CN105041396B - Combined cycle energy supplying system - Google Patents
Combined cycle energy supplying system Download PDFInfo
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- CN105041396B CN105041396B CN201510330916.8A CN201510330916A CN105041396B CN 105041396 B CN105041396 B CN 105041396B CN 201510330916 A CN201510330916 A CN 201510330916A CN 105041396 B CN105041396 B CN 105041396B
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Abstract
The present invention provides combined cycle energy supplying system, belongs to heat energy utilization and technical field of heat pumps.Turbine, boiler, heat exchanger and circulating pump constitute Steam Power Equipment forward circulation system, turbine, boiler, heat exchanger and circulating pump constitute Steam Power Equipment forward circulation system, compressor, cooler, expanding machine, low temperature heat exchanger and regenerator constitute compression reverse circulation system, and absorber, the second absorber, generator, the second generator, condenser, evaporator, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger constitute absorption reverse circulation system;Steam Power Equipment forward circulation provides power to compression reverse circulation, provides driving thermic load to absorption reverse circulation, compression reverse circulation obtains low temperature thermic load and passes through cooler heat supply, absorption reverse circulation obtains low temperature thermic load and by absorber, the second absorber and condenser heat supply, forms combined cycle energy supplying system.
Description
Technical field:
The invention belongs to power, refrigeration and technical field of heat pumps.
Background technique:
Exist in the system that fuel carries out heat supply by burning, between the combustion gas and heated medium of formation of burning very big
The temperature difference;In the system directly freezed using fuel by burning, the combustion gas for formation of burning and refrigerating plant work are situated between
The very big temperature difference is equally existed between matter;In the distributed energy resource system for providing heat source using fuel combustion, power provides real
It is a restricted additional conditions on border, and many times remains the situation that the temperature difference cannot make full use of.Summarize difficulty
To realize situation that thermal energy efficiently utilizes, can mainly be summarized as seven aspects: 1. without living load in the case of, combustion gas with added
There are the unserviceable big temperature difference between thermal medium, it cannot achieve thermal energy and efficiently utilize;2. configure absorption heat pump, absorbed
The limitation in formula heat pump working media operating temperature section drives between combustion gas and absorption heat pump working media there are the big temperature difference,
The temperature difference utilizes unreasonable;3. configuring waste heat boiler, combustion gas provides sensible heat to waste heat boiler, and in steam generation link, there are larger temperature
Difference;When using steam drive absorption heat pump, this will lead to the temperature difference using unreasonable;4. Low Temperature Thermal resource shortage, it is difficult to benefit
With the thermal energy in environment;5. the thermal performance of suitable absorption heat pump unit can not be found when low temperature thermal resource temperature is very low
With all satisfactory working media of security performance;6. when inferior fuel, gas-turbine installation cannot be directlyed adopt to realize height
Warm the reasonable utilization of energy;7. combustion gas low-temperature zone thermal energy is difficult to realize efficient heat supply or highly effective refrigeration.
In view of the above problems, and special consideration should be given to the efficient and deep exploitation of combustion gas low-temperature zone thermal energy, inventor is mentioned
Combined cycle energy supplying system out converts mechanical energy, mechanical energy for the high temperature heat of combustion gas by air-steam combined cycle power plant
It drives compression reverse circulation or power is externally provided simultaneously, the waste heat load of air-steam combined cycle power plant, which drives, to be absorbed
Formula reverse circulation is obtained by compression reverse circulation and absorption reverse circulation and is promoted the temperature of low-grade heat load, reduces
The limiting factor that thermal energy efficiently utilizes, and realize efficient heating and highly effective refrigeration in the case of inferior fuel.
Summary of the invention:
Present invention is primarily intended to combined cycle energy supplying system to be provided, specific summary of the invention subitem is described below:
1. combined cycle energy supplying system, mainly by compressor, boiler, air turbine, steam turbine, waste heat boiler, circulation
Pump, heat exchanger, compressor, cryogenic throttle valve, low temperature heat exchanger, evaporator, absorber, the second absorber, generator,
Two generators, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger institute group
At;Compressor has air duct to be connected to outside, and boiler has pressure again after compressor is connected to there are also compressed air channel with boiler
Contracting air duct is connected to air turbine, and there are also fuel and air channels be connected to outside for boiler, boiler there are also blast tube and
Waste heat boiler connection, there are also air ducts to be connected to waste heat boiler for air turbine, and there are also mixed-gas channels for waste heat boiler successively
The second generator has mixed-gas channel to be connected to outside again after connection generator and the second generator, and steam turbine has low pressure
Steam channel is connected to heat exchanger, and there are also condensate liquid pipelines to be connected to through circulating pump with waste heat boiler for heat exchanger, waste heat boiler
There are also high steam channels to be connected to steam turbine, heat exchanger there are also heated medium pipeline with outside be connected to;Compressor has
The finisher that refrigerant steam channel is connected to evaporator has cryogen liquid pipeline to connect through cryogenic throttle valve and low temperature heat exchanger again
Logical, there are also refrigerant steam channels to be communicated with compressor for low temperature heat exchanger, and low temperature heat exchanger is there are also cryogenic media pipeline and outside
Portion's connection;There are also refrigerant steam channels to be connected to absorber for evaporator, and there are also weak solution pipelines through solution pump and solution for absorber
Heat exchanger is connected to the second absorber, and there are also weak solution pipelines through the second solution pump and the second solution heat exchange for the second absorber
Device is connected to generator, and there are also concentrated solution pipelines to be connected to through the second solution heat exchanger with the second generator for generator, the second hair
There are also concentrated solution pipelines be connected to through solution heat exchanger with absorber for raw device, and there are also refrigerant steam channels and condenser company for generator
Logical, there are also refrigerant steam channels to be connected to the second absorber for the second generator, condenser there are also cryogen liquid pipelines through throttle valve and
Evaporator connection, absorber, the second absorber and condenser also have heated medium pipeline to be connected to outside respectively;Compressor,
Boiler, air turbine, steam turbine, waste heat boiler, circulating pump and heat exchanger constitute air-steam forward circulation system, pressure
Contracting machine, evaporator, cryogenic throttle valve and low temperature heat exchanger constitute compression reverse circulation system, absorber, the second absorber,
Generator, the second generator, condenser, evaporator, throttle valve, solution pump, the second solution pump, solution heat exchanger and second are molten
Liquid heat exchanger constitutes absorption reverse circulation system;Air-steam forward circulation to compression reverse circulation provide power or
Power is externally provided simultaneously, and air-steam forward circulation provides driving thermic load to absorption reverse circulation, and compression inversely follows
Ring obtains low temperature thermic load and by evaporator to absorption reverse circulation heat supply, and absorption reverse circulation passes through absorber, the
Two absorbers and the external heat supply of condenser form combined cycle energy supplying system.
It is to increase by the second compressor in the combined cycle energy supplying system described in the 1st 2. combined cycle energy supplying system,
There is cryogen liquid pipeline through cryogenic throttle valve and low temperature again the finisher that compressor has refrigerant steam channel to be connected to evaporator
The finisher that heat exchanger connection is adjusted to compressor and has refrigerant steam channel to be connected to evaporator has refrigerant steam channel again
It is connected to the second compressor, there are also the finishers that refrigerant steam channel is connected to evaporator cryogen liquid pipe again for the second compressor
Road is connected to through cryogenic throttle valve with low temperature heat exchanger, forms combined cycle energy supplying system.
3. combined cycle energy supplying system, mainly by compressor, boiler, air turbine, steam turbine, waste heat boiler, circulation
Pump, heat exchanger, compressor, the second condenser, cryogenic throttle valve, low temperature heat exchanger, evaporator, absorber, second absorb
Device, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat
Exchanger is formed;Compressor has air duct to be connected to outside, after compressor is connected to there are also compressed air channel with boiler
Boiler has compressed air channel to be connected to air turbine again, boiler there are also fuel and air channel with outside be connected to, boiler is also
Blast tube is connected to waste heat boiler, and there are also air ducts to be connected to waste heat boiler for air turbine, and there are also gaseous mixtures for waste heat boiler
The second generator has mixed-gas channel to be connected to outside again after body channel is sequentially communicated generator and the second generator, steam
Turbine has low-pressure steam channel to be connected to heat exchanger, and there are also condensate liquid pipelines through circulating pump and waste heat boiler company for heat exchanger
Logical, there are also high steam channels to be connected to steam turbine for waste heat boiler, and there are also heated medium pipelines to connect with outside for heat exchanger
It is logical;The second condenser has cryogen liquid pipeline to throttle through low temperature again after compressor has refrigerant steam channel to be connected to the second condenser
Valve is connected to low temperature heat exchanger, and there are also refrigerant steam channels to be communicated with compressor for low temperature heat exchanger, and low temperature heat exchanger is also
There is cryogenic media pipeline be connected to outside, there are also heated medium pipelines to be connected to external for the second condenser;Evaporator has cryogen
Steam channel is connected to absorber, and there are also weak solution pipelines through solution pump and solution heat exchanger and the second absorber company for absorber
Logical, there are also weak solution pipelines to be connected to through the second solution pump and the second solution heat exchanger with generator for the second absorber, generator
There are also concentrated solution pipelines to be connected to through the second solution heat exchanger with the second generator, and there are also concentrated solution pipelines through molten for the second generator
Liquid heat exchanger is connected to absorber, and there are also refrigerant steam channels to be connected to condenser for generator, and there are also cryogens for the second generator
Steam channel is connected to the second absorber, and there are also cryogen liquid pipelines to be connected to through throttle valve with evaporator for condenser, and evaporator is also
Cryogenic media pipeline is connected to outside, and absorber, the second absorber and condenser also have heated medium pipeline and outside respectively
Connection;It is positive that compressor, boiler, air turbine, steam turbine, waste heat boiler, circulating pump and heat exchanger constitute air-steam
The circulatory system, compressor, the second condenser, cryogenic throttle valve and low temperature heat exchanger constitute compression reverse circulation system, inhale
Receive device, the second absorber, generator, the second generator, condenser, evaporator, throttle valve, solution pump, the second solution pump, solution
Heat exchanger and the second solution heat exchanger constitute absorption reverse circulation system;Air-steam forward circulation is inverse to compression
Power is provided to circulation or power is externally provided simultaneously, and air-steam forward circulation provides driving heat to absorption reverse circulation
Load, compression reverse circulation obtain low temperature thermic load and by the external heat supplies of the second condenser, and absorption reverse circulation obtains
Low temperature thermic load simultaneously passes through absorber, the second absorber and the external heat supply of condenser, formation combined cycle energy supplying system.
It is to increase by the second compressor in the combined cycle energy supplying system described in the 3rd 4. combined cycle energy supplying system,
The second condenser has cryogen liquid pipeline to throttle through low temperature again after having refrigerant steam channel to be connected to the second condenser on compressor
Valve is connected to low temperature heat exchanger be adjusted to compressor and there is refrigerant steam channel to be connected to the second condenser after the second condenser
There is refrigerant steam channel to be connected to the second compressor again, there are also refrigerant steam channels to be connected to it with the second condenser for the second compressor
The second condenser has cryogen liquid pipeline to be connected to through cryogenic throttle valve with low temperature heat exchanger again afterwards, forms combined cycle energy supply system
System.
