solution pipeline is connected with the second generator through the second solution pump and the second solution heat exchanger, the second generator also has dense molten
Liquid pipeline is connected with absorber through the second solution heat exchanger, generator is had refrigerant steam channel to connect with compressor and is adjusted to
After generator has refrigerant steam channel to connect with the second generator, the second generator has cryogen liquid pipeline again through second throttle
Connect with condenser, the second generator also has refrigerant steam channel to connect with compressor, form first kind thermal drivers compression-absorption
Formula heat pump.
35. first kind thermal drivers compressing-absorbing type heat pumps, be the described arbitrary first kind thermal drivers compression of 24-31 item-
In absorption heat pump, increase the second generator, second throttle and the second solution heat exchanger, absorber is had weak solution pipeline
Connect with generator through solution pump and solution heat exchanger and be adjusted to absorber and have weak solution pipeline through solution pump, solution heat exchange
Device and the second solution heat exchanger are connected with generator, and generator is had concentrated solution pipeline through solution heat exchanger with absorber even
Logical be adjusted to generator and have concentrated solution pipeline to connect with the second generator through the second solution heat exchanger, the second generator has dense again
Solution line is connected with absorber through solution heat exchanger, by generator have refrigerant steam channel connect with compressor be adjusted to send out
Raw device have refrigerant steam channel to connect with the second generator after the second generator have cryogen liquid pipeline through second throttle again and
Condenser connects, and the second generator also has refrigerant steam channel to connect with compressor, forms first kind thermal drivers compressing-absorbing type
Heat pump.
36. first kind thermal drivers compressing-absorbing type heat pumps, be the described arbitrary first kind thermal drivers compression of 24-31 item-
In absorption heat pump, increase the second generator, second throttle, the second solution pump and the second solution heat exchanger, by absorber
There is weak solution pipeline to connect with generator through solution pump and solution heat exchanger to be adjusted to absorber and have weak solution pipeline through solution
Pump is connected with the second generator with solution heat exchanger, and the second generator has concentrated solution pipeline molten through the second solution pump and second again
Liquid heat exchanger is connected with generator, by generator have concentrated solution pipeline connect with absorber through solution heat exchanger be adjusted to send out
Raw device has concentrated solution pipeline to connect with absorber with solution heat exchanger through the second solution heat exchanger, and generator is had cryogen to steam
Vapour passage is connected with compressor and is adjusted to after generator has refrigerant steam channel to connect with the second generator the second generator again
Cryogen liquid pipeline is had to connect with condenser through second throttle, the second generator also has refrigerant steam channel to connect with compressor,
Form first kind thermal drivers compressing-absorbing type heat pump.
37. first kind thermal drivers compressing-absorbing type heat pumps, be the described arbitrary first kind thermal drivers compression of 24-31 item-
In absorption heat pump, increase the second generator, second throttle, the second solution pump and the second solution heat exchanger, absorber increases
If weak solution pipeline is connected with the second generator through the second solution pump and the second solution heat exchanger, the second generator also has dense molten
Liquid pipeline is connected with absorber through the second solution heat exchanger, compressor is had refrigerant steam channel to connect with condenser and is adjusted to
After compressor has refrigerant steam channel to connect with the second generator, the second generator has cryogen liquid pipeline again through second throttle
Connect with condenser, the second generator also has refrigerant steam channel to connect with condenser, form first kind thermal drivers compression-absorption
Formula heat pump.
38. first kind thermal drivers compressing-absorbing type heat pumps, be the described arbitrary first kind thermal drivers compression of 24-31 item-
In absorption heat pump, increase the second generator, second throttle and the second solution heat exchanger, absorber is had weak solution pipeline
Connect with generator through solution pump and solution heat exchanger and be adjusted to absorber and have weak solution pipeline through solution pump, solution heat exchange
Device and the second solution heat exchanger are connected with generator, and generator is had concentrated solution pipeline through solution heat exchanger with absorber even
Logical be adjusted to generator and have concentrated solution pipeline to connect with the second generator through the second solution heat exchanger, the second generator has dense again
Solution line is connected with absorber through solution heat exchanger, compressor is had refrigerant steam channel to connect with condenser and is adjusted to pressure
Contracting machine have refrigerant steam channel to connect with the second generator after the second generator have again cryogen liquid pipeline through second throttle with
Condenser connects, and the second generator also has refrigerant steam channel to connect with condenser, forms first kind thermal drivers compressing-absorbing type
Heat pump.
39. first kind thermal drivers compressing-absorbing type heat pumps, be the described arbitrary first kind thermal drivers compression of 24-31 item-
In absorption heat pump, increase the second generator, second throttle, the second solution pump and the second solution heat exchanger, by absorber
There is weak solution pipeline to connect with generator through solution pump and solution heat exchanger to be adjusted to absorber and have weak solution pipeline through solution
Pump is connected with the second generator with solution heat exchanger, and the second generator has concentrated solution pipeline molten through the second solution pump and second again
Liquid heat exchanger is connected with generator, by generator have concentrated solution pipeline connect with absorber through solution heat exchanger be adjusted to send out
Raw device has concentrated solution pipeline to connect with absorber with solution heat exchanger through the second solution heat exchanger, and compressor is had cryogen to steam
Vapour passage is connected with condenser and is adjusted to after compressor has refrigerant steam channel to connect with the second generator the second generator again
Cryogen liquid pipeline is had to connect with condenser through second throttle, the second generator also has refrigerant steam channel to connect with condenser,
Form first kind thermal drivers compressing-absorbing type heat pump.
40. first kind thermal drivers compressing-absorbing type heat pumps, be the described arbitrary first kind thermal drivers compression of 34-39 item-
In absorption heat pump, increase heater, by gas turbine have blast tube be sequentially communicated high temperature regenerator and generator after
Generator has blast tube and ft connection to be adjusted to gas turbine again has blast tube to be sequentially communicated high temperature regenerator, generator
There are blast tube and ft connection with heater after heater again, heater also has heated medium passage and ft connection,
Form first kind thermal drivers compressing-absorbing type heat pump.
41. first kind thermal drivers compressing-absorbing type heat pumps, be the described arbitrary first kind thermal drivers compression of 34-39 item-
In absorption heat pump, increase heater, by gas turbine have blast tube be sequentially communicated high temperature regenerator and generator after
Generator has blast tube and ft connection to be adjusted to gas turbine again has blast tube to be sequentially communicated high temperature regenerator, generation
The finisher of device, heater and evaporimeter has blast tube and ft connection again, heater also have heated medium passage with
Ft connection, forms first kind thermal drivers compressing-absorbing type heat pump.
42. first kind thermal drivers compressing-absorbing type heat pumps, be the described arbitrary first kind thermal drivers compression of 34-39 item-
In absorption heat pump, after gas turbine is had blast tube to be sequentially communicated high temperature regenerator and generator, generator has combustion gas again
Passage and ft connection be adjusted to gas turbine have blast tube be sequentially communicated high temperature regenerator, generator and the second generator it
Second generator has blast tube and ft connection more afterwards, forms first kind thermal drivers compressing-absorbing type heat pump.
43. first kind thermal drivers compressing-absorbing type heat pumps, be the described arbitrary first kind thermal drivers compression of 34-39 item-
In absorption heat pump, increase heater, gas turbine is had blast tube to send out after being sequentially communicated high temperature regenerator and generator
Raw device have again blast tube and ft connection be adjusted to gas turbine have blast tube be sequentially communicated high temperature regenerator, generator,
After second generator and heater, heater has blast tube and ft connection again, heater also have heated medium passage with
Ft connection, forms first kind thermal drivers compressing-absorbing type heat pump.
44. first kind thermal drivers compressing-absorbing type heat pumps, be the described arbitrary first kind thermal drivers compression of 34-39 item-
In absorption heat pump, increase heater, gas turbine is had blast tube to send out after being sequentially communicated high temperature regenerator and generator
Raw device have again blast tube and ft connection be adjusted to gas turbine have blast tube be sequentially communicated high temperature regenerator, generator,
The finisher of the second generator, heater and evaporimeter has blast tube and ft connection again, and heater also has heated Jie
Matter passage and ft connection, form first kind thermal drivers compressing-absorbing type heat pump.
45. first kind thermal drivers compressing-absorbing type heat pumps, be the described arbitrary first kind thermal drivers compression of 23-30 item-
In absorption heat pump, increase the second generator, the second absorber, the second solution pump and the second solution heat exchanger, by evaporimeter
There is refrigerant steam channel to connect with absorber to be adjusted to evaporimeter and have refrigerant steam channel to connect with the second absorber, the second absorption
Device also has weak solution pipeline to connect with the second generator through the second solution pump and the second solution heat exchanger, and the second generator also has
Concentrated solution pipeline is connected with the second absorber through the second solution heat exchanger, and the second generator also has refrigerant steam channel and absorption
Device connect, after gas turbine is had blast tube to be sequentially communicated high temperature regenerator and generator generator have again blast tube with
Ft connection is adjusted to gas turbine has blast tube to be sequentially communicated second after high temperature regenerator, generator and the second generator
Generator has blast tube and ft connection again, and the second absorber also has heated medium passage and ft connection, forms first
Class thermal drivers compressing-absorbing type heat pump.
46. first kind thermal drivers compressing-absorbing type heat pumps, be the described arbitrary first kind thermal drivers compression of 23-30 item-
In absorption heat pump, increase the second generator, the second absorber, the second solution pump, solution choke valve, the second solution choke valve and
Point steam chest, by absorber have weak solution pipeline connect with generator through solution pump and solution heat exchanger be adjusted to absorber have dilute
Solution line is connected with the second absorber with solution heat exchanger through solution pump, and the second absorber also has weak solution pipeline through solution
Choke valve is connected with the second generator, and the second generator has concentrated solution pipeline to connect with generator through the second solution pump again, will send out
Raw device has concentrated solution pipeline to connect with absorber through solution heat exchanger to be adjusted to generator and have concentrated solution pipeline through the second solution
Choke valve and the second absorber are connected with a point steam chest, and a point steam chest has concentrated solution pipeline through solution heat exchanger with absorber even again
Logical, generator there is is refrigerant steam channel connect with compressor and is adjusted to generator and has refrigerant steam channel and the second absorber company
Logical, the second generator and divide a steam chest also to have refrigerant steam channel to connect with compressor respectively, by gas turbine have blast tube according to
After secondary connection high temperature regenerator and generator, generator has blast tube and ft connection to be adjusted to gas turbine again and has combustion gas
After passage is sequentially communicated high temperature regenerator, generator and the second generator, the second generator has blast tube and outside to connect again
Logical, form first kind thermal drivers compressing-absorbing type heat pump.
47. first kind thermal drivers compressing-absorbing type heat pumps, be the described arbitrary first kind thermal drivers compression of 1-46 item-
In absorption heat pump, increase engine, engine connects the 3rd compressor and transmits power to the 3rd compressor, formed additional outer
Portion's power-actuated first kind thermal drivers compressing-absorbing type heat pump.
48. first kind thermal drivers compressing-absorbing type heat pumps, be the described arbitrary first kind thermal drivers compression of 1-46 item-
In absorption heat pump, increase working machine, gas turbine connects working machine and transmits power to working machine, being formed to add externally provides
The first kind thermal drivers compressing-absorbing type heat pump of living load.
Brief description:
Fig. 1 is according to the 1st kind of principled thermal system of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention
Figure.
Fig. 2 is according to the 2nd kind of principled thermal system of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention
Figure.
Fig. 3 is according to the 3rd kind of principled thermal system of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention
Figure.
Fig. 4 is according to the 4th kind of principled thermal system of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention
Figure.
Fig. 5 is according to the 5th kind of principled thermal system of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention
Figure.
Fig. 6 is according to the 6th kind of principled thermal system of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention
Figure.
Fig. 7 is according to the 7th kind of principled thermal system of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention
Figure.
Fig. 8 is according to the 8th kind of principled thermal system of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention
Figure.
Fig. 9 is according to the 9th kind of principled thermal system of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention
Figure.
Figure 10 is according to the 10th kind of principle heating power system of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention
System figure.
Figure 11 is according to the 11st kind of principle heating power system of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention
System figure.
Figure 12 is according to the 12nd kind of principle heating power system of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention
System figure.
Figure 13 is according to the 13rd kind of principle heating power system of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention
System figure.
Figure 14 is according to the 14th kind of principle heating power system of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention
System figure.
Figure 15 is according to the 15th kind of principle heating power system of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention
System figure.
Figure 16 is according to the 16th kind of principle heating power system of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention
System figure.
Figure 17 is according to the 17th kind of principle heating power system of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention
System figure.
In figure, 1- absorber, 2- generator, 3- condenser, 4- evaporimeter, 5- choke valve, 6- solution pump, 7- solution heat is handed over
Parallel operation, 8- compressor, 9- second compressor, 10- combustion chamber, 11- gas turbine, 12- the 3rd compressor, 13- decompressor, 14-
4th compressor, 15- regenerator, 16- low temperature heat exchanger, 17- cryogenic throttle valve, 18- new compressor, 19- heater,
20- high temperature regenerator, 21- second generator, 22- second throttle, 23- the second solution pump, 24- second solution heat exchanger,
25- second absorber, 26- solution choke valve, 27- the second solution choke valve, 28- divides steam chest.
Specific embodiment:
First it is noted that in the statement of structure and flow process, inessential in the case of do not repeat;To apparent
Flow process do not state.To describe the present invention with example in detail below in conjunction with the accompanying drawings.
First kind thermal drivers compressing-absorbing type heat pump shown in Fig. 1 is realized in:
(1), in structure, it is mainly handed over by absorber, generator, condenser, evaporimeter, choke valve, solution pump, solution heat
Parallel operation, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor and decompressor are formed;Absorber 1 has dilute molten
Liquid pipeline is connected with generator 2 with solution heat exchanger 7 through solution pump 6, and generator 2 also has concentrated solution pipeline through solution heat exchange
Device 7 is connected with absorber 1, and generator 2 also has refrigerant steam channel to connect with compressor 8, and compressor 8 also has refrigerant steam channel
Connect with condenser 3, condenser 3 also has cryogen liquid pipeline to connect with evaporimeter 4 through choke valve 5, and evaporimeter 4 also has refrigerant vapour
Passage is connected with absorber 1, and outside has air duct to connect with the second compressor 9, and the second compressor 9 also has compressed air channel
Connect with combustion chamber 10, combustion chamber 10 also has fuel channel and ft connection, combustion chamber 10 also has blast tube and gas turbine
11 connections, after gas turbine 11 also has blast tube to connect with generator 2, generator 2 has blast tube and ft connection again,
Outside also have low-temperature heat medium passage to connect with the 3rd compressor 12, and the 3rd compressor 12 also has low-temperature heat medium passage through evaporation
Device 4 is connected with decompressor 13, and decompressor 13 also has low-temperature heat medium passage and ft connection, absorber 1 and condenser 3 also to distinguish
Heated medium pipeline and ft connection, gas turbine 11 and decompressor 13 is had to connect compressor 8, the second compressor 9 and the 3rd
Compressor 12 simultaneously transmits power.
(2), in flow process, the weak solution of absorber 1 enters generator 2 through solution pump 6 and solution heat exchanger 7, and combustion gas flows through
Generator 2, heating enter its interior solution release refrigerant vapour and provide to compressor 8, and the concentrated solution of generator 2 is through solution heat
Exchanger 7 enters absorber 1, absorbs refrigerant vapour and heat release is in heated medium;Refrigerant vapour flows through compressor 8 boosting and rises
Temperature, the refrigerant vapour of compressor 8 discharge enters condenser 3, heat release becomes cryogen liquid, the cryogen liquid of condenser 3 in heated medium
Throttle through choke valve 5 and enter evaporimeter 4, absorb heat into refrigerant vapour and provide to absorber 1;Air enters 9 liters of the second compressor
Pressure heats up, and the compressed air of the second compressor 9 discharge enters combustion chamber 10, and external fuel enters combustion chamber 10 and compressed air
Mix and burn into high-temperature fuel gas, high-temperature fuel gas enter gas turbine 11 step-down work done, the combustion gas of gas turbine 11 discharge flows through
Externally discharge after generator 2 heat release cooling;Low-temperature heat medium enters the 3rd compressor 12 boosting and heats up, and flows through evaporimeter 4 simultaneously
Heat release, enters decompressor 13 step-down work done afterwards and externally discharges;The work(of gas turbine 11 and decompressor 13 output is supplied to pressure
Contracting machine 8, the second compressor 9 and the 3rd compressor 12 are used as power, and form first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Fig. 2 is realized in:
(1), in structure, it is mainly handed over by absorber, generator, condenser, evaporimeter, choke valve, solution pump, solution heat
Parallel operation, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor, decompressor and the 4th compressor are formed;Inhale
Receiving device 1 has weak solution pipeline to connect with generator 2 with solution heat exchanger 7 through solution pump 6, and generator 2 also has concentrated solution pipeline
Connect with absorber 1 through solution heat exchanger 7, generator 2 also has refrigerant steam channel to connect with compressor 8, and compressor 8 also has
Refrigerant steam channel is connected with condenser 3, and condenser 3 also has cryogen liquid pipeline to connect with evaporimeter 4 through choke valve 5, evaporimeter 4
Refrigerant steam channel is also had to connect with absorber 1, outside has air duct to connect with the second compressor 9, and the second compressor 9 also has
Compressed air channel is connected with combustion chamber 10, and combustion chamber 10 also has fuel channel and ft connection, and combustion chamber 10 also has combustion gas to lead to
Road is connected with gas turbine 11, and after gas turbine 11 also has blast tube to connect with generator 2, generator 2 has blast tube again
With ft connection, outside also have low-temperature heat medium passage to connect with the 3rd compressor 12, and the 3rd compressor 12 also has Low Temperature Thermal to be situated between
Matter passage is connected with the 4th compressor 14 through evaporimeter 4, the 4th compressor 14 also have low-temperature heat medium passage through evaporimeter 4 with swollen
Swollen machine 13 connects, and decompressor 13 also has low-temperature heat medium passage and ft connection, and absorber 1 and condenser 3 also have respectively and added
Heat medium pipeline and ft connection, gas turbine 11 and decompressor 13 connect compressor 8, the second compressor 9, the 3rd compressor 12
With the 4th compressor 14 and transmit power.
(2), in flow process, the weak solution of absorber 1 enters generator 2 through solution pump 6 and solution heat exchanger 7, and combustion gas flows through
Generator 2, heating enter its interior solution release refrigerant vapour and provide to compressor 8, and the concentrated solution of generator 2 is through solution heat
Exchanger 7 enters absorber 1, absorbs refrigerant vapour and heat release is in heated medium;Refrigerant vapour flows through compressor 8 boosting and rises
Temperature, the refrigerant vapour of compressor 8 discharge enters condenser 3, heat release becomes cryogen liquid, the cryogen liquid of condenser 3 in heated medium
Throttle through choke valve 5 and enter evaporimeter 4, absorb heat into refrigerant vapour and provide to absorber 1;Air enters 9 liters of the second compressor
Pressure heats up, and the compressed air of the second compressor 9 discharge enters combustion chamber 10, and external fuel enters combustion chamber 10 and compressed air
Mix and burn into high-temperature fuel gas, high-temperature fuel gas enter gas turbine 11 step-down work done, the combustion gas of gas turbine 11 discharge flows through
Externally discharge after generator 2 heat release cooling;Low-temperature heat medium enters the 3rd compressor 12 boosting and heats up, and flows through evaporimeter 4 and puts
Enter the 4th compressor 14 boosting after heat to heat up, the low-temperature heat medium of the 4th compressor 14 discharge flows through evaporimeter 4 heat release,
Enter decompressor 13 step-down work done afterwards and externally discharge;Gas turbine 11 and decompressor 13 output work(be supplied to compressor 8,
Second compressor 9, the 3rd compressor 12 and the 4th compressor 14 are used as power, and form first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Fig. 3 is realized in:
(1), in structure, it is mainly handed over by absorber, generator, condenser, evaporimeter, choke valve, solution pump, solution heat
Parallel operation, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor, decompressor and regenerator are formed;Absorber
1 has weak solution pipeline to connect with generator 2 with solution heat exchanger 7 through solution pump 6, and generator 2 also has concentrated solution pipeline through molten
Liquid heat exchanger 7 is connected with absorber 1, and generator 2 also has refrigerant steam channel to connect with compressor 8, and compressor 8 also has cryogen
Steam channel is connected with condenser 3, and condenser 3 also has cryogen liquid pipeline to connect with evaporimeter 4 through choke valve 5, and evaporimeter 4 also has
Refrigerant steam channel is connected with absorber 1, and outside has air duct to connect with the second compressor 9, and the second compressor 9 also has compression
Air duct is connected with combustion chamber 10, combustion chamber 10 also have fuel channel and ft connection, combustion chamber 10 also have blast tube with
Gas turbine 11 connects, and after gas turbine 11 also has blast tube to connect with generator 2, generator 2 has blast tube again with outward
Portion connects, and outside also have low-temperature heat medium passage to connect with the 3rd compressor 12 through regenerator 15, and the 3rd compressor 12 is also low
Warm passage is connected with decompressor 13 with regenerator 15 through evaporimeter 4, and decompressor 13 also has low-temperature heat medium passage with outward
Portion connects, and absorber 1 and condenser 3 also have heated medium pipeline and ft connection, gas turbine 11 and decompressor 13 respectively
Connect compressor 8, the second compressor 9 and the 3rd compressor 12 and transmit power.
(2), in flow process, the weak solution of absorber 1 enters generator 2 through solution pump 6 and solution heat exchanger 7, and combustion gas flows through
Generator 2, heating enter its interior solution release refrigerant vapour and provide to compressor 8, and the concentrated solution of generator 2 is through solution heat
Exchanger 7 enters absorber 1, absorbs refrigerant vapour and heat release is in heated medium;Refrigerant vapour flows through compressor 8 boosting and rises
Temperature, the refrigerant vapour of compressor 8 discharge enters condenser 3, heat release becomes cryogen liquid, the cryogen liquid of condenser 3 in heated medium
Throttle through choke valve 5 and enter evaporimeter 4, absorb heat into refrigerant vapour and provide to absorber 1;Air enters 9 liters of the second compressor
Pressure heats up, and the compressed air of the second compressor 9 discharge enters combustion chamber 10, and external fuel enters combustion chamber 10 and compressed air
Mix and burn into high-temperature fuel gas, high-temperature fuel gas enter gas turbine 11 step-down work done, the combustion gas of gas turbine 11 discharge flows through
Externally discharge after generator 2 heat release cooling;Low-temperature heat medium flows through regenerator 15 and absorbs heat, and enters the 3rd compressor 12 afterwards
Boosting heats up;The low-temperature heat medium of the 3rd compressor 12 discharge flows through evaporimeter 4 and regenerator 15 progressively heat release, afterwards successively
Enter decompressor 13 step-down work done and externally discharge;The work(of gas turbine 11 and decompressor 13 output is supplied to compressor 8, second
Compressor 9 and the 3rd compressor 12 are used as power, and form first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Fig. 4 is realized in:
(1), in structure, it is mainly handed over by absorber, generator, condenser, evaporimeter, choke valve, solution pump, solution heat
Parallel operation, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor, decompressor and low temperature heat exchanger are formed;
Absorber 1 has weak solution pipeline to connect with generator 2 with solution heat exchanger 7 through solution pump 6, and generator 2 also has concentrated solution pipe
Road is connected with absorber 1 through solution heat exchanger 7, and generator 2 also has refrigerant steam channel to connect with compressor 8, and compressor 8 is also
Refrigerant steam channel is had to connect with condenser 3, condenser 3 also has cryogen liquid pipeline to connect with evaporimeter 4 through choke valve 5, evaporation
Device 4 also has refrigerant steam channel to connect with absorber 1, and outside has air duct to connect with the second compressor 9, the second compressor 9
Compressed air channel is also had to connect with combustion chamber 10, combustion chamber 10 also has fuel channel and ft connection, combustion chamber 10 also has fires
Gas passage is connected with gas turbine 11, and after gas turbine 11 also has blast tube to connect with generator 2, generator 2 has combustion gas again
Passage and ft connection, the 3rd compressor 12 has circulatory mediator passage to connect with decompressor 13 through evaporimeter 4, and decompressor 13 also has
Circulatory mediator passage is connected with the 3rd compressor 12 through low temperature heat exchanger 16, and absorber 1 and condenser 3 also have heated respectively
Medium pipeline and ft connection, low temperature heat exchanger 16 also has low-temperature heat medium passage and ft connection, gas turbine 11 and swollen
Swollen machine 13 connects compressor 8, the second compressor 9 and the 3rd compressor 12 and transmits power.
(2), in flow process, the weak solution of absorber 1 enters generator 2 through solution pump 6 and solution heat exchanger 7, and combustion gas flows through
Generator 2, heating enter its interior solution release refrigerant vapour and provide to compressor 8, and the concentrated solution of generator 2 is through solution heat
Exchanger 7 enters absorber 1, absorbs refrigerant vapour and heat release is in heated medium;Refrigerant vapour flows through compressor 8 boosting and rises
Temperature, the refrigerant vapour of compressor 8 discharge enters condenser 3, heat release becomes cryogen liquid, the cryogen liquid of condenser 3 in heated medium
Throttle through choke valve 5 and enter evaporimeter 4, absorb heat into refrigerant vapour and provide to absorber 1;Air enters 9 liters of the second compressor
Pressure heats up, and the compressed air of the second compressor 9 discharge enters combustion chamber 10, and external fuel enters combustion chamber 10 and compressed air
Mix and burn into high-temperature fuel gas, high-temperature fuel gas enter gas turbine 11 step-down work done, the combustion gas of gas turbine 11 discharge flows through
Externally discharge after generator 2 heat release cooling;The cycle fluid of the 3rd compressor 12 discharge flows through evaporimeter 4 heat release, afterwards
Enter decompressor 13 step-down work done;The cycle fluid of decompressor 13 discharge flows through low temperature heat exchanger 16 and absorbs heat, and enters afterwards
3rd compressor 12 boosting heats up;The work(of gas turbine 11 and decompressor 13 output is supplied to compressor 8, the second compressor 9 and
3rd compressor 12 is used as power, and forms first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Fig. 5 is realized in:
(1), in structure, it is mainly handed over by absorber, generator, condenser, evaporimeter, choke valve, solution pump, solution heat
Parallel operation, compressor, the second compressor, combustion chamber, gas turbine and the 3rd compressor are formed;Absorber 1 has weak solution pipeline
Connect with generator 2 with solution heat exchanger 7 through solution pump 6, generator 2 also have concentrated solution pipeline through solution heat exchanger 7 with
Absorber 1 connects, and generator 2 also has refrigerant steam channel to connect with compressor 8, compressor 8 also refrigerant steam channel with cold
Condenser 3 connects, and condenser 3 also has cryogen liquid pipeline to connect with evaporimeter 4 through choke valve 5, and evaporimeter 4 also has refrigerant steam channel
Connect with absorber 1, outside has air duct to connect with the second compressor 9, the second compressor 9 also has compressed air channel and combustion
Burn room 10 to connect, combustion chamber 10 also has fuel channel and ft connection, combustion chamber 10 also has blast tube with gas turbine 11 even
Logical, after gas turbine 11 also has blast tube to connect with generator 2, generator 2 has blast tube and ft connection again, outside
Low-temperature heat medium passage is also had to connect with the 3rd compressor 12, the 3rd compressor 12 also has low-temperature heat medium passage through evaporimeter 4
With ft connection, absorber 1 and condenser 3 also have heated medium pipeline and ft connection respectively, and gas turbine 11 connects pressure
Contracting machine 8, the second compressor 9 and the 3rd compressor 12 simultaneously transmit power.