5. combined cycle energy supplying system, mainly by compressor, boiler, air turbine, steam turbine, waste heat boiler, circulation
Pump, heat exchanger, compressor, cooler, cryogenic throttle valve, low temperature heat exchanger, evaporator, absorber, the second absorber, hair
Raw device, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchange
Device is formed;Compressor has air duct to be connected to outside, boiler after compressor is connected to there are also compressed air channel with boiler
There is compressed air channel to be connected to air turbine again, boiler there are also fuel and air channel with outside be connected to, there are also combustion gas for boiler
Channel is connected to waste heat boiler, and there are also air ducts to be connected to waste heat boiler for air turbine, and that there are also mixed gas is logical for waste heat boiler
The second generator has mixed-gas channel to be connected to outside again after road is sequentially communicated generator and the second generator, steam turbine
There is low-pressure steam channel to be connected to heat exchanger, there are also condensate liquid pipelines to be connected to through circulating pump with waste heat boiler for heat exchanger, remaining
There are also high steam channels to be connected to steam turbine for heat boiler, and there are also heated medium pipelines to be connected to outside for heat exchanger;Pressure
The aftercooler that contracting machine has refrigerant steam channel to be connected to cooler has refrigerant steam channel to be connected to evaporator again, and evaporator is also
There is cryogen liquid pipeline to be connected to through cryogenic throttle valve with low temperature heat exchanger, there are also refrigerant steam channels and compression for low temperature heat exchanger
Machine connection, there are also cryogenic media pipelines be connected to external for low temperature heat exchanger, and there are also heated medium pipelines and outside for cooler
Connection;There are also refrigerant steam channels to be connected to absorber for evaporator, and there are also weak solution pipelines through solution pump and solution heat for absorber
Exchanger is connected to the second absorber, and there are also weak solution pipelines through the second solution pump and the second solution heat exchanger for the second absorber
It is connected to generator, there are also concentrated solution pipelines to be connected to through the second solution heat exchanger with the second generator for generator, and second occurs
There are also concentrated solution pipelines to be connected to through solution heat exchanger with absorber for device, and there are also refrigerant steam channels and condenser to connect for generator
Logical, there are also refrigerant steam channels to be connected to the second absorber for the second generator, condenser there are also cryogen liquid pipelines through throttle valve and
Evaporator connection, absorber, the second absorber and condenser also have heated medium pipeline to be connected to outside respectively;Compressor,
Boiler, air turbine, steam turbine, waste heat boiler, circulating pump and heat exchanger constitute air-steam forward circulation system, pressure
Contracting machine, cooler, evaporator, cryogenic throttle valve and low temperature heat exchanger constitute compression reverse circulation system, absorber, second
Absorber, generator, the second generator, condenser, evaporator, throttle valve, solution pump, the second solution pump, solution heat exchanger
Absorption reverse circulation system is constituted with the second solution heat exchanger;Air-steam forward circulation is mentioned to compression reverse circulation
Power is externally provided for power or simultaneously, and air-steam forward circulation provides driving thermic load, compression to absorption reverse circulation
Formula reverse circulation obtains low temperature thermic load and passes through the external heat supply of cooler respectively and pass through evaporator to absorption reverse circulation
Heat supply, absorption reverse circulation form combined cycle energy supply system by absorber, the second absorber and the external heat supply of condenser
System.
It is to increase by the second compressor in the combined cycle energy supplying system described in the 5th 6. combined cycle energy supplying system,
There is refrigerant steam channel to be connected to adjustment with evaporator again the aftercooler that compressor has refrigerant steam channel to be connected to cooler
There is refrigerant steam channel to be connected to the second compressor again for the aftercooler that compressor has refrigerant steam channel to be connected to cooler,
There are also the aftercoolers that refrigerant steam channel is connected to cooler to have refrigerant steam channel to be connected to evaporator again for second compressor,
Form combined cycle energy supplying system.
7. combined cycle energy supplying system, mainly by compressor, boiler, air turbine, steam turbine, waste heat boiler, circulation
Pump, heat exchanger, compressor, the second compressor, the second condenser, cryogenic throttle valve, the second cryogenic throttle valve, low temperature heat exchange
Device, evaporator, absorber, the second absorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution
Pump, solution heat exchanger and the second solution heat exchanger are formed;Compressor has air duct to be connected to outside, and compressor is also
Boiler has compressed air channel to be connected to air turbine again after compressed air channel is connected to boiler, and there are also fuel and sky for boiler
Gas channel is connected to outside, and there are also blast tubes to be connected to waste heat boiler for boiler, and there are also air ducts and waste heat pot for air turbine
Furnace connection, waste heat boiler there are also mixed-gas channel be sequentially communicated the second generator after generator and the second generator have again it is mixed
It closes gas passage to be connected to outside, steam turbine has low-pressure steam channel to be connected to heat exchanger, and there are also condensate liquids for heat exchanger
Pipeline is connected to through circulating pump with waste heat boiler, and there are also high steam channels to be connected to steam turbine for waste heat boiler, and heat exchanger is also
There is heated medium pipeline to be connected to outside;Compressor has low pressure refrigerant steam channel to be connected to evaporator, and there are also low for evaporator
Pressure cryogen liquid pipeline be connected to through cryogenic throttle valve with low temperature heat exchanger after low temperature heat exchanger have again refrigerant steam channel and
Compressor connection, there are also low pressure refrigerant steam channels to be connected to the second compressor for compressor, and there are also high pressure cryogens for the second compressor
Steam channel is connected to the second condenser, and there are also high pressure cryogen liquid pipelines through evaporator and the second cryogenic throttle valve for the second condenser
Low temperature heat exchanger has refrigerant steam channel to be communicated with compressor again after being connected to low temperature heat exchanger, and low temperature heat exchanger is also
There is cryogenic media pipeline be connected to outside, there are also heated medium pipelines to be connected to external for the second condenser;There are also cold for evaporator
Agent steam channel is connected to absorber, and there are also weak solution pipelines through solution pump and solution heat exchanger and the second absorber for absorber
Connection, there are also weak solution pipelines to be connected to through the second solution pump and the second solution heat exchanger with generator for the second absorber, generation
There are also concentrated solution pipelines to be connected to through the second solution heat exchanger with the second generator for device, and there are also concentrated solution pipeline warps for the second generator
Solution heat exchanger is connected to absorber, and there are also refrigerant steam channels to be connected to condenser for generator, and there are also cold for the second generator
Agent steam channel is connected to the second absorber, and there are also cryogen liquid pipelines to be connected to through throttle valve with evaporator for condenser, absorber,
Two absorbers and condenser also have heated medium pipeline to be connected to outside respectively;Compressor, boiler, air turbine, vapor wheel
Machine, waste heat boiler, circulating pump and heat exchanger constitute air-steam forward circulation system, compressor, the second compressor, second
Condenser, evaporator, cryogenic throttle valve, the second cryogenic throttle valve and low temperature heat exchanger constitute compression reverse circulation system;
It is absorber, the second absorber, generator, the second generator, condenser, evaporator, throttle valve, solution pump, the second solution pump, molten
Liquid heat exchanger and the second solution heat exchanger constitute absorption reverse circulation system;Air-steam forward circulation is to compression
Reverse circulation provides power or externally provides power simultaneously, and air-steam forward circulation provides driving to absorption reverse circulation
Thermic load, compression reverse circulation obtain low temperature thermic load and respectively by the external heat supply of the second condenser and by evaporator to
Absorption reverse circulation heat supply, absorption reverse circulation form connection by absorber, the second absorber and the external heat supply of condenser
Close circulation energy supplying system.
8. combined cycle energy supplying system, mainly by compressor, boiler, air turbine, steam turbine, waste heat boiler, circulation
Pump, heat exchanger, compressor, the second condenser, cryogenic throttle valve, the second cryogenic throttle valve, low temperature heat exchanger, evaporator,
Absorber, the second absorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat are handed over
Parallel operation and the second solution heat exchanger are formed;Compressor has air duct to be connected to outside, and there are also compressed airs to lead to for compressor
Boiler has compressed air channel to be connected to air turbine again after road is connected to boiler, and boiler is there are also fuel and air channel and outside
Portion's connection, there are also blast tubes to be connected to waste heat boiler for boiler, and there are also air ducts to be connected to waste heat boiler for air turbine, waste heat
The second generator has mixed-gas channel again after boiler is sequentially communicated generator and the second generator there are also mixed-gas channel
It is connected to outside, steam turbine has low-pressure steam channel to be connected to heat exchanger, and there are also condensate liquid pipelines through recycling for heat exchanger
Pump is connected to waste heat boiler, and there are also high steam channels to be connected to steam turbine for waste heat boiler, and heat exchanger is also heated Jie
Matter pipeline is connected to outside;Compressor has low pressure refrigerant steam channel to be connected to evaporator, and there are also low pressure cryogen liquid pipes for evaporator
Low temperature heat exchanger has refrigerant steam channel to be communicated with compressor again after road is connected to through cryogenic throttle valve with low temperature heat exchanger,
There are also high pressure refrigerant steam channels to be connected to the second condenser for compressor, and there are also high pressure cryogen liquid pipelines through evaporating for the second condenser
Low temperature heat exchanger has refrigerant steam channel and compressor again after device and the second cryogenic throttle valve are connected to low temperature heat exchanger
Connection, there are also cryogenic media pipelines be connected to external for low temperature heat exchanger, the second condenser there are also heated medium pipeline with outside
Portion's connection;There are also refrigerant steam channels to be connected to absorber for evaporator, and there are also weak solution pipelines through solution pump and solution for absorber
Heat exchanger is connected to the second absorber, and there are also weak solution pipelines through the second solution pump and the second solution heat exchange for the second absorber
Device is connected to generator, and there are also concentrated solution pipelines to be connected to through the second solution heat exchanger with the second generator for generator, the second hair
There are also concentrated solution pipelines be connected to through solution heat exchanger with absorber for raw device, and there are also refrigerant steam channels and condenser company for generator
Logical, there are also refrigerant steam channels to be connected to the second absorber for the second generator, condenser there are also cryogen liquid pipelines through throttle valve and
Evaporator connection, absorber, the second absorber and condenser also have heated medium pipeline to be connected to outside respectively;Compressor,
Boiler, air turbine, steam turbine, waste heat boiler, circulating pump and heat exchanger constitute air-steam forward circulation system, pressure
It is reverse that contracting machine, the second condenser, evaporator, cryogenic throttle valve, the second cryogenic throttle valve and low temperature heat exchanger constitute compression
The circulatory system, absorber, the second absorber, generator, the second generator, condenser, evaporator, throttle valve, solution pump, second
Solution pump, solution heat exchanger and the second solution heat exchanger constitute absorption reverse circulation system;Air-steam forward circulation
Power is provided to compression reverse circulation or power is externally provided simultaneously, and air-steam forward circulation is to absorption reverse circulation
Driving thermic load is provided, compression reverse circulation obtains low temperature thermic load and passes through the external heat supply of the second condenser respectively and pass through
Evaporator is externally supplied to absorption reverse circulation heat supply, absorption reverse circulation by absorber, the second absorber and condenser
Heat forms combined cycle energy supplying system.
9. combined cycle energy supplying system, mainly by compressor, boiler, air turbine, steam turbine, waste heat boiler, circulation
Pump, heat exchanger, compressor, expanding machine, low temperature heat exchanger, evaporator, absorber, the second absorber, generator, the second hair
Raw device, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger device are formed;
Compressor has air duct to be connected to outside, and boiler has compression empty again after compressor is connected to there are also compressed air channel with boiler
Gas channel is connected to air turbine, boiler there are also fuel and air channel with outside be connected to, there are also blast tubes and waste heat for boiler
Boiler connection, there are also air ducts to be connected to waste heat boiler for air turbine, and there are also mixed-gas channels to be sequentially communicated for waste heat boiler
The second generator has mixed-gas channel to be connected to outside again after generator and the second generator, and steam turbine has low-pressure steam
Channel is connected to heat exchanger, and there are also condensate liquid pipelines to be connected to through circulating pump with waste heat boiler for heat exchanger, and waste heat boiler is also
High steam channel is connected to steam turbine, heat exchanger there are also heated medium pipeline with outside be connected to;Compressor has cryogen
The finisher that gas passage is connected to evaporator has refrigerant gas channel to be connected to expanding machine again, and there are also refrigerant gas for expanding machine
Channel is communicated with compressor through low temperature heat exchanger, low temperature heat exchanger there are also cryogenic media pipeline with outside be connected to;Evaporator
There are also refrigerant steam channels to be connected to absorber, and there are also weak solution pipelines through solution pump and solution heat exchanger and second for absorber
Absorber connection, there are also weak solution pipelines through the second solution pump and the second solution heat exchanger and generator company for the second absorber
Logical, there are also concentrated solution pipelines to be connected to through the second solution heat exchanger with the second generator for generator, and there are also dense molten for the second generator
Liquid pipeline is connected to through solution heat exchanger with absorber, and there are also refrigerant steam channels to be connected to condenser for generator, and second occurs
There are also refrigerant steam channels to be connected to the second absorber for device, and there are also cryogen liquid pipelines to be connected to through throttle valve with evaporator for condenser,
Absorber, the second absorber and condenser also have heated medium pipeline to be connected to outside respectively;Compressor, boiler, Air wheel
Machine, steam turbine, waste heat boiler, circulating pump and heat exchanger constitute air-steam forward circulation system, compressor, evaporator,
Expanding machine and low temperature heat exchanger constitute compression reverse circulation system, and absorber, the second absorber, generator, second occur
Device, condenser, evaporator, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger are constituted
Absorption reverse circulation system;Air-steam forward circulation provides power to compression reverse circulation or externally provides simultaneously dynamic
Power, air-steam forward circulation provide driving thermic load to absorption reverse circulation, and it is negative that compression reverse circulation obtains Low Temperature Thermal
Lotus simultaneously passes through evaporator to absorption reverse circulation heat supply, and absorption reverse circulation passes through absorber, the second absorber and condensation
The external heat supply of device forms combined cycle energy supplying system.
It is to increase by the second compressor in the combined cycle energy supplying system described in the 9th 10. combined cycle energy supplying system,
There is refrigerant gas channel to be connected to adjustment with expanding machine again the finisher that compressor has refrigerant gas channel to be connected to evaporator
There is refrigerant gas channel to be connected to the second compressor again for the finisher that compressor has refrigerant gas channel to be connected to evaporator,
There are also the finishers that refrigerant gas channel is connected to evaporator to have refrigerant gas channel to be connected to expanding machine again for second compressor,
Form combined cycle energy supplying system.
11. combined cycle energy supplying system, mainly by compressor, boiler, air turbine, steam turbine, waste heat boiler, circulation
Pump, compressor, expanding machine, low temperature heat exchanger, regenerator, evaporator, absorber, the second absorber, occurs heat exchanger
Device, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger
It is formed;Compressor has air duct to be connected to outside, and boiler is again after compressor is connected to there are also compressed air channel with boiler
There is compressed air channel to be connected to air turbine, boiler there are also fuel and air channel with outside be connected to, boiler there are also combustion gas lead to
Road is connected to waste heat boiler, and there are also air ducts to be connected to waste heat boiler for air turbine, and there are also mixed-gas channels for waste heat boiler
The second generator has mixed-gas channel to be connected to outside again after being sequentially communicated generator and the second generator, and steam turbine has
Low-pressure steam channel is connected to heat exchanger, and there are also condensate liquid pipelines to be connected to through circulating pump with waste heat boiler for heat exchanger, waste heat
There are also high steam channels to be connected to steam turbine for boiler, and there are also heated medium pipelines to be connected to outside for heat exchanger;Compression
The finisher that machine has refrigerant gas channel to be connected to evaporator has refrigerant gas channel to be connected to through regenerator with expanding machine again, swollen
There are also refrigerant gas channels to be communicated with compressor through low temperature heat exchanger and regenerator for swollen machine, and there are also low temperature Jie for low temperature heat exchanger
Matter pipeline is connected to outside;There are also refrigerant steam channels to be connected to absorber for evaporator, and there are also weak solution pipelines through molten for absorber
Liquid pump and solution heat exchanger are connected to the second absorber, and there are also weak solution pipelines through the second solution pump and second for the second absorber
Solution heat exchanger is connected to generator, and there are also concentrated solution pipelines through the second solution heat exchanger and the second generator company for generator
Logical, there are also concentrated solution pipelines to be connected to through solution heat exchanger with absorber for the second generator, and there are also refrigerant steam channels for generator
It is connected to condenser, there are also refrigerant steam channels to be connected to the second absorber for the second generator, and there are also cryogen liquid pipelines for condenser
It is connected to through throttle valve with evaporator, absorber, the second absorber and condenser also have heated medium pipeline and outside to connect respectively
It is logical;Compressor, boiler, air turbine, steam turbine, waste heat boiler, circulating pump and heat exchanger constitute air-steam forward direction and follow
Loop system;Compressor, evaporator, expanding machine, low temperature heat exchanger and regenerator constitute compression reverse circulation system, absorb
Device, the second absorber, generator, the second generator, condenser, evaporator, throttle valve, solution pump, the second solution pump, solution heat
Exchanger and the second solution heat exchanger constitute absorption reverse circulation system;Air-steam forward circulation is reverse to compression
Circulation provides power or externally provides power simultaneously, and air-steam forward circulation is negative to absorption reverse circulation offer driving heat
Lotus, compression reverse circulation obtains low temperature thermic load and by evaporator to absorption reverse circulation heat supply, absorption inversely to follow
Ring forms combined cycle energy supplying system by absorber, the second absorber and the external heat supply of condenser.
It is to increase by the second compression in the combined cycle energy supplying system described in the 11st 12. combined cycle energy supplying system
The finisher that compressor has refrigerant gas channel to be connected to evaporator is had refrigerant gas channel through regenerator and expansion by machine again
Machine connection is adjusted to the finisher that compressor has refrigerant gas channel to be connected to logical evaporator refrigerant gas channel and the again
The connection of two compressors, there are also the finishers that refrigerant gas channel is connected to evaporator refrigerant gas channel again for the second compressor
It is connected to through regenerator with expanding machine, forms combined cycle energy supplying system.
13. combined cycle energy supplying system, mainly by compressor, boiler, air turbine, steam turbine, waste heat boiler, circulation
Pump, compressor, expanding machine, cooler, low temperature heat exchanger, evaporator, absorber, the second absorber, occurs heat exchanger
Device, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger
It is formed;Compressor has air duct to be connected to outside, and boiler is again after compressor is connected to there are also compressed air channel with boiler
There is compressed air channel to be connected to air turbine, boiler there are also fuel and air channel with outside be connected to, boiler there are also combustion gas lead to
Road is connected to waste heat boiler, and there are also air ducts to be connected to waste heat boiler for air turbine, and there are also mixed-gas channels for waste heat boiler
The second generator has mixed-gas channel to be connected to outside again after being sequentially communicated generator and the second generator, and steam turbine has
Low-pressure steam channel is connected to heat exchanger, and there are also condensate liquid pipelines to be connected to through circulating pump with waste heat boiler for heat exchanger, waste heat
There are also high steam channels to be connected to steam turbine for boiler, and there are also heated medium pipelines to be connected to outside for heat exchanger;Compression
Machine has refrigerant gas channel to be connected to through cooler with expanding machine, and there are also refrigerant gas channels through low temperature heat exchanger and pressure for expanding machine
The connection of contracting machine, there are also cryogenic media pipelines be connected to external for low temperature heat exchanger, cooler there are also heated medium pipeline with outside
Portion's connection;Evaporator has refrigerant steam channel to be connected to absorber, and there are also weak solution pipelines through solution pump and solution heat for absorber
Exchanger is connected to the second absorber, and there are also weak solution pipelines through the second solution pump and the second solution heat exchanger for the second absorber
It is connected to generator, there are also concentrated solution pipelines to be connected to through the second solution heat exchanger with the second generator for generator, and second occurs
There are also concentrated solution pipelines to be connected to through solution heat exchanger with absorber for device, and there are also refrigerant steam channels and condenser to connect for generator
Logical, there are also refrigerant steam channels to be connected to the second absorber for the second generator, condenser there are also cryogen liquid pipelines through throttle valve and
Evaporator connection, there are also cryogenic media pipelines to be connected to external for evaporator, and absorber, the second absorber and condenser also have respectively
Heated medium pipeline is connected to outside;Compressor, boiler, air turbine, steam turbine, waste heat boiler, circulating pump and Re Jiao
Parallel operation constitutes air-steam forward circulation system, and it is inverse that compressor, cooler, expanding machine and low temperature heat exchanger constitute compression
To the circulatory system, absorber, the second absorber, generator, the second generator, condenser, evaporator, throttle valve, solution pump,
Two solution pumps, solution heat exchanger and the second solution heat exchanger constitute absorption reverse circulation system;Air-steam forward direction is followed
Circumferential compression reverse circulation provides power or externally provides power simultaneously, and air-steam forward circulation is inversely followed to absorption
Ring provides driving thermic load, and compression reverse circulation obtains low temperature thermic load and by the external heat supply of cooler, absorption reverse
Circulation obtains low temperature thermic load and by absorber, the second absorber and the external heat supply of condenser, forms combined cycle energy supply system
System.
It is to increase by the second compression in the combined cycle energy supplying system described in the 13rd 14. combined cycle energy supplying system
Compressor is had refrigerant gas channel to be connected to expanding machine through cooler and is adjusted to compressor and has refrigerant gas channel through cooling by machine
Device is connected to the second compressor, and there are also refrigerant gas channels to be connected to through cooler with expanding machine for the second compressor, and formation, which is combined, to follow
Ring energy supplying system.