(2), in flow process, the weak solution of absorber 1 enters generator 2 through solution pump 6 and solution heat exchanger 7, and combustion gas flows through
Generator 2, heating enter its interior solution release refrigerant vapour and provide to compressor 8, and the concentrated solution of generator 2 is through solution heat
Exchanger 7 enters absorber 1, absorbs refrigerant vapour and heat release is in heated medium;Refrigerant vapour flows through compressor 8 boosting and rises
Temperature, the refrigerant vapour of compressor 8 discharge enters condenser 3, heat release becomes cryogen liquid, the cryogen liquid of condenser 3 in heated medium
Throttle through choke valve 5 and enter evaporimeter 4, absorb heat into refrigerant vapour and provide to absorber 1;Air enters 9 liters of the second compressor
Pressure heats up, and the compressed air of the second compressor 9 discharge enters combustion chamber 10, and external fuel enters combustion chamber 10 and compressed air
Mix and burn into high-temperature fuel gas, high-temperature fuel gas enter gas turbine 11 step-down work done, the combustion gas of gas turbine 11 discharge flows through
Externally discharge after generator 2 heat release cooling;Outer low temperature thermal medium enters the 3rd compressor 12 boosting and heats up, and flows through evaporimeter
4 simultaneously heat releases, externally discharge afterwards;The work(of gas turbine 11 output is supplied to compressor 8, the second compressor 9 and the 3rd compressor
12 are used as power, and form first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Fig. 6 is realized in:
(1), in structure, it is mainly handed over by absorber, generator, condenser, evaporimeter, choke valve, solution pump, solution heat
Parallel operation, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor, low temperature heat exchanger and cryogenic throttle valve institute
Composition;Absorber 1 has weak solution pipeline to connect with generator 2 with solution heat exchanger 7 through solution pump 6, and generator 2 also has dense molten
Liquid pipeline is connected with absorber 1 through solution heat exchanger 7, and generator 2 also has refrigerant steam channel to connect with compressor 8, compression
Machine 8 also has refrigerant steam channel to connect with condenser 3, and condenser 3 also has cryogen liquid pipeline to connect with evaporimeter 4 through choke valve 5,
Evaporimeter 4 also has refrigerant steam channel to connect with absorber 1, and outside has air duct to connect with the second compressor 9, the second compression
Machine 9 also has compressed air channel to connect with combustion chamber 10, and combustion chamber 10 also has fuel channel and ft connection, and combustion chamber 10 also has
Blast tube is connected with gas turbine 11, and after gas turbine 11 also has blast tube to connect with generator 2, generator 2 has combustion again
Gas passage and ft connection, the 3rd compressor 12 has circulatory mediator passage to hand over Low Temperature Thermal through evaporimeter 4 and cryogenic throttle valve 17
Parallel operation 16 connects, and low temperature heat exchanger 16 also has circulatory mediator passage to connect with the 3rd compressor 12, absorber 1 and condenser 3
Also there are heated medium pipeline and ft connection respectively, low temperature heat exchanger 16 also has low temperature heat exchanger passage to connect with outside
Logical, gas turbine 11 connects compressor 8, the second compressor 9 and the 3rd compressor 12 and transmits power.
(2), in flow process, the weak solution of absorber 1 enters generator 2 through solution pump 6 and solution heat exchanger 7, and combustion gas flows through
Generator 2, heating enter its interior solution release refrigerant vapour and provide to compressor 8, and the concentrated solution of generator 2 is through solution heat
Exchanger 7 enters absorber 1, absorbs refrigerant vapour and heat release is in heated medium;Refrigerant vapour flows through compressor 8 boosting and rises
Temperature, the refrigerant vapour of compressor 8 discharge enters condenser 3, heat release becomes cryogen liquid, the cryogen liquid of condenser 3 in heated medium
Throttle through choke valve 5 and enter evaporimeter 4, absorb heat into refrigerant vapour and provide to absorber 1;Air enters 9 liters of the second compressor
Pressure heats up, and the compressed air of the second compressor 9 discharge enters combustion chamber 10, and external fuel enters combustion chamber 10 and compressed air
Mix and burn into high-temperature fuel gas, high-temperature fuel gas enter gas turbine 11 step-down work done, the combustion gas of gas turbine 11 discharge flows through
Externally discharge after generator 2 heat release cooling;The cycle fluid of the 3rd compressor 12 discharge flows through evaporimeter 4 and heat release becomes cryogen
Liquid, after through cryogenic throttle valve 17 reducing pressure by regulating flow enter low temperature heat exchanger 16;Low-temperature heat medium flow through low temperature heat exchanger 16,
Heating enters its interior cryogen liquid and becomes refrigerant vapour, and the refrigerant vapour that low temperature heat exchanger 16 produces enters 12 liters of the 3rd compressor
Pressure heats up;The work(of gas turbine 11 output is supplied to compressor 8, the second compressor 9 and the 3rd compressor 12 and is used as power, and forms the
One class thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Fig. 7 is realized in:
(1), in structure, it is mainly handed over by absorber, generator, condenser, evaporimeter, choke valve, solution pump, solution heat
Parallel operation, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor, the 4th compressor, low temperature heat exchanger and low
Warm choke valve is formed;Absorber 1 has weak solution pipeline to connect with generator 2 with solution heat exchanger 7 through solution pump 6, occurs
Device 2 also has concentrated solution pipeline to connect with absorber 1 through solution heat exchanger 7, and generator 2 also has refrigerant steam channel and compressor
8 connections, compressor 8 also has refrigerant steam channel to connect with condenser 3, and condenser 3 also has cryogen liquid pipeline through choke valve 5 and steaming
Send out device 4 to connect, evaporimeter 4 also has refrigerant steam channel to connect with absorber 1, there are air duct and the second compressor 9 in outside even
Logical, the second compressor 9 also has compressed air channel to connect with combustion chamber 10, and combustion chamber 10 also has fuel channel and ft connection,
Combustion chamber 10 also has blast tube to connect with gas turbine 11, after gas turbine 11 also has blast tube to connect with generator 2
Generator 2 has blast tube and ft connection again, and the 3rd compressor 12 has circulatory mediator passage through evaporimeter 4 and the 4th compressor
14 connections, the 4th compressor 14 also has circulatory mediator passage to connect with low temperature heat exchanger 16 through evaporimeter 4 and cryogenic throttle valve 17
Logical, low temperature heat exchanger 16 also has circulatory mediator passage to connect with the 3rd compressor 12, and absorber 1 and condenser 3 also have respectively
Heated medium pipeline and ft connection, low temperature heat exchanger 16 also has low temperature heat exchanger passage and ft connection, combustion gas wheel
Machine 11 connects compressor 8, the second compressor 9, the 3rd compressor 12 and the 4th compressor 14 and transmits power.
(2), in flow process, the weak solution of absorber 1 enters generator 2 through solution pump 6 and solution heat exchanger 7, and combustion gas flows through
Generator 2, heating enter its interior solution release refrigerant vapour and provide to compressor 8, and the concentrated solution of generator 2 is through solution heat
Exchanger 7 enters absorber 1, absorbs refrigerant vapour and heat release is in heated medium;Refrigerant vapour flows through compressor 8 boosting and rises
Temperature, the refrigerant vapour of compressor 8 discharge enters condenser 3, heat release becomes cryogen liquid, the cryogen liquid of condenser 3 in heated medium
Throttle through choke valve 5 and enter evaporimeter 4, absorb heat into refrigerant vapour and provide to absorber 1;Air enters 9 liters of the second compressor
Pressure heats up, and the compressed air of the second compressor 9 discharge enters combustion chamber 10, and external fuel enters combustion chamber 10 and compressed air
Mix and burn into high-temperature fuel gas, high-temperature fuel gas enter gas turbine 11 step-down work done, the combustion gas of gas turbine 11 discharge flows through
Externally discharge after generator 2 heat release cooling;The cycle fluid of the 3rd compressor 12 discharge flows through evaporimeter 4 heat release cooling,
Enter the 4th compressor 14 boosting afterwards to heat up;The cycle fluid of the 4th compressor 14 discharge flows through evaporimeter 4 heat release and becomes cryogen
Liquid, after through cryogenic throttle valve 17 reducing pressure by regulating flow enter low temperature heat exchanger 16;Low-temperature heat medium flow through low temperature heat exchanger 16,
Heating enters its interior cryogen liquid and becomes refrigerant vapour, and the refrigerant vapour that low temperature heat exchanger 16 produces enters 12 liters of the 3rd compressor
Pressure heats up;The work(of gas turbine 11 output is supplied to compressor 8, the second compressor 9, the 3rd compressor 12 and the 4th compressor 14
It is used as power, form first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Fig. 8 is realized in:
In the compressing-absorbing type heat pump of first kind thermal drivers shown in Fig. 1, cancel the outside fuel connecting with combustion chamber 10 and lead to
Road, increases new compressor, and the outside fuel gas passage that increases is connected with new compressor 18, and new compressor 18 also has to be compressed
Fuel gas passage is connected with combustion chamber 10, and gas turbine 11 connects new compressor 18 and transmits power, forms first kind heat
Drive compression-absorption heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Fig. 9 is realized in:
In the compressing-absorbing type heat pump of first kind thermal drivers shown in Fig. 1, increase heater, gas turbine 11 is had combustion gas
After passage is connected with generator 2, generator 2 has blast tube and ft connection to be adjusted to gas turbine 11 and have blast tube again
The finisher 4 being sequentially communicated generator 2, heater 19 and evaporimeter 4 has blast tube and ft connection again, and heater 19 is also
There are heated medium passage and ft connection;The combustion gas of gas turbine 11 discharge flows through generator 2, heater 19 and evaporation successively
Device 4 progressively heat release cooling, externally discharge afterwards, form first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Figure 10 is realized in:
(1), in structure, it is mainly handed over by absorber, generator, condenser, evaporimeter, choke valve, solution pump, solution heat
Parallel operation, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor, decompressor and high temperature regenerator are formed;Inhale
Receiving device 1 has weak solution pipeline to connect with generator 2 with solution heat exchanger 7 through solution pump 6, and generator 2 also has concentrated solution pipeline
Connect with absorber 1 through solution heat exchanger 7, generator 2 also has refrigerant steam channel to connect with compressor 8, and compressor 8 also has
Refrigerant steam channel is connected with condenser 3, and condenser 3 also has cryogen liquid pipeline to connect with evaporimeter 4 through choke valve 5, evaporimeter 4
Refrigerant steam channel is also had to connect with absorber 1, outside has air duct to connect with the second compressor 9, and the second compressor 9 also has
Compressed air channel is connected with combustion chamber 10 through high temperature regenerator 20, and combustion chamber 10 also has fuel channel and ft connection, burning
Room 10 also has blast tube to connect with gas turbine 11, and gas turbine 11 also has blast tube to be sequentially communicated high temperature regenerator 20 He
After generator 2, generator 2 has blast tube and ft connection again, and outside also have low-temperature heat medium passage and the 3rd compressor 12
Connection, the 3rd compressor 12 also has low-temperature heat medium passage to connect with decompressor 13 through evaporimeter 4, and decompressor 13 also has Low Temperature Thermal
Medium channel and ft connection, absorber 1 and condenser 3 also have heated medium pipeline and ft connection, gas turbine respectively
11 and decompressor 13 connect compressor 8, the second compressor 9 and the 3rd compressor 12 and transmit power.
(2), in flow process, the weak solution of absorber 1 enters generator 2 through solution pump 6 and solution heat exchanger 7, and combustion gas flows through
Generator 2, heating enter its interior solution release refrigerant vapour and provide to compressor 8, and the concentrated solution of generator 2 is through solution heat
Exchanger 7 enters absorber 1, absorbs refrigerant vapour and heat release is in heated medium;Refrigerant vapour flows through compressor 8 boosting and rises
Temperature, the refrigerant vapour of compressor 8 discharge enters condenser 3, heat release becomes cryogen liquid, the cryogen liquid of condenser 3 in heated medium
Throttle through choke valve 5 and enter evaporimeter 4, absorb heat into refrigerant vapour and provide to absorber 1;Air enters 9 liters of the second compressor
Pressure heats up, and the compressed air of the second compressor 9 discharge enters combustion chamber 10, external fuel after flowing through high temperature regenerator 20 heat absorption
Enter combustion chamber 10 and mix and burn into high-temperature fuel gas with compressed air, high-temperature fuel gas enter gas turbine 11 step-down work done, combustion
The combustion gas of gas-turbine 11 discharge flows through high temperature regenerator 20 successively and generator 2 progressively externally discharges after heat release is lowered the temperature;Low temperature
Thermal medium enters the 3rd compressor 12 boosting and heats up, and flows through evaporimeter 4 heat release, and entrance decompressor 13 step-down work done afterwards is simultaneously right
Outer discharge;The work(of gas turbine 11 and decompressor 13 output is supplied to compressor 8, the second compressor 9 and the 3rd compressor 12 and makees
Power, forms first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Figure 11 is realized in:
(1) in structure, in the compressing-absorbing type heat pump of first kind thermal drivers shown in Fig. 1, increase the second generator, second
Choke valve, the second solution pump and the second solution heat exchanger, absorber 1 sets up weak solution pipeline through the second solution pump 23 and second
Solution heat exchanger 24 is connected with the second generator 21, and the second generator 21 also has concentrated solution pipeline through the second solution heat exchanger
24 are connected with absorber 1, generator 2 is had refrigerant steam channel to connect with compressor 8 and is adjusted to generator 2 and has refrigerant vapour to lead to
After road is connected with the second generator 21, the second generator 21 has cryogen liquid pipeline through second throttle 22 with condenser 3 even again
Logical, the second generator 21 also has refrigerant steam channel to connect with compressor 8.