15. combined cycle energy supplying system, mainly by compressor, boiler, air turbine, steam turbine, waste heat boiler, circulation
Pump, heat exchanger, compressor, cooler, expanding machine, low temperature heat exchanger, regenerator, evaporator, absorber, second absorb
Device, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat
Exchanger is formed;Compressor has air duct to be connected to outside, after compressor is connected to there are also compressed air channel with boiler
Boiler has compressed air channel to be connected to air turbine again, boiler there are also fuel and air channel with outside be connected to, boiler is also
Blast tube is connected to waste heat boiler, and there are also air ducts to be connected to waste heat boiler for air turbine, and there are also gaseous mixtures for waste heat boiler
The second generator has mixed-gas channel to be connected to outside again after body channel is sequentially communicated generator and the second generator, steam
Turbine has low-pressure steam channel to be connected to heat exchanger, and there are also condensate liquid pipelines through circulating pump and waste heat boiler company for heat exchanger
Logical, there are also high steam channels to be connected to steam turbine for waste heat boiler, and there are also heated medium pipelines to connect with outside for heat exchanger
It is logical;Compressor has refrigerant gas channel to be connected to through cooler and regenerator with expanding machine, and there are also refrigerant gas channel warps for expanding machine
Low temperature heat exchanger and regenerator are communicated with compressor, low temperature heat exchanger there are also cryogenic media pipeline with outside be connected to, cool down
Device there are also heated medium pipeline with outside be connected to;Evaporator has refrigerant steam channel to be connected to absorber, and there are also dilute for absorber
Solution line is connected to through solution pump and solution heat exchanger with the second absorber, and there are also weak solution pipelines through second for the second absorber
Solution pump and the second solution heat exchanger are connected to generator, generator there are also concentrated solution pipeline through the second solution heat exchanger with
The connection of second generator, there are also concentrated solution pipelines to be connected to through solution heat exchanger with absorber for the second generator, and generator is also
Refrigerant steam channel is connected to condenser, and there are also refrigerant steam channels to be connected to the second absorber for the second generator, and condenser is also
There is cryogen liquid pipeline to be connected to through throttle valve with evaporator, evaporator there are also cryogenic media pipeline with outside be connected to, absorber, second
Absorber and condenser also have heated medium pipeline to be connected to outside respectively;Compressor, boiler, air turbine, steam turbine,
Waste heat boiler, circulating pump and heat exchanger constitute air-steam forward circulation system, compressor, cooler, expanding machine, low temperature
Heat exchanger and regenerator constitute compression reverse circulation system, absorber, the second absorber, generator, the second generator, cold
Condenser, evaporator, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger constitute absorption
Reverse circulation system;Air-steam forward circulation provides power to compression reverse circulation or externally provides power simultaneously, empty
Gas-steam forward circulation provides driving thermic load to absorption reverse circulation, and compression reverse circulation obtains low temperature thermic load simultaneously
By the external heat supply of cooler, absorption reverse circulation obtains low temperature thermic load and passes through absorber, the second absorber and condensation
The external heat supply of device forms combined cycle energy supplying system.
It is to increase by the second compression in the combined cycle energy supplying system described in the 15th 16. combined cycle energy supplying system
Compressor is had refrigerant gas channel to be connected to expanding machine through cooler and regenerator and is adjusted to compressor and has refrigerant gas to lead to by machine
Road is connected to through cooler with the second compressor, and the second compressor has refrigerant gas channel through cooler and regenerator and expanding machine again
Connection forms combined cycle energy supplying system.
17. combined cycle energy supplying system, mainly by compressor, boiler, air turbine, steam turbine, waste heat boiler, circulation
Pump, compressor, cooler, expanding machine, low temperature heat exchanger, evaporator, absorber, the second absorber, occurs heat exchanger
Device, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger
It is formed;Compressor has air duct to be connected to outside, and boiler is again after compressor is connected to there are also compressed air channel with boiler
There is compressed air channel to be connected to air turbine, boiler there are also fuel and air channel with outside be connected to, boiler there are also combustion gas lead to
Road is connected to waste heat boiler, and there are also air ducts to be connected to waste heat boiler for air turbine, and there are also mixed-gas channels for waste heat boiler
The second generator has mixed-gas channel to be connected to outside again after being sequentially communicated generator and the second generator, and steam turbine has
Low-pressure steam channel is connected to heat exchanger, and there are also condensate liquid pipelines to be connected to through circulating pump with waste heat boiler for heat exchanger, waste heat
There are also high steam channels to be connected to steam turbine for boiler, and there are also heated medium pipelines to be connected to outside for heat exchanger;Compression
The finisher that machine has refrigerant gas channel to be connected to through cooler with evaporator has refrigerant gas channel to be connected to expanding machine again, swollen
There are also refrigerant gas channels to be communicated with compressor through low temperature heat exchanger for swollen machine, low temperature heat exchanger there are also cryogenic media pipeline with
Outside connection, there are also heated medium pipelines to be connected to external for cooler;There are also refrigerant steam channels and absorber to connect for evaporator
Logical, there are also weak solution pipelines to be connected to through solution pump and solution heat exchanger with the second absorber for absorber, and the second absorber is also
Weak solution pipeline is connected to through the second solution pump and the second solution heat exchanger with generator, and there are also concentrated solution pipelines through for generator
Two solution heat exchangers are connected to the second generator, and there are also concentrated solution pipelines through solution heat exchanger and absorber for the second generator
Connection, there are also refrigerant steam channels be connected to condenser for generator, and there are also refrigerant steam channels and the second absorption for the second generator
Device connection, there are also cryogen liquid pipelines to be connected to through throttle valve with evaporator for condenser, and absorber, the second absorber and condenser also divide
There is not heated medium pipeline to be connected to outside;Compressor, boiler, air turbine, steam turbine, waste heat boiler, circulating pump and
Heat exchanger constitutes air-steam forward circulation system, compressor, cooler, evaporator, expanding machine and low temperature heat exchanger structure
At compression reverse circulation system, absorber, the second absorber, generator, the second generator, condenser, evaporator, throttling
Valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger constitute absorption reverse circulation system;It is empty
Gas-steam forward circulation to compression reverse circulation provide power or simultaneously externally provide power, air-steam forward circulation to
Absorption reverse circulation provides driving thermic load, and compression reverse circulation acquisition low temperature thermic load is simultaneously external by cooler respectively
Heat supply and by evaporator to absorption reverse circulation heat supply, absorption reverse circulation passes through absorber, the second absorber and cold
The external heat supply of condenser forms combined cycle energy supplying system.
It is to increase by the second compression in the combined cycle energy supplying system described in the 17th 18. combined cycle energy supplying system
The finisher that compressor has refrigerant gas channel to be connected to through cooler with evaporator is had refrigerant gas channel and expansion by machine again
Machine connection is adjusted to the finisher that compressor has refrigerant gas channel to be connected to through cooler with evaporator has refrigerant gas logical again
Road is connected to the second compressor, and the finisher that the second compressor is connected to there are also refrigerant gas channel with evaporator through cooler is again
There is refrigerant gas channel to be connected to expanding machine, forms combined cycle energy supplying system.
19. combined cycle energy supplying system, mainly by compressor, boiler, air turbine, steam turbine, waste heat boiler, circulation
Pump, heat exchanger, compressor, cooler, regenerator, expanding machine, low temperature heat exchanger, evaporator, absorber, second absorb
Device, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat
Exchanger is formed;Compressor has air duct to be connected to outside, after compressor is connected to there are also compressed air channel with boiler
Boiler has compressed air channel to be connected to air turbine again, boiler there are also fuel and air channel with outside be connected to, boiler is also
Blast tube is connected to waste heat boiler, and there are also air ducts to be connected to waste heat boiler for air turbine, and there are also gaseous mixtures for waste heat boiler
The second generator has mixed-gas channel to be connected to outside again after body channel is sequentially communicated generator and the second generator, steam
Turbine has low-pressure steam channel to be connected to heat exchanger, and there are also condensate liquid pipelines through circulating pump and waste heat boiler company for heat exchanger
Logical, there are also high steam channels to be connected to steam turbine for waste heat boiler, and there are also heated medium pipelines to connect with outside for heat exchanger
It is logical;The finisher that compressor has refrigerant gas channel to be connected to through cooler with evaporator has refrigerant gas channel through regenerator again
It is connected to expanding machine, there are also refrigerant gas channels to be communicated with compressor through low temperature heat exchanger and regenerator for expanding machine, Low Temperature Thermal
There are also cryogenic media pipelines be connected to outside for exchanger, and there are also heated medium pipelines to be connected to external for cooler;Evaporator is also
There is refrigerant steam channel to be connected to absorber, there are also weak solution pipelines through solution pump and solution heat exchanger and the second suction for absorber
Device connection is received, there are also weak solution pipelines to be connected to through the second solution pump and the second solution heat exchanger with generator for the second absorber,
There are also concentrated solution pipelines to be connected to through the second solution heat exchanger with the second generator for generator, and there are also concentrated solution pipes for the second generator
Road is connected to through solution heat exchanger with absorber, and there are also refrigerant steam channels to be connected to condenser for generator, and the second generator is also
There is refrigerant steam channel to be connected to the second absorber, there are also cryogen liquid pipelines to be connected to through throttle valve with evaporator for condenser, absorbs
Device, the second absorber and condenser also have heated medium pipeline to be connected to outside respectively;Compressor, boiler, air turbine, steaming
Steam turbine, waste heat boiler, circulating pump and heat exchanger constitute air-steam forward circulation system, compressor, cooler, evaporation
Device, regenerator, expanding machine and low temperature heat exchanger constitute compression reverse circulation system, and absorber, occurs the second absorber
Device, the second generator, condenser, evaporator, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat
Exchanger constitutes absorption reverse circulation system;Air-steam forward circulation is to compression reverse circulation offer power or simultaneously
Power is externally provided, air-steam forward circulation provides driving thermic load to absorption reverse circulation, and compression reverse circulation obtains
Take low temperature thermic load and respectively by the external heat supply of cooler and by evaporator to absorption reverse circulation heat supply, it is absorption inverse
To absorber, the second absorber and the external heat supply of condenser is cycled through, combined cycle energy supplying system is formed.
It is to increase by the second compression in the combined cycle energy supplying system described in the 19th 20. combined cycle energy supplying system
The finisher that compressor has refrigerant gas channel to be connected to through cooler with evaporator is had refrigerant gas channel through backheat by machine again
Device be connected to expanding machine be adjusted to the finisher that compressor has refrigerant gas channel to be connected to through cooler with evaporator have again it is cold
Agent gas passage is connected to the second compressor, after the second compressor is connected to through cooler with evaporator there are also refrigerant gas channel
Evaporator has refrigerant gas channel to be connected to through regenerator with expanding machine again, forms combined cycle energy supplying system.
It is to increase third in any combined cycle energy supplying system described in 1-20 21. combined cycle energy supplying system
Generator, second throttle, third solution pump and third solution heat exchanger, the second absorber add weak solution pipeline through third
Solution pump and third solution heat exchanger are connected to third generator, and there are also concentrated solution pipelines through third solution heat for third generator
Exchanger is connected to the second generator, is had refrigerant steam channel to be connected to condenser in generator and is adjusted to generator and has cryogen steaming
Third generator has cryogen liquid pipeline to be connected to through second throttle with condenser again after vapour channel is connected to third generator, the
There are also refrigerant steam channels to be connected to condenser for three generators, forms combined cycle energy supplying system.
It is to increase third in any combined cycle energy supplying system described in 1-20 22. combined cycle energy supplying system
Second absorber is had weak solution pipeline through the second solution pump and by generator, second throttle and third solution heat exchanger
Two solution heat exchangers be connected to generator be adjusted to the second absorber have weak solution pipeline through the second solution pump, the second solution heat
Exchanger and third solution heat exchanger are connected to generator, by generator have concentrated solution pipeline through the second solution heat exchanger with
The connection of second generator, which is adjusted to generator, has concentrated solution pipeline to be connected to through third solution heat exchanger with third generator, third
Generator has concentrated solution pipeline to be connected to through the second solution heat exchanger with the second generator again, and generator is had refrigerant steam channel
Third generator after being adjusted to generator and having refrigerant steam channel to be connected to third generator is connected to condenser cryogen again
Liquid pipeline is connected to through second throttle with condenser, and there are also refrigerant steam channels to be connected to condenser for third generator, forms connection
Close circulation energy supplying system.