(2), in flow process, the refrigerant vapour that generator 2 produces is supplied to the second generator 21 and makees to drive thermal medium, absorber 1
Part weak solution enter the second generator 21 through the second solution pump 23 and the second solution heat exchanger 24, refrigerant vapour flows through the
Two generators 21, heating enter its interior solution release refrigerant vapour and provide to compressor 8, the concentrated solution of the second generator 21
Enter absorber 1 through the second solution heat exchanger 24;The refrigerant vapour heat release flowing through the second generator 21 becomes cryogen liquid, after warp
Second throttle 22 throttling enters condenser 3, forms first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Figure 12 is realized in:
(1) in structure, in the compressing-absorbing type heat pump of first kind thermal drivers shown in Fig. 1, increase the second generator, second
Choke valve and the second solution heat exchanger, absorber 1 is had weak solution pipeline through solution pump 6 and solution heat exchanger 7 and generation
Device 2 connection be adjusted to absorber 1 have weak solution pipeline through solution pump 6, solution heat exchanger 7 and the second solution heat exchanger 24 with
Generator 2 connects, and generator 2 is had concentrated solution pipeline to connect with absorber 1 through solution heat exchanger 7 and is adjusted to generator 2 and has
Concentrated solution pipeline is connected with the second generator 21 through the second solution heat exchanger 24, and the second generator 21 has concentrated solution pipeline warp again
Solution heat exchanger 7 is connected with absorber 1, generator 2 is had refrigerant steam channel to connect with compressor 8 and is adjusted to generator 2
After having refrigerant steam channel to connect with the second generator 21, the second generator 21 has cryogen liquid pipeline again through second throttle 22
Connect with condenser 3, the second generator 21 also has refrigerant steam channel to connect with compressor 8.
(2), in flow process, the refrigerant vapour that generator 2 produces is supplied to the second generator 21 and makees to drive thermal medium, absorber 1
Weak solution through solution pump 6, solution heat exchanger 7 and the second solution heat exchanger 24 enter generator 2, generator 2 dense molten
Liquid enters the second generator 21 through the second solution heat exchanger 24, and refrigerant vapour flows through the second generator 21, heating enters in it
Solution release refrigerant vapour providing to compressor 8, the concentrated solution of the second generator 21 enters through solution heat exchanger 7 and absorbs
Device 1;The refrigerant vapour heat release flowing through the second generator 21 becomes cryogen liquid, after through second throttle 22 throttle enter condenser 3,
Form first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Figure 13 is realized in:
(1) in structure, in the compressing-absorbing type heat pump of first kind thermal drivers shown in Fig. 1, increase the second generator, second
Choke valve, the second solution pump and the second solution heat exchanger, absorber 1 is had weak solution pipeline to hand over through solution pump 6 and solution heat
Parallel operation 7 is connected with generator 2 and is adjusted to absorber 1 and has weak solution pipeline through solution pump 6 and solution heat exchanger 7 and the second generation
Device 21 connects, and the second generator 21 has concentrated solution pipeline again through the second solution pump 23 and the second solution heat exchanger 24 and generator
2 connections, generator 2 are had concentrated solution pipeline to connect with absorber 1 through solution heat exchanger 7 and are adjusted to generator 2 and have concentrated solution
Pipeline is connected with absorber 1 with solution heat exchanger 7 through the second solution heat exchanger 24, and generator 2 is had refrigerant steam channel
Connect with compressor 8 and be adjusted to after generator 2 has refrigerant steam channel to connect with the second generator 21 second generator 21 again
Cryogen liquid pipeline is had to connect with condenser 3 through second throttle 22, the second generator 21 also has refrigerant steam channel and compressor 8
Connection.
(2), in flow process, the refrigerant vapour that generator 2 produces is supplied to the second generator 21 and makees to drive thermal medium, absorber 1
Weak solution enter the second generator 21 through solution pump 6 and solution heat exchanger 7, refrigerant vapour flow through the second generator 21, plus
Heat enters its interior solution release refrigerant vapour and provides to compressor 8, and the concentrated solution of the second generator 21 is through the second solution pump
23 and the second solution heat exchanger 24 enter generator 2, the concentrated solution of generator 2 is through the second solution heat exchanger 24 and solution heat
Exchanger 7 enters absorber 1;The refrigerant vapour heat release flowing through the second generator 21 becomes cryogen liquid, after through second throttle 22
Throttling enters condenser 3, forms first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Figure 14 is realized in:
(1) in structure, in the compressing-absorbing type heat pump of first kind thermal drivers shown in Fig. 1, increase the second generator, second
Choke valve, the second solution pump and the second solution heat exchanger, absorber 1 is had weak solution pipeline to hand over through solution pump 6 and solution heat
Parallel operation 7 is connected with generator 2 and is adjusted to absorber 1 and has weak solution pipeline through solution pump 6 and solution heat exchanger 7 and the second generation
Device 21 connects, and the second generator 21 has concentrated solution pipeline again through the second solution pump 23 and the second solution heat exchanger 24 and generator
2 connections, generator 2 are had concentrated solution pipeline to connect with absorber 1 through solution heat exchanger 7 and are adjusted to generator 2 and have concentrated solution
Pipeline is connected with absorber 1 with solution heat exchanger 7 through the second solution heat exchanger 24, and compressor 8 is had refrigerant steam channel
Connect with condenser 3 and be adjusted to after compressor 8 has refrigerant steam channel to connect with the second generator 21 second generator 21 again
Cryogen liquid pipeline is had to connect with condenser 3 through second throttle 22, the second generator 21 also has refrigerant steam channel and condenser 3
Connection.
(2), in flow process, the refrigerant vapour of compressor 8 discharge is supplied to the second generator 21 and makees to drive thermal medium, absorber 1
Weak solution enter the second generator 21 through solution pump 6 and solution heat exchanger 7, refrigerant vapour flow through the second generator 21, plus
Heat enters its interior solution release refrigerant vapour and provides to condenser 3, and the concentrated solution of the second generator 21 is through the second solution pump
23 and the second solution heat exchanger 24 enter generator 2, the concentrated solution of generator 2 is through the second solution heat exchanger 24 and solution heat
Exchanger 7 enters absorber 1;The refrigerant vapour heat release flowing through the second generator 21 becomes cryogen liquid, after through second throttle 22
Throttling enters condenser 3, forms first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Figure 15 is realized in:
In the compressing-absorbing type heat pump of first kind thermal drivers shown in Figure 12, increase heater, gas turbine 11 is had combustion gas
After passage is connected with generator 2, generator 2 has blast tube and ft connection to be adjusted to gas turbine 11 and have blast tube again
It is sequentially communicated generator 2, the finisher 4 of the second generator 21, heater 17 and evaporimeter 4 has blast tube and outside to connect again
Logical, heater 17 also has heated medium passage and ft connection;Gas turbine 11 discharge combustion gas flow through successively generator 2,
Second generator 21, heater 17 and evaporimeter 4 progressively heat release cooling, externally discharge afterwards, form first kind thermal drivers pressure
Contracting-absorption heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Figure 16 is realized in:
(1) in structure, in the compressing-absorbing type heat pump of first kind thermal drivers shown in Fig. 1, increase the second generator, second
Absorber, the second solution pump and the second solution heat exchanger, evaporimeter 4 is had refrigerant steam channel to connect adjustment with absorber 1
Refrigerant steam channel is had to connect with the second absorber 25 for evaporimeter 4, the second absorber 25 also has weak solution pipeline molten through second
Liquid pump 23 is connected with the second generator 21 with the second solution heat exchanger 24, and the second generator 21 also has concentrated solution pipeline through second
Solution heat exchanger 24 is connected with the second absorber 25, and the second generator 21 also has refrigerant steam channel to connect with absorber 1, will
After gas turbine 11 has blast tube to connect with generator 2, generator 2 has blast tube and ft connection to be adjusted to combustion gas again
After turbine 11 has blast tube to be sequentially communicated generator 2 and the second generator 21, the second generator 21 has blast tube again with outward
Portion connects, and the second absorber 25 also has heated medium passage and ft connection.
(2), in flow process, the refrigerant vapour that evaporimeter 4 produces enters the second absorber 25, the weak solution of the second absorber 25
Enter the second generator 21 through the second solution pump 23 and the second solution heat exchanger 24, combustion gas flows through the second generator 21, heating
Enter its interior solution release refrigerant vapour and provide to absorber 1, the concentrated solution of the second generator 21 is handed over through the second solution heat
Parallel operation 24 enters the second absorber 25, absorbs refrigerant vapour and heat release is in heated medium, forms first kind thermal drivers compression-suction
Receipts formula heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Figure 17 is realized in:
(1) in structure, in the compressing-absorbing type heat pump of first kind thermal drivers shown in Fig. 1, increase the second generator, second
Absorber, the second solution pump, solution choke valve, the second solution choke valve and point steam chest, absorber 1 is had weak solution pipeline through molten
Liquid pump 6 connect with generator 2 with solution heat exchanger 7 be adjusted to absorber 1 have weak solution pipeline through solution pump 6 and solution heat hand over
Parallel operation 7 is connected with the second absorber 25, and the second absorber 25 also has weak solution pipeline through solution choke valve 26 and the second generator
21 connections, the second generator 21 is had concentrated solution pipeline to be connected with generator 2 through the second solution pump 23 again, generator 2 is had dense molten
Liquid pipeline is connected with absorber 1 through solution heat exchanger 7 and is adjusted to generator 2 and has concentrated solution pipeline through the second solution choke valve 27
Connect with a point steam chest 28 with the second absorber 25, a point steam chest 28 has concentrated solution pipeline through solution heat exchanger 7 with absorber 1 even again
Logical, generator 2 there is is refrigerant steam channel connect with compressor 8 and is adjusted to generator 2 and has refrigerant steam channel and second to absorb
Device 25 connects, and the second generator 21 also has refrigerant steam channel to connect with compressor 8 with a point steam chest 28 respectively, by gas turbine 11
After having blast tube to connect with generator 2, generator 2 has blast tube and ft connection to be adjusted to gas turbine 11 again and has combustion
After gas passage is sequentially communicated generator 2 and the second generator 21, the second generator 21 has blast tube and ft connection again.
(2), in flow process, the weak solution of absorber 1 enters the second absorber 25, inhales through solution pump 6 and solution heat exchanger 7
Receive refrigerant vapour heat release, the weak solution of the second absorber 25 enters the second generator 21 through solution choke valve 26 reducing pressure by regulating flow,
Combustion gas flows through the second generator 21, heating enters its interior solution release refrigerant vapour and provides to compressor 8;Second generator
21 concentrated solution enters generator 2 through the second solution pump 23, and it is cold that combustion gas flows through generator 2, heating enters its interior solution release
Agent steam simultaneously provides to the second absorber 25, and the concentrated solution of generator 2 flows through through after the second solution choke valve 27 reducing pressure by regulating flow
Second absorber 25 heat absorption part vaporization;Solution after part vaporizes enters a point steam chest 28, and a point steam chest 28 release cryogen steams
Vapour simultaneously provides to compressor 8, and the concentrated solution of point steam chest 28 enters absorber 1 through solution heat exchanger 7, forms first kind thermal drivers
Compressing-absorbing type heat pump.
Effect that the technology of the present invention can be realized first kind thermal drivers compressing-absorbing type heat proposed by the invention
Pump, has the effect that and advantage:
(1) new approaches and the new technology of temperature difference utilization are proposed.
(2) heat energy (temperature difference) drives, and realizes heat supply/refrigeration, or may be selected externally to provide power simultaneously.
(3) rationally, performance index is variable and thermodynamic parameter change is corresponding, is capable of filling of heat energy (temperature difference) for flow process
Divide and efficient utilization.
(4) if necessary, realize heat supply/refrigeration by external impetus, flexibly, adaptability is good for mode.
(5) utilize the gas-turbine installation reply high temperature section temperature difference to utilize, effectively realize high temperature section heat energy efficient utilization.
(6) effectively utilizes of low temperature heat energy are realized, it is to avoid conflicting between low-temperature heat medium parameter and cryogen fluidity energy, more
Mend the deficiency of absorption heat pump technology.
(7), when the gaseous material with air as representative makees low-temperature heat source, heating power change procedure can be participated in directly as working medium,
Link is minimum;Be conducive to improving utilization efficiency of heat energy, advantageously reduce device fabrication cost.
(8) utilize compressor lifting condensation parameter, be conducive to the distribution of different temperatures section heat energy and rationally utilize, be conducive to
The lifting temperature difference utilizes level.
(9) compare thermal drivers compression heat pump, refrigerant vapour boosting is completed using absorption heat pump flow process, reduces motion portion
Part, improves device security, reduces on environmentally undesirable impact.
(10) provide multiple concrete technical schemes, cope with numerous different actual states, have the wider scope of application.
(11) extend heat pump techniques, enrich the type of compressing-absorbing type heat pump, be conducive to heat energy height is better achieved
Effect utilizes.