It is to increase third in any combined cycle energy supplying system described in 1-20 23. combined cycle energy supplying system
Second absorber is had weak solution pipeline through second by generator, second throttle, third solution pump and third solution heat exchanger
Solution pump and the second solution heat exchanger are connected to generator to be adjusted to the second absorber and has weak solution pipeline through the second solution pump
It is connected to the second solution heat exchanger with third generator, third generator has concentrated solution pipeline through third solution pump and third again
Solution heat exchanger is connected to generator, has concentrated solution pipeline to connect through the second solution heat exchanger and the second generator in generator
The logical generator that is adjusted to has concentrated solution pipeline to connect through third solution heat exchanger and the second solution heat exchanger and the second generator
It is logical, there is refrigerant steam channel be connected to condenser in generator and is adjusted to generator and has refrigerant steam channel and third generator company
Third generator has cryogen liquid pipeline to be connected to through second throttle with condenser again after logical, and there are also refrigerant vapours for third generator
Channel is connected to condenser, forms combined cycle energy supplying system.
It is to increase third in any combined cycle energy supplying system described in 1-20 24. combined cycle energy supplying system
Generator is had mixed-gas channel and the second hair by generator, second throttle, third solution pump and third solution heat exchanger
After raw device connection the second generator have again mixed-gas channel with it is external be connected to be adjusted to generator have mixed-gas channel according to
The second generator has mixed-gas channel to be connected to outside again after secondary connection third generator and the second generator, and second absorbs
Device is added weak solution pipeline and is connected to through third solution pump and third solution heat exchanger with third generator, and third generator is also
Concentrated solution pipeline is connected to through third solution heat exchanger with the second generator, has refrigerant steam channel and condenser to connect in generator
It is logical be adjusted to generator and there is refrigerant steam channel to be connected to third generator after third generator have cryogen liquid pipeline through the again
Two throttle valves are connected to condenser, and there are also refrigerant steam channels to be connected to condenser for third generator, form combined cycle energy supply
System.
It is to increase third in any combined cycle energy supplying system described in 1-20 25. combined cycle energy supplying system
Generator is had mixed-gas channel to be connected to it with the second generator by generator, second throttle and third solution heat exchanger
The second generator has mixed-gas channel to be connected to outside again and is adjusted to generator and has mixed-gas channel to be sequentially communicated third afterwards
The second generator has mixed-gas channel to be connected to outside again after generator and the second generator, the second absorber is had dilute molten
Liquid pipeline, which is connected to through the second solution pump and the second solution heat exchanger with generator, to be adjusted to the second absorber and has weak solution pipeline
It is connected to through the second solution pump, the second solution heat exchanger and third solution heat exchanger with generator, generator is had into concentrated solution
Pipeline be connected to through the second solution heat exchanger with the second generator be adjusted to generator have concentrated solution pipeline through third solution heat hand over
Parallel operation is connected to third generator, and third generator has concentrated solution pipeline to connect through the second solution heat exchanger and the second generator again
It is logical, there is refrigerant steam channel be connected to condenser in generator and is adjusted to generator and has refrigerant steam channel and third generator company
Third generator has cryogen liquid pipeline to be connected to through second throttle with condenser again after logical, and there are also refrigerant vapours for third generator
Channel is connected to condenser, forms combined cycle energy supplying system.
It is to increase third in any combined cycle energy supplying system described in 1-20 26. combined cycle energy supplying system
Generator is had mixed-gas channel and the second hair by generator, second throttle, third solution pump and third solution heat exchanger
After raw device connection the second generator have again mixed-gas channel with it is external be connected to be adjusted to generator have mixed-gas channel according to
The second generator has mixed-gas channel to be connected to outside again after secondary connection third generator and the second generator, and second is inhaled
It receives device and there is weak solution pipeline to be connected to through the second solution pump and the second solution heat exchanger with generator and be adjusted to the second absorber and have
Weak solution pipeline is connected to through the second solution pump and the second solution heat exchanger with third generator, and third generator has concentrated solution again
Pipeline is connected to through third solution pump and third solution heat exchanger with generator, has concentrated solution pipeline through the second solution in generator
Heat exchanger is connected to the second generator to be adjusted to generator and has concentrated solution pipeline through third solution heat exchanger and the second solution
Heat exchanger is connected to the second generator, is had refrigerant steam channel to be connected to condenser in generator and is adjusted to generator and has cryogen
Third generator has cryogen liquid pipeline to be connected to through second throttle with condenser again after steam channel is connected to third generator,
There are also refrigerant steam channels to be connected to condenser for third generator, forms combined cycle energy supplying system.
It is to increase by the 4th hair in any combined cycle energy supplying system described in the 21st 27. combined cycle energy supplying system
Raw device, third throttle valve, the 4th solution pump and the 4th solution heat exchanger, it is molten through the 4th that the second absorber adds weak solution pipeline
Liquid pump and the 4th solution heat exchanger are connected to the 4th generator, and there are also concentrated solution pipelines to hand over through the 4th solution heat for the 4th generator
Parallel operation is connected to the second generator, is had refrigerant steam channel to be connected to condenser in third generator and is adjusted to third generator and has
The 4th generator has cryogen liquid pipeline through third throttle valve and condenser again after refrigerant steam channel is connected to the 4th generator
Connection, there are also refrigerant steam channels to be connected to condenser for the 4th generator, formation combined cycle energy supplying system.
It is to increase by the 4th hair in any combined cycle energy supplying system described in the 22nd 28. combined cycle energy supplying system
Second absorber is had weak solution pipeline through the second solution pump, second molten by raw device, third throttle valve and the 4th solution heat exchanger
Liquid heat exchanger and third solution heat exchanger are connected to generator to be adjusted to the second absorber and has weak solution pipeline molten through second
Liquid pump, the second solution heat exchanger, the 4th solution heat exchanger and third solution heat exchanger are connected to generator, and third is sent out
Raw device has concentrated solution pipeline to be connected to through the second solution heat exchanger with the second generator to be adjusted to third generator and have concentrated solution pipe
Tetra- solution heat exchanger of Lu Jing is connected to the 4th generator, and the 4th generator has concentrated solution pipeline through the second solution heat exchange again
Device is connected to the second generator, by third generator have refrigerant steam channel be connected to condenser be adjusted to third generator have it is cold
The 4th generator has cryogen liquid pipeline to connect through third throttle valve and condenser again after agent steam channel is connected to the 4th generator
Logical, there are also refrigerant steam channels to be connected to condenser for the 4th generator, formation combined cycle energy supplying system.
It is to increase by the 4th hair in any combined cycle energy supplying system described in the 23rd 29. combined cycle energy supplying system
Raw device, third throttle valve, the 4th solution pump and the 4th solution heat exchanger, have weak solution pipeline molten through second second absorber
Liquid pump and the second solution heat exchanger are connected to third generator to be adjusted to the second absorber and has weak solution pipeline through the second solution
Pump and the second solution heat exchanger are connected to the 4th generator, and the 4th generator has concentrated solution pipeline through the 4th solution pump and the again
Four solution heat exchangers are connected to third generator, have concentrated solution pipeline molten through third solution heat exchanger and second in generator
Liquid heat exchanger is connected to the second generator to be adjusted to generator and has concentrated solution pipeline through third solution heat exchanger, the 4th solution
Heat exchanger and the second solution heat exchanger are connected to the second generator, and third generator is had refrigerant steam channel and condenser
The 4th generator has cryogen liquid pipe again after connection is adjusted to third generator and has refrigerant steam channel to be connected to the 4th generator
Road is connected to through third throttle valve with condenser, and there are also refrigerant steam channels to be connected to condenser for the 4th generator, and formation, which is combined, to follow
Ring energy supplying system.
It is to increase by the 4th hair in any combined cycle energy supplying system described in the 21st 30. combined cycle energy supplying system
Generator is had mixed-gas channel and second to occur by raw device, third throttle valve, the 4th solution pump and the 4th solution heat exchanger
The second generator has mixed-gas channel to be adjusted to generator with external be connected to and have mixed-gas channel successively again after device connection
The second generator has mixed-gas channel and outside to connect again after connection third generator, the 4th generator and the second generator
Logical, the second absorber is added weak solution pipeline and is connected to through the 4th solution pump and the 4th solution heat exchanger with the 4th generator, the
There are also concentrated solution pipelines to be connected to through the 4th solution heat exchanger with the second generator for four generators, and third generator is had cryogen steaming
Vapour channel is connected to condenser be adjusted to third generator and there is refrigerant steam channel to be connected to the 4th generator after the 4th occur
Device has cryogen liquid pipeline to be connected to through third throttle valve with condenser again, and there are also refrigerant steam channels and condenser to connect for the 4th generator
It is logical, form combined cycle energy supplying system.
It is to increase by the 4th hair in any combined cycle energy supplying system described in the 22nd 31. combined cycle energy supplying system
Raw device, third throttle valve and the 4th solution heat exchanger, after thering is mixed-gas channel to be connected to the second generator in generator
Second generator have again mixed-gas channel with outside be connected to be adjusted to generator have mixed-gas channel be sequentially communicated third send out
The second generator has mixed-gas channel to be connected to outside again after raw device, the 4th generator and the second generator, and second is inhaled
Receiving device has weak solution pipeline to be connected to tune with generator through the second solution pump, the second solution heat exchanger and third solution heat exchanger
Whole is that the second absorber has weak solution pipeline through the second solution pump, the second solution heat exchanger, the 4th solution heat exchanger and
Three solution heat exchangers are connected to generator, have concentrated solution pipeline to send out through the second solution heat exchanger and second in third generator
Raw device connection, which is adjusted to third generator, has concentrated solution pipeline to be connected to through the 4th solution heat exchanger with the 4th generator, the 4th hair
Raw device has concentrated solution pipeline to be connected to through the second solution heat exchanger with the second generator again, has refrigerant vapour to lead in third generator
Road is connected to condenser be adjusted to third generator and there is refrigerant steam channel to be connected to the 4th generator after the 4th generator again
There is cryogen liquid pipeline to be connected to through third throttle valve with condenser, there are also refrigerant steam channels to be connected to condenser for the 4th generator,
Form combined cycle energy supplying system.
It is to increase by the 4th hair in any combined cycle energy supplying system described in the 23rd 32. combined cycle energy supplying system
Generator is had mixed-gas channel and second to occur by raw device, third throttle valve, the 4th solution pump and the 4th solution heat exchanger
The second generator has mixed-gas channel to be adjusted to generator with external be connected to and have mixed-gas channel successively again after device connection
The second generator has mixed-gas channel and outside to connect again after connection third generator, the 4th generator and the second generator
It is logical, there is weak solution pipeline to be connected to adjustment with third generator through the second solution pump and the second solution heat exchanger the second absorber
There is weak solution pipeline to be connected to through the second solution pump and the second solution heat exchanger with the 4th generator for the second absorber, the 4th hair
Raw device has concentrated solution pipeline to be connected to through the 4th solution pump and the 4th solution heat exchanger with third generator again, generator is had dense
Solution line be connected to through third solution heat exchanger and the second solution heat exchanger with the second generator be adjusted to generator have it is dense
Solution line connects through third solution heat exchanger, the 4th solution heat exchanger and the second solution heat exchanger and the second generator
It is logical, there is refrigerant steam channel to be connected to condenser in third generator and is adjusted to third generator and has refrigerant steam channel and the 4th
The 4th generator has cryogen liquid pipeline to be connected to through third throttle valve with condenser again after generator connection, and the 4th generator is also
Refrigerant steam channel is connected to condenser, forms combined cycle energy supplying system.
It is in any combined cycle energy supplying system described in 27-32, by third 33. combined cycle energy supplying system
Generator has cryogen liquid pipeline to be connected to through second throttle with condenser to be adjusted to third generator and have cryogen liquid pipeline through the 4th
Generator and second throttle are connected to condenser, form combined cycle energy supplying system.
It is to increase by second in any combined cycle energy supplying system described in 1-33 34. combined cycle energy supplying system
Heat exchanger, second heat exchanger has heated medium pipeline to be connected to outside, and following any technology is taken to arrange
It imposes to form combined cycle energy supplying system: 1. thering is mixed-gas channel to be connected to outside in the second generator and be adjusted to the second generation
Device has mixed-gas channel to be connected to through second heat exchanger with outside;2. thering is mixed-gas channel to connect with outside in the second generator
Logical second generator that is adjusted to has mixed-gas channel to be connected to through second heat exchanger and evaporator with outside;3. second is occurred
Device has mixed-gas channel to be connected to outside to be adjusted to the second generator and have mixed-gas channel through second heat exchanger, evaporator
It is connected to low temperature heat exchanger with outside.
It is to increase third in any combined cycle energy supplying system described in 1-20 35. combined cycle energy supplying system
Second generator is had mixed-gas channel and outer by generator, third solution pump, third solution heat exchanger and third absorber
Third generator has gaseous mixture again after portion's connection is adjusted to the second generator and has mixed-gas channel to be connected to third generator
Body channel is connected to outside, is had refrigerant steam channel to be connected to absorber evaporator and is adjusted to evaporator and has refrigerant steam channel
It is connected to third absorber, there are also weak solution pipelines through third solution pump and third solution heat exchanger and third for third absorber
Generator connection, there are also concentrated solution pipelines to be connected to through third solution heat exchanger with third absorber for third generator, and third is sent out
There are also refrigerant steam channels be connected to absorber for raw device, and there are also heated medium pipelines to be connected to external for third absorber, formation
Combined cycle energy supplying system.
It is to increase by the second heat in any combined cycle energy supplying system described in the 40th 36. combined cycle energy supplying system
Exchanger, second heat exchanger has heated medium pipeline to be connected to outside, and takes following any technical measures
To form combined cycle energy supplying system: 1. thering is mixed-gas channel to be connected to outside in third generator and be adjusted to third generator
There is mixed-gas channel to be connected to through second heat exchanger with outside;2. thering is mixed-gas channel to be connected to outside in third generator
Being adjusted to third generator has mixed-gas channel to be connected to through second heat exchanger and evaporator with outside;3. by third generator
Have mixed-gas channel with outside be connected to be adjusted to third generator have mixed-gas channel through second heat exchanger, evaporator and
Low temperature heat exchanger is connected to outside.
It is to increase high temperature in any combined cycle energy supplying system described in 1-20 37. combined cycle energy supplying system
Heat exchanger and second circulation pump, the after thering is mixed-gas channel to be sequentially communicated generator and the second generator waste heat boiler
Two generators have mixed-gas channel to be connected to outside to be adjusted to waste heat boiler and have mixed-gas channel and high-temperature heat exchanger again
High-temperature heat exchanger has mixed-gas channel to be connected to outside again after connection, and high-temperature heat exchanger, generator and second occur
Closed loop is constituted by second circulation pump and circulating thermal medium pipeline between device, forms combined cycle energy supplying system.
It is to increase by the second heat in any combined cycle energy supplying system described in the 42nd 38. combined cycle energy supplying system
Exchanger, second heat exchanger has heated medium pipeline to be connected to outside, and takes following any technical measures
To form combined cycle energy supplying system: 1. second circulation will be relied on to pump between high-temperature heat exchanger, generator and the second generator
Closed loop, which is constituted, with circulating thermal medium pipeline is adjusted to high-temperature heat exchanger, generator, the second generator and the second heat
Closed loop is constituted by second circulation pump and circulating thermal medium pipeline between exchanger;2. by high-temperature heat exchanger, hair
Closed loop, which is constituted, by second circulation pump and circulating thermal medium pipeline between raw device and the second generator is adjusted to high temperature
By second circulation pump and circulating thermal medium between heat exchanger, generator, the second generator, second heat exchanger and evaporator
Pipeline constitutes closed loop;3. will between high-temperature heat exchanger, generator and the second generator by second circulation pump and
Circulating thermal medium pipeline constitutes closed loop and is adjusted to high-temperature heat exchanger, generator, the second generator, the second heat exchange
Closed loop is constituted by second circulation pump and circulating thermal medium pipeline between device, evaporator and low temperature heat exchanger.
It is to increase high temperature in any combined cycle energy supplying system described in 1-20 39. combined cycle energy supplying system
Heat exchanger, second circulation pump, third generator, third solution pump, third solution heat exchanger and third absorber, by waste heat
After boiler has mixed-gas channel to be sequentially communicated generator and the second generator the second generator have again mixed-gas channel with
There is mixed high-temperature heat exchanger again after outside connection is adjusted to waste heat boiler and has mixed-gas channel to be connected to high-temperature heat exchanger
It closes gas passage to be connected to outside, be followed between high-temperature heat exchanger, generator, the second generator and third generator by second
Ring pump and circulating thermal medium pipeline constitute closed loop;There is refrigerant steam channel to be connected to absorber evaporator to be adjusted to
Evaporator has refrigerant steam channel to be connected to third absorber, and there are also weak solution pipelines through third solution pump and for third absorber
Three solution heat exchangers are connected to third generator, and there are also concentrated solution pipelines through third solution heat exchanger and for third generator
The connection of three absorbers, there are also refrigerant steam channels to be connected to absorber for third generator, and there are also heated mediums for third absorber
Pipeline is connected to outside, forms combined cycle energy supplying system.
It is to cancel boiler in any combined cycle energy supplying system described in 1-20 40. combined cycle energy supplying system
There is blast tube to be connected to waste heat boiler, cancelling air turbine has air duct to be connected to waste heat boiler, and cancelling waste heat boiler has
The second generator has mixed-gas channel to connect with outside again after mixed-gas channel is sequentially communicated generator and the second generator
It is logical;The second generator has combustion gas logical again after boiler has blast tube to be sequentially communicated waste heat boiler, generator and the second generator
Road is connected to outside, the second hair after air turbine has air duct to be sequentially communicated waste heat boiler, generator and the second generator
Raw device has air duct to be connected to outside again, forms combined cycle energy supplying system.
41. combined cycle energy supplying system, be in any combined cycle energy supplying system described in 1-39, by fuel and
Air duct is changed to high temperature heat source medium channel, and blast tube is changed to low-temperature heat source medium channel, mixed gas is led to
Road is changed to blending agent channel, forms combined cycle energy supplying system.
It is in any combined cycle energy supplying system described in the 40th, by fuel and sky 42. combined cycle energy supplying system
Gas channel is changed to high temperature heat source medium channel, and blast tube is changed to low-temperature heat source medium channel, forms combined cycle and supplies
It can system.
It is to increase work in any combined cycle energy supplying system described in 1-42 43. combined cycle energy supplying system
Machine, air-steam forward circulation provide power to working machine respectively, provide power to compression reverse circulation and to absorption inverse
Driving thermic load is provided to circulation, forms combined cycle energy supplying system.
Detailed description of the invention:
Fig. 1 be according to the present invention provided by combined cycle the 1st kind of principled thermal system figure of energy supplying system.
Fig. 2 be according to the present invention provided by combined cycle the 2nd kind of principled thermal system figure of energy supplying system.
Fig. 3 be according to the present invention provided by combined cycle the 3rd kind of principled thermal system figure of energy supplying system.
Fig. 4 be according to the present invention provided by combined cycle the 4th kind of principled thermal system figure of energy supplying system.
Fig. 5 be according to the present invention provided by combined cycle the 5th kind of principled thermal system figure of energy supplying system.
Fig. 6 be according to the present invention provided by combined cycle the 6th kind of principled thermal system figure of energy supplying system.
Fig. 7 be according to the present invention provided by combined cycle the 7th kind of principled thermal system figure of energy supplying system.
Fig. 8 be according to the present invention provided by combined cycle the 8th kind of principled thermal system figure of energy supplying system.
Fig. 9 be according to the present invention provided by combined cycle the 9th kind of principled thermal system figure of energy supplying system.
Figure 10 be according to the present invention provided by combined cycle the 10th kind of principled thermal system figure of energy supplying system.
Figure 11 be according to the present invention provided by combined cycle the 11st kind of principled thermal system figure of energy supplying system.
Figure 12 be according to the present invention provided by combined cycle the 12nd kind of principled thermal system figure of energy supplying system.
Figure 13 be according to the present invention provided by combined cycle the 13rd kind of principled thermal system figure of energy supplying system.
Figure 14 be according to the present invention provided by combined cycle the 14th kind of principled thermal system figure of energy supplying system.
Figure 15 be according to the present invention provided by combined cycle the 15th kind of principled thermal system figure of energy supplying system.
Figure 16 be according to the present invention provided by combined cycle the 16th kind of principled thermal system figure of energy supplying system.
Figure 17 be according to the present invention provided by combined cycle the 17th kind of principled thermal system figure of energy supplying system.
Figure 18 be according to the present invention provided by combined cycle the 18th kind of principled thermal system figure of energy supplying system.
Figure 19 be according to the present invention provided by combined cycle the 19th kind of principled thermal system figure of energy supplying system.
Figure 20 be according to the present invention provided by combined cycle the 20th kind of principled thermal system figure of energy supplying system.
Figure 21 be according to the present invention provided by combined cycle the 21st kind of principled thermal system figure of energy supplying system.
Figure 22 be according to the present invention provided by combined cycle the 22nd kind of principled thermal system figure of energy supplying system.
Figure 23 be according to the present invention provided by combined cycle the 23rd kind of principled thermal system figure of energy supplying system.
Figure 24 be according to the present invention provided by combined cycle the 24th kind of principled thermal system figure of energy supplying system.
Figure 25 be according to the present invention provided by combined cycle the 25th kind of principled thermal system figure of energy supplying system.
Figure 26 be according to the present invention provided by combined cycle the 26th kind of principled thermal system figure of energy supplying system.
Figure 27 be according to the present invention provided by combined cycle the 27th kind of principled thermal system figure of energy supplying system.
Figure 28 be according to the present invention provided by combined cycle the 28th kind of principled thermal system figure of energy supplying system.
Figure 29 be according to the present invention provided by combined cycle the 29th kind of principled thermal system figure of energy supplying system.
Figure 30 be according to the present invention provided by combined cycle the 30th kind of principled thermal system figure of energy supplying system.
Figure 31 be according to the present invention provided by combined cycle the 31st kind of principled thermal system figure of energy supplying system.