Claims (48)
1. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporimeter, choke valve, molten
Liquid pump, solution heat exchanger, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor and decompressor are formed;
Absorber (1) has weak solution pipeline to connect with generator (2) with solution heat exchanger (7) through solution pump (6), and generator (2) is also
Concentrated solution pipeline is had to connect with absorber (1) through solution heat exchanger (7), generator (2) also has refrigerant steam channel and compression
Machine (8) connects, and compressor (8) also has refrigerant steam channel to connect with condenser (3), and condenser (3) also has cryogen liquid pipeline warp
Choke valve (5) is connected with evaporimeter (4), and evaporimeter (4) also has refrigerant steam channel to connect with absorber (1), and there is air outside
Passage is connected with the second compressor (9), and the second compressor (9) also has compressed air channel to connect with combustion chamber (10), combustion chamber
(10) also have fuel channel and ft connection, combustion chamber (10) also have blast tube to connect with gas turbine (11), gas turbine
(11) after also having blast tube to connect with generator (2), generator (2) has blast tube and ft connection again, and outside is also low
Warm passage is connected with the 3rd compressor (12), and the 3rd compressor (12) also has low-temperature heat medium passage through evaporimeter (4)
Connect with decompressor (13), decompressor (13) also has low-temperature heat medium passage and ft connection, absorber (1) and condenser (3)
Heated medium pipeline and ft connection, gas turbine (11) and decompressor (13) is also had to connect compressor (8), the second pressure respectively
Contracting machine (9) and the 3rd compressor (12) simultaneously transmit power, form first kind thermal drivers compressing-absorbing type heat pump.
2. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporimeter, choke valve, molten
Liquid pump, solution heat exchanger, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor, decompressor and the 4th pressure
Contracting machine is formed;Absorber (1) has weak solution pipeline to connect with generator (2) with solution heat exchanger (7) through solution pump (6),
Generator (2) also has concentrated solution pipeline to connect with absorber (1) through solution heat exchanger (7), and generator (2) also has refrigerant vapour
Passage is connected with compressor (8), and compressor (8) also has refrigerant steam channel to connect with condenser (3), and condenser (3) is also cold
Agent liquid pipeline is connected with evaporimeter (4) through choke valve (5), and evaporimeter (4) also has refrigerant steam channel to connect with absorber (1),
Outside has air duct to connect with the second compressor (9), and the second compressor (9) also has compressed air channel with combustion chamber (10) even
Logical, combustion chamber (10) also have fuel channel and ft connection, and combustion chamber (10) also have blast tube to connect with gas turbine (11),
After gas turbine (11) also has blast tube to connect with generator (2), generator (2) has blast tube and ft connection, outward again
Portion also has low-temperature heat medium passage to connect with the 3rd compressor (12), and the 3rd compressor (12) also has low-temperature heat medium passage through steaming
Send out device (4) to connect with the 4th compressor (14), the 4th compressor (14) also has low-temperature heat medium passage through evaporimeter (4) and expansion
Machine (13) connects, and decompressor (13) also has low-temperature heat medium passage and ft connection, absorber (1) and condenser (3) also to distinguish
Heated medium pipeline and ft connection, gas turbine (11) and decompressor (13) is had to connect compressor (8), the second compressor
(9), the 3rd compressor (12) and the 4th compressor (14) transmit power, forms first kind thermal drivers compressing-absorbing type heat pump.
3. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporimeter, choke valve, molten
Liquid pump, solution heat exchanger, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor, decompressor and regenerator
Formed;Absorber (1) has weak solution pipeline to connect with generator (2) with solution heat exchanger (7) through solution pump (6), occurs
Device (2) also has concentrated solution pipeline to connect with absorber (1) through solution heat exchanger (7), and generator (2) also has refrigerant steam channel
Connect with compressor (8), compressor (8) also has refrigerant steam channel to connect with condenser (3), and condenser (3) also has cryogen liquid
Pipeline is connected with evaporimeter (4) through choke valve (5), and evaporimeter (4) also has refrigerant steam channel to connect with absorber (1), outside
Air duct is had to connect with the second compressor (9), the second compressor (9) also has compressed air channel to connect with combustion chamber (10),
Combustion chamber (10) also has fuel channel and ft connection, and combustion chamber (10) also have blast tube to connect with gas turbine (11), combustion
After gas-turbine (11) also has blast tube to connect with generator (2), generator (2) has blast tube and ft connection again, outside
Low-temperature heat medium passage is also had to connect with the 3rd compressor (12) through regenerator (15), the 3rd compressor (12) also has Low Temperature Thermal to be situated between
Matter passage is connected with decompressor (13) with regenerator (15) through evaporimeter (4), decompressor (13) also have low-temperature heat medium passage with
Ft connection, absorber (1) and condenser (3) also have heated medium pipeline and ft connection respectively, gas turbine (11) and
Decompressor (13) connects compressor (8), the second compressor (9) and the 3rd compressor (12) and transmits power, forms first kind heat
Drive compression-absorption heat pump.
4. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporimeter, choke valve, molten
Liquid pump, solution heat exchanger, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor, decompressor and Low Temperature Thermal
Exchanger is formed;Absorber (1) has weak solution pipeline to connect with generator (2) through solution pump (6) and solution heat exchanger (7)
Logical, generator (2) also has concentrated solution pipeline to connect with absorber (1) through solution heat exchanger (7), and generator (2) also has cryogen
Steam channel is connected with compressor (8), and compressor (8) also has refrigerant steam channel to connect with condenser (3), and condenser (3) is also
Cryogen liquid pipeline is had to connect with evaporimeter (4) through choke valve (5), evaporimeter (4) also has refrigerant steam channel with absorber (1) even
Logical, outside has air duct to connect with the second compressor (9), and the second compressor (9) also has compressed air channel and combustion chamber
(10) connect, combustion chamber (10) also have fuel channel and ft connection, combustion chamber (10) also have blast tube and gas turbine
(11) connect, after gas turbine (11) also has blast tube to connect with generator (2), generator (2) has blast tube again with outward
Portion connects, and the 3rd compressor (12) has circulatory mediator passage to connect with decompressor (13) through evaporimeter (4), and decompressor (13) also has
Circulatory mediator passage is connected with the 3rd compressor (12) through low temperature heat exchanger (16), and absorber (1) and condenser (3) are also distinguished
There are heated medium pipeline and ft connection, low temperature heat exchanger (16) also has low-temperature heat medium passage and ft connection, combustion gas
Turbine (11) and decompressor (13) connect compressor (8), the second compressor (9) and the 3rd compressor (12) and transmit power, shape
Become first kind thermal drivers compressing-absorbing type heat pump.
5. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporimeter, choke valve, molten
Liquid pump, solution heat exchanger, compressor, the second compressor, combustion chamber, gas turbine and the 3rd compressor are formed;Absorber
(1) weak solution pipeline is had to connect with generator (2) with solution heat exchanger (7) through solution pump (6), generator (2) also has dense molten
Liquid pipeline is connected with absorber (1) through solution heat exchanger (7), and generator (2) also has refrigerant steam channel with compressor (8) even
Logical, compressor (8) also has refrigerant steam channel to connect with condenser (3), and condenser (3) also has cryogen liquid pipeline through choke valve
(5) connect with evaporimeter (4), evaporimeter (4) also have refrigerant steam channel connect with absorber (1), outside have air duct and
Second compressor (9) connects, and the second compressor (9) also has compressed air channel to connect with combustion chamber (10), and combustion chamber (10) are gone back
There are fuel channel and ft connection, combustion chamber (10) also have blast tube to connect with gas turbine (11), gas turbine (11) is also
After having blast tube to connect with generator (2), generator (2) has blast tube and ft connection again, and outside also have Low Temperature Thermal to be situated between
Matter passage is connected with the 3rd compressor (12), and the 3rd compressor (12) also has low-temperature heat medium passage through evaporimeter (4) and outside
Connection, absorber (1) and condenser (3) also have heated medium pipeline and ft connection respectively, and gas turbine (11) connects pressure
Contracting machine (8), the second compressor (9) and the 3rd compressor (12) simultaneously transmit power, form first kind thermal drivers compressing-absorbing type heat
Pump.
6. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporimeter, choke valve, molten
Liquid pump, solution heat exchanger, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor, low temperature heat exchanger and
Cryogenic throttle valve is formed;Absorber (1) has weak solution pipeline through solution pump (6) and solution heat exchanger (7) and generator (2)
Connection, generator (2) also has concentrated solution pipeline to connect with absorber (1) through solution heat exchanger (7), and generator (2) is also cold
Agent steam channel is connected with compressor (8), and compressor (8) also has refrigerant steam channel to connect with condenser (3), condenser (3)
Cryogen liquid pipeline is also had to connect with evaporimeter (4) through choke valve (5), evaporimeter (4) also has refrigerant steam channel and absorber (1)
Connection, outside has air duct to connect with the second compressor (9), and the second compressor (9) also has compressed air channel and combustion chamber
(10) connect, combustion chamber (10) also have fuel channel and ft connection, combustion chamber (10) also have blast tube and gas turbine
(11) connect, after gas turbine (11) also has blast tube to connect with generator (2), generator (2) has blast tube again with outward
Portion connects, and the 3rd compressor (12) has circulatory mediator passage through evaporimeter (4) and cryogenic throttle valve (17) and low temperature heat exchanger
(16) connect, low temperature heat exchanger (16) also have circulatory mediator passage connect with the 3rd compressor (12), absorber (1) and condense
Device (3) also has heated medium pipeline and ft connection respectively, low temperature heat exchanger (16) also have low temperature heat exchanger passage with
Ft connection, gas turbine (11) connects compressor (8), the second compressor (9) and the 3rd compressor (12) and transmits power, shape
Become first kind thermal drivers compressing-absorbing type heat pump.
7. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, evaporimeter, choke valve, molten
Liquid pump, solution heat exchanger, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor, the 4th compressor, low
Temperature heat exchanger and cryogenic throttle valve are formed;Absorber (1) has weak solution pipeline through solution pump (6) and solution heat exchanger
(7) connect with generator (2), generator (2) also has concentrated solution pipeline to connect with absorber (1) through solution heat exchanger (7), sends out
Raw device (2) also has refrigerant steam channel to connect with compressor (8), and compressor (8) also has refrigerant steam channel with condenser (3) even
Logical, condenser (3) also has cryogen liquid pipeline to connect with evaporimeter (4) through choke valve (5), and evaporimeter (4) also has refrigerant vapour to lead to
Road is connected with absorber (1), and outside has air duct to connect with the second compressor (9), and the second compressor (9) also has compressed air
Passage is connected with combustion chamber (10), and combustion chamber (10) also have fuel channel and ft connection, and combustion chamber (10) also have blast tube
Connect with gas turbine (11), after gas turbine (11) also has blast tube to connect with generator (2), generator (2) has combustion again
Gas passage and ft connection, the 3rd compressor (12) has circulatory mediator passage to connect with the 4th compressor (14) through evaporimeter (4),
4th compressor (14) also has circulatory mediator passage to connect with low temperature heat exchanger (16) through evaporimeter (4) and cryogenic throttle valve (17)
Logical, low temperature heat exchanger (16) also has circulatory mediator passage to connect with the 3rd compressor (12), absorber (1) and condenser (3)
Also there are heated medium pipeline and ft connection respectively, low temperature heat exchanger (16) also has low temperature heat exchanger passage to connect with outside
Logical, gas turbine (11) connects compressor (8), the second compressor (9), the 3rd compressor (12) and the 4th compressor (14) and passes
Defeated power, forms first kind thermal drivers compressing-absorbing type heat pump.
8. first kind thermal drivers compressing-absorbing type heat pump, is in first kind thermal drivers compression-suction arbitrary described in claim 1-7
In receipts formula heat pump, cancel the outside fuel channel connecting with combustion chamber (10), increase new compressor, outside increase fuel gas
Passage is connected with new compressor (18), and new compressor (18) also has compressed gaseous fuel channel to connect with combustion chamber (10),
Gas turbine (11) connects new compressor (18) and transmits power, forms first kind thermal drivers compressing-absorbing type heat pump.
9. first kind thermal drivers compressing-absorbing type heat pump, is in first kind thermal drivers compression-suction arbitrary described in claim 1-8
In receipts formula heat pump, increase heater, after gas turbine (11) is had blast tube to connect with generator (2) generator (2) is again
Having blast tube and ft connection to be adjusted to gas turbine (11) has blast tube to be sequentially communicated generator (2) and heater (19)
Heater (19) has blast tube and ft connection more afterwards, and heater (19) also has heated medium passage and ft connection,
Form first kind thermal drivers compressing-absorbing type heat pump.
10. first kind thermal drivers compressing-absorbing type heat pump, be arbitrary first kind thermal drivers compression described in claim 1-8-
In absorption heat pump, increase heater, generator (2) after gas turbine (11) is had blast tube to connect with generator (2)
Having blast tube and ft connection to be adjusted to gas turbine (11) again has blast tube to be sequentially communicated generator (2), heater
(19) and the finisher (4) of evaporimeter (4) has blast tube and ft connection again, heater (19) also has heated medium to lead to
Road and ft connection, form first kind thermal drivers compressing-absorbing type heat pump.
11. first kind thermal drivers compressing-absorbing type heat pumps, be arbitrary first kind thermal drivers compression described in claim 1-8-
In absorption heat pump, increase the second generator, second throttle, the second solution pump and the second solution heat exchanger, absorber (1)
Set up weak solution pipeline to connect with the second generator (21) with the second solution heat exchanger (24) through the second solution pump (23), second
Generator (21) also has concentrated solution pipeline to connect with absorber (1) through the second solution heat exchanger (24), generator (2) is had cold
Agent steam channel is connected with compressor (8) and is adjusted to generator (2) and has refrigerant steam channel to connect it with the second generator (21)
Second generator (21) has cryogen liquid pipeline to connect with condenser (3) through second throttle (22) more afterwards, the second generator (21)
Also have refrigerant steam channel to connect with compressor (8), form first kind thermal drivers compressing-absorbing type heat pump.