In figure, A- compressor, B- boiler, C- air turbine, D- steam turbine, E- waste heat boiler, F- circulating pump, the friendship of G- heat
Parallel operation, H- compressor, I- cryogenic throttle valve, J- low temperature heat exchanger, the second compressor of K-, the second condenser of L-, M- cooler,
The second cryogenic throttle valve of N-, O- expanding machine, P- regenerator, Q- high-temperature heat exchanger, R- second circulation pump, S- working machine;1- inhales
Receipts device, the second absorber of 2-, 3- generator, the second generator of 4-, 5- condenser, 6- evaporator, 7- throttle valve, 8- solution pump,
The second solution pump of 9-, 10- solution heat exchanger, the second solution heat exchanger of 11-, 12- second heat exchanger, 13- third occur
Device, 14- second throttle, 15- third solution pump, 16- third solution heat exchanger, 17- third generator, the throttling of 18- third
Valve, the 4th solution pump of 19-, the 4th solution heat exchanger of 20-, 21- third absorber.
Here following explanation is also provided:
(1) evaporator --- it is named from absorption reverse circulation angle, is evaporator in absorption reverse circulation, is pressing
Make condenser in contracting formula reverse circulation or cooler uses.
(2) throttle valve --- the throttle valve in compression reverse circulation is respectively designated as cryogenic throttle valve and the second low temperature
Throttle valve in absorption reverse circulation is respectively designated as throttle valve, second throttle and third throttle valve by throttle valve.
(3) compressor and compressor --- the compressor of the compressed air in air turbine device is referred to as to calm the anger
The compressor of compression work medium in reverse circulation is referred to as compressor by machine.
(4) working media --- claim the gaseous working medium in compressed steam circulation and Absorption heat-transformer to refrigerant vapour, liquid
Working medium claims cryogen liquid, by compressed gas recycle in working medium claim refrigerant gas;Liquid refrigerant in Steam Power Circulation is claimed cold
Lime set, such as condensate or other liquid mediums.
(5) condenser and cooler --- the heat exchanger based on working medium release latent heat claims condenser, and working medium discharges sensible heat
Based on heat exchanger claim cooler.
(6) boiler --- fuel chemical energy is changed by thermal energy by burning, heating device is carried out to working medium;Here it also wraps
Waste heat boiler is included, high temperature heat source medium flows through boiler and heats to working medium at this time, and the heat source medium after reduction temperature mentions
Supply reverse circulation system makees driving thermal medium, and blending agent is claimed when heat source medium mixes with air.
(7) process and structure of substantive content of the present invention it are not related to, not in express ranges of the present invention.
Specific embodiment:
First it is noted that in the statement of structure and process, do not repeat in inessential situation;To apparent
Process do not state.Carry out the present invention is described in detail with example with reference to the accompanying drawing.
Combined cycle energy supplying system shown in Fig. 1 is achieved in that
(1) in structure, it is mainly handed over by compressor, boiler, air turbine, steam turbine, waste heat boiler, circulating pump, heat
Parallel operation, compressor, cryogenic throttle valve, low temperature heat exchanger, evaporator, absorber, the second absorber, generator, second occur
Device, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and working machine institute group
At;Compressor A has air duct to be connected to outside, and boiler B is again after compressor A is connected to there are also compressed air channel with boiler B
There is compressed air channel to be connected to air turbine C, boiler B there are also fuel and air channel with outside be connected to, there are also combustion gas by boiler B
Channel is connected to waste heat boiler E, and there are also air ducts to be connected to waste heat boiler E by air turbine C, and there are also gaseous mixtures by waste heat boiler E
Second generator 4 has mixed-gas channel to be connected to outside again after body channel is sequentially communicated generator 3 and the second generator 4,
Steam turbine D has low-pressure steam channel to be connected to heat exchanger G, and there are also condensate liquid pipelines through circulating pump F and waste heat by heat exchanger G
Boiler E connection, there are also high steam channels to be connected to steam turbine D by waste heat boiler E, and there are also heated medium pipes by heat exchanger G
Road is connected to outside;The finisher 6 that compressor H has refrigerant steam channel to be connected to evaporator 6 has cryogen liquid pipeline through low again
Warm throttle valve I is connected to low temperature heat exchanger J, and there are also refrigerant steam channels to be connected to compressor H by low temperature heat exchanger J, low temperature
Heat exchanger J there are also cryogenic media pipeline with outside be connected to;Evaporator 6 is connected to there are also refrigerant steam channel with absorber 1, is absorbed
Device 1 is connected to through solution pump 8 and solution heat exchanger 10 with the second absorber 2 there are also weak solution pipeline, and there are also dilute for the second absorber 2
Solution line is connected to through the second solution pump 9 and the second solution heat exchanger 11 with generator 3, and there are also concentrated solution pipelines for generator 3
It is connected to through the second solution heat exchanger 11 with the second generator 4, there are also concentrated solution pipelines through solution heat exchanger for the second generator 4
10 are connected to absorber 1, and generator 3 is connected to there are also refrigerant steam channel with condenser 5, and there are also refrigerant vapours for the second generator 4
Channel is connected to the second absorber 2, and condenser 5 is connected to there are also cryogen liquid pipeline with evaporator 6 through throttle valve 7, absorber 1, the
Two absorbers 2 and condenser 5 also have heated medium pipeline to be connected to outside respectively;Compressor, boiler, air turbine, steam
Turbine, waste heat boiler, circulating pump, heat exchanger and operating mechanism at air-steam forward circulation system, compressor, evaporator,
Cryogenic throttle valve and low temperature heat exchanger constitute compression reverse circulation system, absorber, the second absorber, generator, second
Generator, condenser, evaporator, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger
Constitute absorption reverse circulation system.
(2) in process, compressor, boiler, air turbine, steam turbine, waste heat boiler, circulating pump and heat exchanger are carried out
Air-steam forward circulation --- fuel and air enter boiler B and burn, combustion gas in boiler B heat release in compressed air it
Enter waste heat boiler E afterwards, air flows through compressor A boosting heating, enters after compressed air flows through boiler B, heat absorption heats up empty
Gas-turbine C, compressed air flow through air turbine C decompression work done, and the air after work done enters waste heat boiler E, combustion gas and air
Condensate liquid is heated in waste heat boiler E to form mixed gas at high steam, combustion gas and air and be supplied to generator 3 and second
Generator 4 makees driving thermal medium, and the high steam that waste heat boiler E is generated enters steam turbine D decompression work done, steam turbine E row
Low-pressure steam out enters heat exchanger G, heat release in heated medium into condensate liquid, and condensate liquid mentions after circulating pump F pressurization
Supply waste heat boiler E, heat absorption is provided at high steam and to steam turbine D;Compressor, evaporator, cryogenic throttle valve and low temperature
Heat exchanger carries out compression reverse circulation --- and refrigerant vapour enters compressor H, flows through evaporator 6 after boosting heating and puts
For heat at cryogen liquid, cryogen liquid enters low temperature heat exchanger J, heat absorption at refrigerant vapour and to pressure after cryogenic throttle valve I throttling
Contracting machine H is provided;Absorber, the second absorber, generator, the second generator, condenser, evaporator, throttle valve, solution pump,
Two solution pumps, solution heat exchanger and the second solution heat exchanger carry out absorption reverse circulation --- the weak solution of absorber 1
Enter the second absorber 2 through solution pump 8 and solution heat exchanger 10, absorb refrigerant vapour and heat release is in heated medium, second
The weak solution of absorber 2 enters generator 3, heat absorption release refrigerant vapour through the second solution pump 9 and the second solution heat exchanger 11
And provided to condenser 5, the concentrated solution of generator 3 is cold into the second generator 4, heat absorption release through the second solution heat exchanger 11
Agent steam is simultaneously provided to the second absorber 2, and the concentrated solution of the second generator 4 enters absorber 1 through solution heat exchanger 10, absorbs
Simultaneously heat release is in heated medium for refrigerant vapour, and the refrigerant vapour heat release of condenser 5 is in heated medium at cryogen liquid, condenser 5
Cryogen liquid through throttle valve 7 throttling enter evaporator 6, heat absorption at refrigerant vapour and to absorber 1 provide;Air-steam is positive
Circulation provides power to working machine and compression reverse circulation respectively, and air-steam forward circulation is mentioned to absorption reverse circulation
For driving thermic load, compression reverse circulation obtains low temperature thermic load and by evaporator to absorption reverse circulation heat supply, inhales
Receipts formula reverse circulation forms combined cycle energy supplying system by absorber, the second absorber and the external heat supply of condenser.
Combined cycle energy supplying system shown in Fig. 2 is achieved in that
In combined cycle energy supplying system shown in Fig. 1, increase the second compressor, by compressor H have refrigerant steam channel with
The finisher 6 of 6 connection of evaporator has cryogen liquid pipeline to be connected to through cryogenic throttle valve I with low temperature heat exchanger J to be adjusted to press again
The finisher 6 that contracting machine H has refrigerant steam channel to be connected to evaporator 6 has refrigerant steam channel to be connected to the second compressor K again,
There are also the finishers 6 that refrigerant steam channel is connected to evaporator 6 to have cryogen liquid pipeline through cryogenic throttle valve again by second compressor K
I is connected to low temperature heat exchanger J;The refrigerant vapour that compressor H is generated enters the second compression after flowing through 6 heat release of evaporator cooling
Machine K, the refrigerant vapour that the second compressor K is generated are provided to evaporator 6, form combined cycle energy supplying system.
Combined cycle energy supplying system shown in Fig. 3 is achieved in that
(1) in structure, it is mainly handed over by compressor, boiler, air turbine, steam turbine, waste heat boiler, circulating pump, heat
Parallel operation, the second condenser, cryogenic throttle valve, low temperature heat exchanger, evaporator, absorber, the second absorber, occurs compressor
Device, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger
It is formed;Compressor A has air duct to be connected to outside, boiler after compressor A is connected to there are also compressed air channel with boiler B
B has compressed air channel to be connected to air turbine C again, boiler B there are also fuel and air channel with outside be connected to, boiler B is also
Blast tube is connected to waste heat boiler E, and there are also air ducts to be connected to waste heat boiler E by air turbine C, and there are also mixed by waste heat boiler E
Close the second generator 4 after gas passage is sequentially communicated generator 3 and the second generator 4 has mixed-gas channel to connect with outside again
Logical, steam turbine D has low-pressure steam channel to be connected to heat exchanger G, heat exchanger G there are also condensate liquid pipelines through circulating pump F and
Waste heat boiler E connection, there are also high steam channels to be connected to steam turbine D by waste heat boiler E, and heat exchanger G is also heated Jie
Matter pipeline is connected to outside;The second condenser L has cold again after compressor H has refrigerant steam channel to be connected to the second condenser L
Agent liquid pipeline is connected to through cryogenic throttle valve I with low temperature heat exchanger J, and there are also refrigerant steam channels and compression by low temperature heat exchanger J
Machine H connection, there are also cryogenic media pipelines to be connected to external by low temperature heat exchanger J, and there are also heated medium pipelines by the second condenser L
It is connected to outside;Evaporator 6 has refrigerant steam channel to be connected to absorber 1, and there are also weak solution pipelines through solution pump 8 for absorber 1
It is connected to solution heat exchanger 10 with the second absorber 2, there are also weak solution pipelines through the second solution pump 9 and for the second absorber 2
Two solution heat exchangers 11 are connected to generator 3, and there are also concentrated solution pipelines through the second solution heat exchanger 11 and second for generator 3
Generator 4 is connected to, and the second generator 4 is connected to through solution heat exchanger 10 with absorber 1 there are also concentrated solution pipeline, and generator 3 is also
There is refrigerant steam channel to be connected to condenser 5, the second generator 4 is connected to there are also refrigerant steam channel with the second absorber 2, is condensed
Device 5 is connected to through throttle valve 7 with evaporator 6 there are also cryogen liquid pipeline, and the also cryogenic media pipeline of evaporator 6 is connected to outside, is inhaled
Receive device 1, the second absorber 2 and condenser 5 also has heated medium pipeline to be connected to outside respectively;Compressor, boiler, Air wheel
Machine, steam turbine, waste heat boiler, circulating pump and heat exchanger constitute air-steam forward circulation system, compressor, second cold
Condenser, cryogenic throttle valve and low temperature heat exchanger constitute compression reverse circulation system, absorber, the second absorber, generator,
Second generator, condenser, evaporator, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat are handed over
Parallel operation constitutes absorption reverse circulation system.