12. first kind thermal drivers compressing-absorbing type heat pumps, be arbitrary first kind thermal drivers compression described in claim 1-8-
In absorption heat pump, increase the second generator, second throttle and the second solution heat exchanger, absorber (1) is had weak solution
Pipeline is connected with generator (2) through solution pump (6) and solution heat exchanger (7) and is adjusted to absorber (1) and has weak solution pipeline warp
Solution pump (6), solution heat exchanger (7) are connected with generator (2) with the second solution heat exchanger (24), and generator (2) is had
Concentrated solution pipeline is connected with absorber (1) through solution heat exchanger (7) and is adjusted to generator (2) and has concentrated solution pipeline molten through second
Liquid heat exchanger (24) is connected with the second generator (21), and the second generator (21) has concentrated solution pipeline again through solution heat exchanger
(7) connect with absorber (1), generator (2) is had refrigerant steam channel to connect with compressor (8) and is adjusted to generator (2) and has
After refrigerant steam channel is connected with the second generator (21), the second generator (21) has cryogen liquid pipeline again through second throttle
(22) connect with condenser (3), the second generator (21) also has refrigerant steam channel to connect with compressor (8), forms the first kind
Thermal drivers compressing-absorbing type heat pump.
13. first kind thermal drivers compressing-absorbing type heat pumps, be arbitrary first kind thermal drivers compression described in claim 1-8-
In absorption heat pump, increase the second generator, second throttle, the second solution pump and the second solution heat exchanger, by absorber
(1) have weak solution pipeline connect with generator (2) through solution pump (6) and solution heat exchanger (7) be adjusted to absorber (1) have dilute
Solution line is connected with the second generator (21) with solution heat exchanger (7) through solution pump (6), and the second generator (21) has dense again
Solution line is connected with generator (2) with the second solution heat exchanger (24) through the second solution pump (23), generator (2) is had dense
Solution line is connected with absorber (1) through solution heat exchanger (7) and is adjusted to generator (2) and has concentrated solution pipeline through the second solution
Heat exchanger (24) is connected with absorber (1) with solution heat exchanger (7), and generator (2) is had refrigerant steam channel and compression
Machine (8) connection is adjusted to the second generator (21) after generator (2) has refrigerant steam channel to connect with the second generator (21)
Cryogen liquid pipeline is had to connect with condenser (3) through second throttle (22) again, the second generator (21) also has refrigerant steam channel
Connect with compressor (8), form first kind thermal drivers compressing-absorbing type heat pump.
14. first kind thermal drivers compressing-absorbing type heat pumps, be arbitrary first kind thermal drivers compression described in claim 1-8-
In absorption heat pump, increase the second generator, second throttle, the second solution pump and the second solution heat exchanger, absorber (1)
Set up weak solution pipeline to connect with the second generator (21) with the second solution heat exchanger (24) through the second solution pump (23), second
Generator (21) also has concentrated solution pipeline to connect with absorber (1) through the second solution heat exchanger (24), compressor (8) is had cold
Agent steam channel is connected with condenser (3) and is adjusted to compressor (8) and has refrigerant steam channel to connect it with the second generator (21)
Second generator (21) has cryogen liquid pipeline to connect with condenser (3) through second throttle (22) more afterwards, the second generator (21)
Also have refrigerant steam channel to connect with condenser (3), form first kind thermal drivers compressing-absorbing type heat pump.
15. first kind thermal drivers compressing-absorbing type heat pumps, be arbitrary first kind thermal drivers compression described in claim 1-8-
In absorption heat pump, increase the second generator, second throttle and the second solution heat exchanger, absorber (1) is had weak solution
Pipeline is connected with generator (2) through solution pump (6) and solution heat exchanger (7) and is adjusted to absorber (1) and has weak solution pipeline warp
Solution pump (6), solution heat exchanger (7) are connected with generator (2) with the second solution heat exchanger (24), and generator (2) is had
Concentrated solution pipeline is connected with absorber (1) through solution heat exchanger (7) and is adjusted to generator (2) and has concentrated solution pipeline molten through second
Liquid heat exchanger (24) is connected with the second generator (21), and the second generator (21) has concentrated solution pipeline again through solution heat exchanger
(7) connect with absorber (1), compressor (8) is had refrigerant steam channel to connect with condenser (3) and is adjusted to compressor (8) and has
After refrigerant steam channel is connected with the second generator (21), the second generator (21) has cryogen liquid pipeline again through second throttle
(22) connect with condenser (3), the second generator (21) also has refrigerant steam channel to connect with condenser (3), forms the first kind
Thermal drivers compressing-absorbing type heat pump.
16. first kind thermal drivers compressing-absorbing type heat pumps, be arbitrary first kind thermal drivers compression described in claim 1-8-
In absorption heat pump, increase the second generator, second throttle, the second solution pump and the second solution heat exchanger, by absorber
(1) have weak solution pipeline connect with generator (2) through solution pump (6) and solution heat exchanger (7) be adjusted to absorber (1) have dilute
Solution line is connected with the second generator (21) with solution heat exchanger (7) through solution pump (6), and the second generator (21) has dense again
Solution line is connected with generator (2) with the second solution heat exchanger (24) through the second solution pump (23), generator (2) is had dense
Solution line is connected with absorber (1) through solution heat exchanger (7) and is adjusted to generator (2) and has concentrated solution pipeline through the second solution
Heat exchanger (24) is connected with absorber (1) with solution heat exchanger (7), and compressor (8) is had refrigerant steam channel and condensation
Device (3) connection is adjusted to the second generator (21) after compressor (8) has refrigerant steam channel to connect with the second generator (21)
Cryogen liquid pipeline is had to connect with condenser (3) through second throttle (22) again, the second generator (21) also has refrigerant steam channel
Connect with condenser (3), form first kind thermal drivers compressing-absorbing type heat pump.
17. first kind thermal drivers compressing-absorbing type heat pumps, are the arbitrary first kind thermal drivers pressures described in claim 11-16
In contracting-absorption heat pump, increase heater, generator after gas turbine (11) is had blast tube to connect with generator (2)
(2) having blast tube and ft connection to be adjusted to gas turbine (11) again has blast tube to be sequentially communicated generator (2) and heat supply
After device (17), heater (17) has blast tube and ft connection again, and heater (17) also has heated medium passage and outside
Connection, forms first kind thermal drivers compressing-absorbing type heat pump.
18. first kind thermal drivers compressing-absorbing type heat pumps, are the arbitrary first kind thermal drivers pressures described in claim 11-16
In contracting-absorption heat pump, increase heater, generator after gas turbine (11) is had blast tube to connect with generator (2)
(2) having blast tube and ft connection to be adjusted to gas turbine (11) again has blast tube to be sequentially communicated generator (2), heater
(17) and the finisher (4) of evaporimeter (4) has blast tube and ft connection again, heater (17) also has heated medium to lead to
Road and ft connection, form first kind thermal drivers compressing-absorbing type heat pump.
19. first kind thermal drivers compressing-absorbing type heat pumps, are the arbitrary first kind thermal drivers pressures described in claim 11-16
In contracting-absorption heat pump, after gas turbine (11) is had blast tube to connect with generator (2), generator (2) has combustion gas again
Passage and ft connection be adjusted to gas turbine (11) have blast tube be sequentially communicated generator (2) and the second generator (21) it
Second generator (21) has blast tube and ft connection more afterwards, forms first kind thermal drivers compressing-absorbing type heat pump.
20. first kind thermal drivers compressing-absorbing type heat pumps, are the arbitrary first kind thermal drivers pressures described in claim 11-16
In contracting-absorption heat pump, increase heater, generator after gas turbine (11) is had blast tube to connect with generator (2)
(2) have again blast tube and ft connection be adjusted to gas turbine (11) have blast tube be sequentially communicated generator (2), second
After raw device (21) and heater (17), heater (17) has blast tube and ft connection again, and heater (17) also has heated
Medium channel and ft connection, form first kind thermal drivers compressing-absorbing type heat pump.
21. first kind thermal drivers compressing-absorbing type heat pumps, are the arbitrary first kind thermal drivers pressures described in claim 11-16
In contracting-absorption heat pump, increase heater, generator after gas turbine (11) is had blast tube to connect with generator (2)
(2) have again blast tube and ft connection be adjusted to gas turbine (11) have blast tube be sequentially communicated generator (2), second
The finisher (4) of raw device (21), heater (17) and evaporimeter (4) has blast tube and ft connection, heater (17) again
Also have heated medium passage and ft connection, form first kind thermal drivers compressing-absorbing type heat pump.
22. first kind thermal drivers compressing-absorbing type heat pumps, be arbitrary first kind thermal drivers compression described in claim 1-8-
In absorption heat pump, increase the second generator, the second absorber, the second solution pump and the second solution heat exchanger, by evaporimeter
(4) there is refrigerant steam channel to connect with absorber (1) to be adjusted to evaporimeter (4) and have refrigerant steam channel and the second absorber (25)
Connection, the second absorber (25) also has weak solution pipeline through the second solution pump (23) and the second solution heat exchanger (24) and second
Generator (21) connects, and the second generator (21) also has concentrated solution pipeline through the second solution heat exchanger (24) and the second absorber
(25) connect, the second generator (21) also has refrigerant steam channel to connect with absorber (1), gas turbine (11) is had combustion gas to lead to
After road is connected with generator (2), generator (2) has blast tube and ft connection to be adjusted to gas turbine (11) and have combustion gas again
After passage is sequentially communicated generator (2) and the second generator (21), the second generator (21) has blast tube to connect with outside again
Logical, the second absorber (25) also has heated medium passage and ft connection, forms first kind thermal drivers compressing-absorbing type heat
Pump.
23. first kind thermal drivers compressing-absorbing type heat pumps, be arbitrary first kind thermal drivers compression described in claim 1-8-
In absorption heat pump, increase the second generator, the second absorber, the second solution pump, solution choke valve, the second solution choke valve and
Divide steam chest, absorber (1) is had weak solution pipeline to connect adjustment with solution heat exchanger (7) with generator (2) through solution pump (6)
Weak solution pipeline is had to connect with the second absorber (25) with solution heat exchanger (7) through solution pump (6) for absorber (1), second
Absorber (25) also has weak solution pipeline to connect with the second generator (21) through solution choke valve (26), and the second generator (21) is again
There is concentrated solution pipeline to connect with generator (2) through the second solution pump (23), generator (2) is had concentrated solution pipeline to hand over through solution heat
Parallel operation (7) connect with absorber (1) be adjusted to generator (2) have concentrated solution pipeline through the second solution choke valve (27) and second suction
Receive device (25) to connect with a point steam chest (28), a point steam chest (28) has concentrated solution pipeline again through solution heat exchanger (7) and absorber (1)
Connection, by generator (2) have refrigerant steam channel connect with compressor (8) be adjusted to generator (2) have refrigerant steam channel and
Second absorber (25) connects, and the second generator (21) and a point steam chest (28) also have refrigerant steam channel and compressor (8) respectively
Connection, after gas turbine (11) is had blast tube to connect with generator (2), generator (2) has blast tube to connect with outside again
The logical gas turbine (11) that is adjusted to has blast tube to be sequentially communicated the second generator after generator (2) and the second generator (21)
(21) there are blast tube and ft connection again, form first kind thermal drivers compressing-absorbing type heat pump.
24. first kind thermal drivers compressing-absorbing type heat pumps, mainly by absorber, generator, condenser, evaporimeter, choke valve,
Solution pump, solution heat exchanger, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor, decompressor and high temperature
Regenerator is formed;Absorber (1) has weak solution pipeline to connect with generator (2) through solution pump (6) and solution heat exchanger (7)
Logical, generator (2) also has concentrated solution pipeline to connect with absorber (1) through solution heat exchanger (7), and generator (2) also has cryogen
Steam channel is connected with compressor (8), and compressor (8) also has refrigerant steam channel to connect with condenser (3), and condenser (3) is also
Cryogen liquid pipeline is had to connect with evaporimeter (4) through choke valve (5), evaporimeter (4) also has refrigerant steam channel with absorber (1) even
Logical, outside has air duct to connect with the second compressor (9), and the second compressor (9) also has compressed air channel through high temperature backheat
Device (20) is connected with combustion chamber (10), and combustion chamber (10) also have fuel channel and ft connection, and combustion chamber (10) also have combustion gas to lead to
Road is connected with gas turbine (11), and gas turbine (11) also has blast tube to be sequentially communicated high temperature regenerator (20) and generator
(2) after, generator (2) has blast tube and ft connection again, and outside also have low-temperature heat medium passage and the 3rd compressor (12)
Connection, the 3rd compressor (12) also has low-temperature heat medium passage to connect with decompressor (13) through evaporimeter (4), and decompressor (13) is also
Low-temperature heat medium passage and ft connection, absorber (1) and condenser (3) is had also to have heated medium pipeline and outside to connect respectively
Lead to, gas turbine (11) and decompressor (13) connect compressor (8), the second compressor (9) and the 3rd compressor (12) and transmit
Power, forms first kind thermal drivers compressing-absorbing type heat pump.
25. first kind thermal drivers compressing-absorbing type heat pumps, mainly by absorber, generator, condenser, evaporimeter, choke valve,
Solution pump, solution heat exchanger, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor, decompressor, the 4th
Compressor and high temperature regenerator are formed;Absorber (1) have weak solution pipeline through solution pump (6) and solution heat exchanger (7) with
Generator (2) connects, and generator (2) also has concentrated solution pipeline to connect with absorber (1) through solution heat exchanger (7), generator
(2) refrigerant steam channel is also had to connect with compressor (8), compressor (8) also has refrigerant steam channel to connect with condenser (3),
Condenser (3) also has cryogen liquid pipeline connect with evaporimeter (4) through choke valve (5), evaporimeter (4) also refrigerant steam channel and
Absorber (1) connects, and outside has air duct to connect with the second compressor (9), and the second compressor (9) also has compressed air channel
Connect with combustion chamber (10) through high temperature regenerator (20), combustion chamber (10) also have fuel channel and ft connection, combustion chamber (10)
Blast tube is also had to connect with gas turbine (11), gas turbine (11) also has blast tube to be sequentially communicated high temperature regenerator (20)
There are blast tube and ft connection with generator (2) after generator (2) again, outside also have low-temperature heat medium passage and the 3rd pressure
Contracting machine (12) connects, and the 3rd compressor (12) also has low-temperature heat medium passage to connect with the 4th compressor (14) through evaporimeter (4),
4th compressor (14) also has low-temperature heat medium passage to connect with decompressor (13) through evaporimeter (4), and decompressor (13) is also low
Warm passage and ft connection, absorber (1) and condenser (3) also have heated medium pipeline and ft connection respectively,
Gas turbine (11) and decompressor (13) connect compressor (8), the second compressor (9), the 3rd compressor (12) and the 4th compression
Machine (14) simultaneously transmits power, forms first kind thermal drivers compressing-absorbing type heat pump.
26. first kind thermal drivers compressing-absorbing type heat pumps, mainly by absorber, generator, condenser, evaporimeter, choke valve,
Solution pump, solution heat exchanger, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor, decompressor, backheat
Device and high temperature regenerator are formed;Absorber (1) has weak solution pipeline through solution pump (6) and solution heat exchanger (7) and generation
Device (2) connects, and generator (2) also has concentrated solution pipeline to connect with absorber (1) through solution heat exchanger (7), and generator (2) is also
Refrigerant steam channel is had to connect with compressor (8), compressor (8) also has refrigerant steam channel to connect with condenser (3), condenser
(3) cryogen liquid pipeline is also had to connect with evaporimeter (4) through choke valve (5), evaporimeter (4) also has refrigerant steam channel and absorber
(1) connect, outside has air duct to connect with the second compressor (9), the second compressor (9) also has compressed air channel through high temperature
Regenerator (20) is connected with combustion chamber (10), and combustion chamber (10) also have fuel channel and ft connection, and combustion chamber (10) also have combustion
Gas passage is connected with gas turbine (11), and gas turbine (11) also has blast tube to be sequentially communicated high temperature regenerator (20) and occur
Generator (2) has blast tube and ft connection again after device (2), outside also have low-temperature heat medium passage through regenerator (15) with
3rd compressor (12) connection, the 3rd compressor (12) also have low-temperature heat medium passage through evaporimeter (4) and regenerator (15) and
Decompressor (13) connects, and decompressor (13) also has low-temperature heat medium passage and ft connection, absorber (1) and condenser (3) also
Heated medium pipeline and ft connection, gas turbine (11) and decompressor (13) is had to connect compressor (8), the second compression respectively
Machine (9) and the 3rd compressor (12) simultaneously transmit power, form first kind thermal drivers compressing-absorbing type heat pump.
27. first kind thermal drivers compressing-absorbing type heat pumps, mainly by absorber, generator, condenser, evaporimeter, choke valve,
Solution pump, solution heat exchanger, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor, decompressor, low temperature
Heat exchanger and high temperature regenerator are formed;Absorber (1) has weak solution pipeline through solution pump (6) and solution heat exchanger (7)
Connect with generator (2), generator (2) also has concentrated solution pipeline to connect with absorber (1) through solution heat exchanger (7), occurs
Device (2) also has refrigerant steam channel to connect with compressor (8), and compressor (8) also has refrigerant steam channel with condenser (3) even
Logical, condenser (3) also has cryogen liquid pipeline to connect with evaporimeter (4) through choke valve (5), and evaporimeter (4) also has refrigerant vapour to lead to
Road is connected with absorber (1), and outside has air duct to connect with the second compressor (9), and the second compressor (9) also has compressed air
Passage is connected with combustion chamber (10) through high temperature regenerator (20), and combustion chamber (10) also have fuel channel and ft connection, combustion chamber
(10) blast tube is also had to connect with gas turbine (11), gas turbine (11) also has blast tube to be sequentially communicated high temperature regenerator
(20) and generator (2) after generator (2) have blast tube and ft connection again, the 3rd compressor (12) have circulatory mediator lead to
Road is connected with decompressor (13) through evaporimeter (4), decompressor (13) also have circulatory mediator passage through low temperature heat exchanger (16) with
3rd compressor (12) connection, absorber (1) and condenser (3) also have heated medium pipeline and ft connection, low temperature respectively
Heat exchanger (16) also has low-temperature heat medium passage and ft connection, gas turbine (11) and decompressor (13) to connect compressor
(8), the second compressor (9) and the 3rd compressor (12) transmit power, forms first kind thermal drivers compressing-absorbing type heat pump.
28. first kind thermal drivers compressing-absorbing type heat pumps, mainly by absorber, generator, condenser, evaporimeter, choke valve,
Solution pump, solution heat exchanger, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor and high temperature regenerator
Formed;Absorber (1) has weak solution pipeline to connect with generator (2) with solution heat exchanger (7) through solution pump (6), occurs
Device (2) also has concentrated solution pipeline to connect with absorber (1) through solution heat exchanger (7), and generator (2) also has refrigerant steam channel
Connect with compressor (8), compressor (8) also has refrigerant steam channel to connect with condenser (3), and condenser (3) also has cryogen liquid
Pipeline is connected with evaporimeter (4) through choke valve (5), and evaporimeter (4) also has refrigerant steam channel to connect with absorber (1), outside
Have air duct to connect with the second compressor (9), the second compressor (9) also have compressed air channel through high temperature regenerator (20) with
Combustion chamber (10) connects, and combustion chamber (10) also have fuel channel and ft connection, and combustion chamber (10) also have blast tube and combustion gas
Turbine (11) connects, and gas turbine (11) also has blast tube to send out after being sequentially communicated high temperature regenerator (20) and generator (2)
Raw device (2) has blast tube and ft connection again, and outside also have low-temperature heat medium passage to connect with the 3rd compressor (12), and the 3rd
Compressor (12) also has low-temperature heat medium passage through evaporimeter (4) and ft connection, and absorber (1) and condenser (3) are also distinguished
There are heated medium pipeline and ft connection, gas turbine (11) connects compressor (8), the second compressor (9) and the 3rd compression
Machine (12) simultaneously transmits power, forms first kind thermal drivers compressing-absorbing type heat pump.
29. first kind thermal drivers compressing-absorbing type heat pumps, mainly by absorber, generator, condenser, evaporimeter, choke valve,
Solution pump, solution heat exchanger, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor, low temperature heat exchange
Device, cryogenic throttle valve and high temperature regenerator are formed;Absorber (1) has weak solution pipeline through solution pump (6) and solution heat exchange
Device (7) is connected with generator (2), and generator (2) also has concentrated solution pipeline to connect with absorber (1) through solution heat exchanger (7),
Generator (2) also has refrigerant steam channel to connect with compressor (8), and compressor (8) also has refrigerant steam channel and condenser (3)
Connection, condenser (3) also has cryogen liquid pipeline to connect with evaporimeter (4) through choke valve (5), and evaporimeter (4) also has refrigerant vapour
Passage is connected with absorber (1), and outside has air duct to connect with the second compressor (9), and the second compressor (9) also has compression empty
Gas passage is connected with combustion chamber (10) through high temperature regenerator (20), and combustion chamber (10) also have fuel channel and ft connection, burning
Room (10) also has blast tube to connect with gas turbine (11), and gas turbine (11) also has blast tube to be sequentially communicated high temperature backheat
After device (20) and generator (2), generator (2) has blast tube and ft connection again, and the 3rd compressor (12) has circulatory mediator
Passage is connected with low temperature heat exchanger (16) with cryogenic throttle valve (17) through evaporimeter (4), and low temperature heat exchanger (16) also follows
Ring medium channel is connected with the 3rd compressor (12), and absorber (1) and condenser (3) also have heated medium pipeline respectively with outward
Portion connects, and low temperature heat exchanger (16) also has low temperature heat exchanger passage and ft connection, and gas turbine (11) connects compressor
(8), the second compressor (9) and the 3rd compressor (12) transmit power, forms first kind thermal drivers compressing-absorbing type heat pump.
30. first kind thermal drivers compressing-absorbing type heat pumps, mainly by absorber, generator, condenser, evaporimeter, choke valve,
Solution pump, solution heat exchanger, compressor, the second compressor, combustion chamber, gas turbine, the 3rd compressor, the 4th compressor,
Low temperature heat exchanger, cryogenic throttle valve and high temperature regenerator are formed;Absorber (1) have weak solution pipeline through solution pump (6) and
Solution heat exchanger (7) is connected with generator (2), and generator (2) also has concentrated solution pipeline through solution heat exchanger (7) and absorption
Device (1) connects, and generator (2) also has refrigerant steam channel to connect with compressor (8), and compressor (8) also has refrigerant steam channel
Connect with condenser (3), condenser (3) also has cryogen liquid pipeline to connect with evaporimeter (4) through choke valve (5), evaporimeter (4) is also
Refrigerant steam channel is had to connect with absorber (1), outside has air duct to connect with the second compressor (9), the second compressor (9)
Compressed air channel is also had to connect with combustion chamber (10) through high temperature regenerator (20), combustion chamber (10) also have fuel channel and outside
Connection, combustion chamber (10) also have blast tube to connect with gas turbine (11), and gas turbine (11) also has blast tube to connect successively
After logical high temperature regenerator (20) and generator (2), generator (2) has blast tube and ft connection, the 3rd compressor (12) again
Circulatory mediator passage is had to connect with the 4th compressor (14) through evaporimeter (4), the 4th compressor (14) also has circulatory mediator passage
Connect with low temperature heat exchanger (16) with cryogenic throttle valve (17) through evaporimeter (4), low temperature heat exchanger (16) also has circulation to be situated between
Matter passage is connected with the 3rd compressor (12), and absorber (1) and condenser (3) also have heated medium pipeline and outside to connect respectively
Logical, low temperature heat exchanger (16) also low temperature heat exchanger passage and ft connection, gas turbine (11) connection compressor (8),
Second compressor (9), the 3rd compressor (12) and the 4th compressor (14) simultaneously transmit power, and formation first kind thermal drivers compression-
Absorption heat pump.
31. first kind thermal drivers compressing-absorbing type heat pumps, are the arbitrary first kind thermal drivers pressures described in claim 24-30
In contracting-absorption heat pump, cancel the outside fuel channel connecting with combustion chamber (10), increase new compressor, outside increase gas
State fuel channel is connected with new compressor (18), and new compressor (18) also has compressed gaseous fuel channel and combustion chamber (10)
Connection, gas turbine (11) connects new compressor (18) and transmits power, forms first kind thermal drivers compressing-absorbing type heat
Pump.
32. first kind thermal drivers compressing-absorbing type heat pumps, are the arbitrary first kind thermal drivers pressures described in claim 24-31
In contracting-absorption heat pump, increase heater, gas turbine (11) is had blast tube to be sequentially communicated high temperature regenerator (20) and sends out
After raw device (2), generator (2) has blast tube and ft connection to be adjusted to gas turbine (11) again has blast tube to connect successively
After logical high temperature regenerator (20), generator (2) and heater (19), heater (19) has blast tube and ft connection again, supplies
Hot device (19) also has heated medium passage and ft connection, forms first kind thermal drivers compressing-absorbing type heat pump.
33. first kind thermal drivers compressing-absorbing type heat pumps, are the arbitrary first kind thermal drivers pressures described in claim 24-31
In contracting-absorption heat pump, increase heater, gas turbine (11) is had blast tube to be sequentially communicated high temperature regenerator (20) and sends out
After raw device (2), generator (2) has blast tube and ft connection to be adjusted to gas turbine (11) again has blast tube to connect successively
Logical high temperature regenerator (20), the finisher (4) of generator (2), heater (19) and evaporimeter (4) have blast tube again with outward
Portion connects, and heater (19) also has heated medium passage and ft connection, forms first kind thermal drivers compressing-absorbing type heat
Pump.
34. first kind thermal drivers compressing-absorbing type heat pumps, are the arbitrary first kind thermal drivers pressures described in claim 24-31
In contracting-absorption heat pump, increase the second generator, second throttle, the second solution pump and the second solution heat exchanger, absorber
(1) set up weak solution pipeline to connect with the second generator (21) with the second solution heat exchanger (24) through the second solution pump (23),
Second generator (21) also has concentrated solution pipeline to connect with absorber (1) through the second solution heat exchanger (24), by generator (2)
There is refrigerant steam channel to connect with compressor (8) to be adjusted to generator (2) and have refrigerant steam channel and the second generator (21) even
After logical, the second generator (21) has cryogen liquid pipeline to connect with condenser (3) through second throttle (22) again, the second generator
(21) also have refrigerant steam channel to connect with compressor (8), form first kind thermal drivers compressing-absorbing type heat pump.
35. first kind thermal drivers compressing-absorbing type heat pumps, are the arbitrary first kind thermal drivers pressures described in claim 24-31
In contracting-absorption heat pump, increase the second generator, second throttle and the second solution heat exchanger, absorber (1) is had dilute molten
Liquid pipeline is connected with generator (2) through solution pump (6) and solution heat exchanger (7) and is adjusted to absorber (1) and has weak solution pipeline
Connect with generator (2) with the second solution heat exchanger (24) through solution pump (6), solution heat exchanger (7), by generator (2)
There is concentrated solution pipeline to connect with absorber (1) through solution heat exchanger (7) to be adjusted to generator (2) and have concentrated solution pipeline through second
Solution heat exchanger (24) is connected with the second generator (21), and the second generator (21) has concentrated solution pipeline again through solution heat exchange
Device (7) is connected with absorber (1), generator (2) is had refrigerant steam channel to connect with compressor (8) and is adjusted to generator (2)
After having refrigerant steam channel to connect with the second generator (21), the second generator (21) has cryogen liquid pipeline again through the second throttling
Valve (22) is connected with condenser (3), and the second generator (21) also has refrigerant steam channel to connect with compressor (8), forms first
Class thermal drivers compressing-absorbing type heat pump.
36. first kind thermal drivers compressing-absorbing type heat pumps, are the arbitrary first kind thermal drivers pressures described in claim 24-31
In contracting-absorption heat pump, increase the second generator, second throttle, the second solution pump and the second solution heat exchanger, will absorb
Device (1) has weak solution pipeline to connect with generator (2) through solution pump (6) and solution heat exchanger (7) to be adjusted to absorber (1) and have
Weak solution pipeline is connected with the second generator (21) with solution heat exchanger (7) through solution pump (6), and the second generator (21) has again
Concentrated solution pipeline is connected with generator (2) with the second solution heat exchanger (24) through the second solution pump (23), and generator (2) is had
Concentrated solution pipeline is connected with absorber (1) through solution heat exchanger (7) and is adjusted to generator (2) and has concentrated solution pipeline molten through second
Liquid heat exchanger (24) is connected with absorber (1) with solution heat exchanger (7), and generator (2) is had refrigerant steam channel and pressure
Contracting machine (8) connection is adjusted to the second generator after generator (2) has refrigerant steam channel to connect with the second generator (21)
(21) cryogen liquid pipeline is had to connect with condenser (3) through second throttle (22) again, the second generator (21) also has refrigerant vapour
Passage is connected with compressor (8), forms first kind thermal drivers compressing-absorbing type heat pump.
37. first kind thermal drivers compressing-absorbing type heat pumps, are the arbitrary first kind thermal drivers pressures described in claim 24-31
In contracting-absorption heat pump, increase the second generator, second throttle, the second solution pump and the second solution heat exchanger, absorber
(1) set up weak solution pipeline to connect with the second generator (21) with the second solution heat exchanger (24) through the second solution pump (23),
Second generator (21) also has concentrated solution pipeline to connect with absorber (1) through the second solution heat exchanger (24), by compressor (8)
There is refrigerant steam channel to connect with condenser (3) to be adjusted to compressor (8) and have refrigerant steam channel and the second generator (21) even
After logical, the second generator (21) has cryogen liquid pipeline to connect with condenser (3) through second throttle (22) again, the second generator
(21) also have refrigerant steam channel to connect with condenser (3), form first kind thermal drivers compressing-absorbing type heat pump.
38. first kind thermal drivers compressing-absorbing type heat pumps, are the arbitrary first kind thermal drivers pressures described in claim 24-31
In contracting-absorption heat pump, increase the second generator, second throttle and the second solution heat exchanger, absorber (1) is had dilute molten
Liquid pipeline is connected with generator (2) through solution pump (6) and solution heat exchanger (7) and is adjusted to absorber (1) and has weak solution pipeline
Connect with generator (2) with the second solution heat exchanger (24) through solution pump (6), solution heat exchanger (7), by generator (2)
There is concentrated solution pipeline to connect with absorber (1) through solution heat exchanger (7) to be adjusted to generator (2) and have concentrated solution pipeline through second
Solution heat exchanger (24) is connected with the second generator (21), and the second generator (21) has concentrated solution pipeline again through solution heat exchange
Device (7) is connected with absorber (1), compressor (8) is had refrigerant steam channel to connect with condenser (3) and is adjusted to compressor (8)
After having refrigerant steam channel to connect with the second generator (21), the second generator (21) has cryogen liquid pipeline again through the second throttling
Valve (22) is connected with condenser (3), and the second generator (21) also has refrigerant steam channel to connect with condenser (3), forms first
Class thermal drivers compressing-absorbing type heat pump.
39. first kind thermal drivers compressing-absorbing type heat pump, it is the arbitrary first kind thermal drivers pressure described in claim 24-31
In contracting-absorption heat pump, increase the second generator, second throttle, the second solution pump and the second solution heat exchanger, will absorb
Device (1) has weak solution pipeline to connect with generator (2) through solution pump (6) and solution heat exchanger (7) to be adjusted to absorber (1) and have
Weak solution pipeline is connected with the second generator (21) with solution heat exchanger (7) through solution pump (6), and the second generator (21) has again
Concentrated solution pipeline is connected with generator (2) with the second solution heat exchanger (24) through the second solution pump (23), and generator (2) is had
Concentrated solution pipeline is connected with absorber (1) through solution heat exchanger (7) and is adjusted to generator (2) and has concentrated solution pipeline molten through second
Liquid heat exchanger (24) is connected with absorber (1) with solution heat exchanger (7), by compressor (8) have refrigerant steam channel with cold
Condenser (3) connection is adjusted to the second generator after compressor (8) has refrigerant steam channel to connect with the second generator (21)
(21) cryogen liquid pipeline is had to connect with condenser (3) through second throttle (22) again, the second generator (21) also has refrigerant vapour
Passage is connected with condenser (3), forms first kind thermal drivers compressing-absorbing type heat pump.
40. first kind thermal drivers compressing-absorbing type heat pumps, are the arbitrary first kind thermal drivers pressures described in claim 34-39
In contracting-absorption heat pump, increase heater, by gas turbine (11) have blast tube be sequentially communicated high temperature regenerator (20) and
After generator (2), generator (2) has blast tube and ft connection to be adjusted to gas turbine (11) again and has blast tube successively
After connection high temperature regenerator (20), generator (2) and heater (17), heater (17) has blast tube and ft connection again,
Heater (17) also has heated medium passage and ft connection, forms first kind thermal drivers compressing-absorbing type heat pump.
41. first kind thermal drivers compressing-absorbing type heat pumps, are the arbitrary first kind thermal drivers pressures described in claim 34-39
In contracting-absorption heat pump, increase heater, by gas turbine (11) have blast tube be sequentially communicated high temperature regenerator (20) and
After generator (2), generator (2) has blast tube and ft connection to be adjusted to gas turbine (11) again and has blast tube successively
Connection high temperature regenerator (20), the finisher (4) of generator (2), heater (17) and evaporimeter (4) have again blast tube and
Ft connection, heater (17) also has heated medium passage and ft connection, forms first kind thermal drivers compressing-absorbing type heat
Pump.
42. first kind thermal drivers compressing-absorbing type heat pumps, are the arbitrary first kind thermal drivers pressures described in claim 34-39
In contracting-absorption heat pump, after gas turbine (11) is had blast tube to be sequentially communicated high temperature regenerator (20) and generator (2)
Generator (2) has blast tube and ft connection to be adjusted to gas turbine (11) again has blast tube to be sequentially communicated high temperature regenerator
(20), after generator (2) and the second generator (21), the second generator (21) has blast tube and ft connection again, forms the
One class thermal drivers compressing-absorbing type heat pump.
43. first kind thermal drivers compressing-absorbing type heat pumps, are the arbitrary first kind thermal drivers pressures described in claim 34-39
In contracting-absorption heat pump, increase heater, gas turbine (11) is had blast tube to be sequentially communicated high temperature regenerator (20) and sends out
After raw device (2), generator (2) has blast tube and ft connection to be adjusted to gas turbine (11) again has blast tube to connect successively
After logical high temperature regenerator (20), generator (2), the second generator (21) and heater (17), heater (17) has combustion gas to lead to again
Road and ft connection, heater (17) also has heated medium passage and ft connection, forms first kind thermal drivers compression-absorption
Formula heat pump.
44. first kind thermal drivers compressing-absorbing type heat pumps, are the arbitrary first kind thermal drivers pressures described in claim 34-39
In contracting-absorption heat pump, increase heater, gas turbine (11) is had blast tube to be sequentially communicated high temperature regenerator (20) and sends out
After raw device (2), generator (2) has blast tube and ft connection to be adjusted to gas turbine (11) again has blast tube to connect successively
Logical high temperature regenerator (20), generator (2), the finisher (4) of the second generator (21), heater (17) and evaporimeter (4)
There are blast tube and ft connection again, heater (17) also has heated medium passage and ft connection, form first kind heat and drive
Dynamic pressure contracting-absorption heat pump.
45. first kind thermal drivers compressing-absorbing type heat pump, it is the arbitrary first kind thermal drivers pressure described in claim 23-30
In contracting-absorption heat pump, increase the second generator, the second absorber, the second solution pump and the second solution heat exchanger, will evaporate
Device (4) has refrigerant steam channel to connect with absorber (1) to be adjusted to evaporimeter (4) and have refrigerant steam channel and the second absorber
(25) connect, the second absorber (25) also have weak solution pipeline through the second solution pump (23) and the second solution heat exchanger (24) and
Second generator (21) connects, and the second generator (21) also has concentrated solution pipeline through the second solution heat exchanger (24) and the second suction
Receive device (25) connection, the second generator (21) also has refrigerant steam channel to connect with absorber (1), and gas turbine (11) is had combustion
After gas passage is sequentially communicated high temperature regenerator (20) and generator (2), generator (2) has blast tube to adjust with ft connection again
Whole for gas turbine (11) have blast tube be sequentially communicated high temperature regenerator (20), generator (2) and the second generator (21) it
Second generator (21) has blast tube and ft connection more afterwards, and the second absorber (25) also has heated medium passage and outside
Connection, forms first kind thermal drivers compressing-absorbing type heat pump.
46. first kind thermal drivers compressing-absorbing type heat pumps, are the arbitrary first kind thermal drivers pressures described in claim 23-30
In contracting-absorption heat pump, increase the second generator, the second absorber, the second solution pump, solution choke valve, the second solution throttling
Valve and point steam chest, absorber (1) is had weak solution pipeline to connect with generator (2) with solution heat exchanger (7) through solution pump (6)
Being adjusted to absorber (1) has weak solution pipeline to connect with the second absorber (25) with solution heat exchanger (7) through solution pump (6),
Second absorber (25) also has weak solution pipeline to connect with the second generator (21) through solution choke valve (26), the second generator
(21) there is concentrated solution pipeline to connect with generator (2) through the second solution pump (23) again, generator (2) is had concentrated solution pipeline through molten
Liquid heat exchanger (7) connect with absorber (1) be adjusted to generator (2) have concentrated solution pipeline through the second solution choke valve (27) and
Second absorber (25) is connected with a point steam chest (28), and a point steam chest (28) has concentrated solution pipeline again through solution heat exchanger (7) and suction
Receive device (1) connection, generator (2) is had refrigerant steam channel to connect with compressor (8) and is adjusted to generator (2) and has refrigerant vapour
Passage is connected with the second absorber (25), and the second generator (21) and a point steam chest (28) also have refrigerant steam channel and compression respectively
Machine (8) connects, and gas turbine (11) is had blast tube to be sequentially communicated high temperature regenerator (20) and generator (2) generator afterwards
(2) have again blast tube and ft connection be adjusted to gas turbine (11) have blast tube be sequentially communicated high temperature regenerator (20),
After generator (2) and the second generator (21), the second generator (21) has blast tube and ft connection again, forms the first kind
Thermal drivers compressing-absorbing type heat pump.
47. first kind thermal drivers compressing-absorbing type heat pumps, are the arbitrary first kind thermal drivers pressures described in claim 1-46
In contracting-absorption heat pump, increase engine, engine connects the 3rd compressor (12) and moves to the 3rd compressor (12) transmission
Power, forms additional external power-actuated first kind thermal drivers compressing-absorbing type heat pump.
48. first kind thermal drivers compressing-absorbing type heat pumps, are the arbitrary first kind thermal drivers pressures described in claim 1-46
In contracting-absorption heat pump, increase working machine, gas turbine (11) connects working machine and transmits power to working machine, is formed additional
The first kind thermal drivers compressing-absorbing type heat pump of living load is externally provided.
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CN110440479A (en) * | 2018-07-01 | 2019-11-12 | 李华玉 | Combined cycle heat pump assembly |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5230225A (en) * | 1992-08-17 | 1993-07-27 | Gas Research Institute | Absorption refrigeration system burner and generator assembly |
CN103851823A (en) * | 2013-02-21 | 2014-06-11 | 李华玉 | Composite generation first-class absorption heat pump |
CN104154674A (en) * | 2014-08-21 | 2014-11-19 | 珠海格力电器股份有限公司 | Second-class absorption heat pump system and heating method thereof |
CN104929706A (en) * | 2014-05-28 | 2015-09-23 | 李华玉 | Combined circulating energy supply system |
-
2016
- 2016-08-29 CN CN201610820920.7A patent/CN106440497A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5230225A (en) * | 1992-08-17 | 1993-07-27 | Gas Research Institute | Absorption refrigeration system burner and generator assembly |
CN103851823A (en) * | 2013-02-21 | 2014-06-11 | 李华玉 | Composite generation first-class absorption heat pump |
CN104929706A (en) * | 2014-05-28 | 2015-09-23 | 李华玉 | Combined circulating energy supply system |
CN104154674A (en) * | 2014-08-21 | 2014-11-19 | 珠海格力电器股份有限公司 | Second-class absorption heat pump system and heating method thereof |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110440479A (en) * | 2018-07-01 | 2019-11-12 | 李华玉 | Combined cycle heat pump assembly |
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