(2) in process, compared with the combined cycle energy supplying system shown in Fig. 1, in addition to no working machine, the difference is that:
Compressor, the second condenser, cryogenic throttle valve and low temperature heat exchanger carry out compression reverse circulation --- and refrigerant vapour enters
Compressor H flows through the second condenser L and heat release in heated medium into cryogen liquid after boosting heating, cryogen liquid is through low temperature section
Valve I throttling is flowed to enter low temperature heat exchanger J later, absorb heat into refrigerant vapour and provide to compressor H;Evaporator 6 is directly from low
Warm medium obtains low temperature thermic load.
Combined cycle energy supplying system shown in Fig. 4 is achieved in that
In combined cycle energy supplying system shown in Fig. 3, increase the second compressor, by compressor H have refrigerant steam channel with
The second condenser L has cryogen liquid pipeline to be connected to through cryogenic throttle valve I with low temperature heat exchanger J again after second condenser L connection
After being adjusted to compressor H and thering is refrigerant steam channel to be connected to the second condenser L the second condenser L have again refrigerant steam channel with
Second compressor K connection, the second condenser L is again after the second compressor K is connected to there are also refrigerant steam channel with the second condenser L
There is cryogen liquid pipeline to be connected to through cryogenic throttle valve I with low temperature heat exchanger J;It is cold that the refrigerant vapour that compressor H is generated flows through second
Enter the second compressor K after condenser L heat release cooling, the refrigerant vapour that the second compressor K is generated is mentioned to the second condenser L again
For forming combined cycle energy supplying system.
Combined cycle energy supplying system shown in Fig. 5 is achieved in that
(1) in structure, it is mainly handed over by compressor, boiler, air turbine, steam turbine, waste heat boiler, circulating pump, heat
Parallel operation, compressor, cooler, cryogenic throttle valve, low temperature heat exchanger, evaporator, absorber, the second absorber, generator,
Two generators, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and work
Machine is formed;Compressor A has air duct to be connected to outside, pot after compressor A is connected to there are also compressed air channel with boiler B
Furnace B has compressed air channel to be connected to air turbine C again, boiler B there are also fuel and air channel with outside be connected to, boiler B is also
There is blast tube to be connected to waste heat boiler E, there are also air ducts to be connected to waste heat boiler E by air turbine C, and waste heat boiler E is also
Second generator 4 has mixed-gas channel and outside again after mixed-gas channel is sequentially communicated generator 3 and the second generator 4
Connection, steam turbine D have low-pressure steam channel to be connected to heat exchanger G, and there are also condensate liquid pipelines through circulating pump F by heat exchanger G
It is connected to waste heat boiler E, there are also high steam channels to be connected to steam turbine D by waste heat boiler E, and heat exchanger G is also heated
Medium pipeline is connected to outside;The aftercooler M that compressor H has refrigerant steam channel to be connected to cooler M has refrigerant vapour again
Channel is connected to evaporator 6, and evaporator 6 is connected to through cryogenic throttle valve I with low temperature heat exchanger J there are also cryogen liquid pipeline, low temperature
There are also refrigerant steam channels to be connected to compressor H by heat exchanger J, and there are also cryogenic media pipelines to connect with outside by low temperature heat exchanger J
Logical, there are also heated medium pipelines to be connected to external by cooler M;Evaporator 6 is connected to there are also refrigerant steam channel with absorber 1,
Absorber 1 is connected to through solution pump 8 and solution heat exchanger 10 with the second absorber 2 there are also weak solution pipeline, and the second absorber 2 is also
There is weak solution pipeline to be connected to through the second solution pump 9 and the second solution heat exchanger 11 with generator 3, there are also concentrated solutions for generator 3
Pipeline is connected to through the second solution heat exchanger 11 with the second generator 4, and the second generator 4 is handed over there are also concentrated solution pipeline through solution heat
Parallel operation 10 is connected to absorber 1, and generator 3 is connected to there are also refrigerant steam channel with condenser 5, and there are also cryogens for the second generator 4
Steam channel is connected to the second absorber 2, and condenser 5 is connected to through throttle valve 7 with evaporator 6 there are also cryogen liquid pipeline, absorber
1, the second absorber 2 and condenser 5 also have heated medium pipeline to be connected to outside respectively;Compressor, boiler, air turbine,
Steam turbine, waste heat boiler, circulating pump, heat exchanger and operating mechanism are compressor, cold at air-steam forward circulation system
But device, evaporator, cryogenic throttle valve and low temperature heat exchanger constitute compression reverse circulation system, absorber, the second absorber,
Generator, the second generator, condenser, evaporator, throttle valve, solution pump, the second solution pump, solution heat exchanger and second are molten
Liquid heat exchanger constitutes absorption reverse circulation system.
(2) in process, compared with the combined cycle energy supplying system shown in Fig. 1, the difference is that: compressor, cooler, steaming
Hair device, cryogenic throttle valve and low temperature heat exchanger carry out compression reverse circulation --- and refrigerant vapour enters compressor H, and boosting rises
Cooler M is flowed through after temperature and heat release cooling, the refrigerant vapour after cooling down flow through 6 heat release of evaporator into cryogen liquid, cryogen liquid
Enter low temperature heat exchanger J after cryogenic throttle valve I throttling, heat absorption is provided at refrigerant vapour and to compressor H.
Combined cycle energy supplying system shown in Fig. 6 is achieved in that
In combined cycle energy supplying system shown in Fig. 5, add the second compressor, by compressor H have refrigerant steam channel with it is cold
But the aftercooler M of device M connection has refrigerant steam channel to be connected to evaporator 6 again and is adjusted to compressor H and has refrigerant steam channel
The aftercooler M being connected to cooler M has refrigerant steam channel to be connected to the second compressor K again, and there are also cryogens by the second compressor K
The aftercooler M that steam channel is connected to cooler M has refrigerant steam channel to be connected to evaporator 6 again;Compressor H is generated cold
Agent steam is supplied to the second compressor K after flowing through cooler M heat release cooling, and the refrigerant vapour that the second compressor K is generated flows through
It is supplied to evaporator 6 after cooler M heat release cooling, forms combined cycle energy supplying system.
Combined cycle energy supplying system shown in Fig. 7 is achieved in that
(1) in structure, it is mainly handed over by compressor, boiler, air turbine, steam turbine, waste heat boiler, circulating pump, heat
Parallel operation, compressor, the second compressor, the second condenser, cryogenic throttle valve, the second cryogenic throttle valve, low temperature heat exchanger, evaporation
Device, absorber, the second absorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat
Exchanger and the second solution heat exchanger are formed;Compressor A has air duct to be connected to outside, and compressor A also compresses sky
Boiler B has compressed air channel to be connected to air turbine C again after gas channel is connected to boiler B, and there are also fuel and air by boiler B
Channel is connected to outside, and there are also blast tubes to be connected to waste heat boiler E by boiler B, and there are also air ducts and waste heat pot by air turbine C
Furnace E connection, there are also mixed-gas channels to be sequentially communicated generator 3 and the second generator 4 second generator 4 later by waste heat boiler E
There is mixed-gas channel to be connected to outside again, steam turbine D has low-pressure steam channel to be connected to heat exchanger G, and heat exchanger G is also
There is condensate liquid pipeline to be connected to through circulating pump F with waste heat boiler E, there are also high steam channels and steam turbine D to connect by waste heat boiler E
Logical, there are also heated medium pipelines to be connected to external by heat exchanger G;Compressor H has low pressure refrigerant steam channel and evaporator 6 to connect
It is logical, low temperature heat exchanger J after evaporator 6 is connected to through cryogenic throttle valve I with low temperature heat exchanger J there are also low pressure cryogen liquid pipeline
There is refrigerant steam channel to be connected to compressor H again, there are also low pressure refrigerant steam channels to be connected to the second compressor K by compressor H, and
There are also high pressure refrigerant steam channels to be connected to the second condenser L by two compressor K, and there are also high pressure cryogen liquid pipelines by the second condenser L
Low temperature heat exchanger J has refrigerant vapour logical again after being connected to through evaporator 6 and the second cryogenic throttle valve N with low temperature heat exchanger J
Road is connected to compressor H, low temperature heat exchanger J there are also cryogenic media pipeline with outside be connected to, the second condenser L is also heated
Medium pipeline is connected to outside;Evaporator 6 is connected to there are also refrigerant steam channel with absorber 1, and there are also weak solution pipelines for absorber 1
It is connected to through solution pump 8 and solution heat exchanger 10 with the second absorber 2, there are also weak solution pipeline is molten through second for the second absorber 2
Liquid pump 9 and the second solution heat exchanger 11 are connected to generator 3, and there are also concentrated solution pipelines through the second solution heat exchange for generator 3
Device 11 is connected to the second generator 4, and the second generator 4 is connected to through solution heat exchanger 10 with absorber 1 there are also concentrated solution pipeline,
Generator 3 is connected to there are also refrigerant steam channel with condenser 5, and there are also refrigerant steam channel and the second absorbers 2 for the second generator 4
Connection, condenser 5 are connected to through throttle valve 7 with evaporator 6 there are also cryogen liquid pipeline, absorber 1, the second absorber 2 and condenser 5
Also there is heated medium pipeline to be connected to outside respectively;Compressor, boiler, air turbine, steam turbine, waste heat boiler, circulation
Pump and heat exchanger constitute air-steam forward circulation system, compressor, the second compressor, the second condenser, evaporator, low
Warm throttle valve, the second cryogenic throttle valve and low temperature heat exchanger constitute compression reverse circulation system;Absorber, second absorb
Device, generator, the second generator, condenser, evaporator, throttle valve, solution pump, the second solution pump, solution heat exchanger and
Two solution heat exchangers constitute absorption reverse circulation system.
(2) in process, compressor, boiler, air turbine, steam turbine, waste heat boiler, circulating pump and heat exchanger are carried out
Air-steam forward circulation --- fuel and air enter boiler B and burn, combustion gas in boiler B heat release in compressed air it
Enter waste heat boiler E afterwards, air flows through compressor A boosting heating, enters after compressed air flows through boiler B, heat absorption heats up empty
Gas-turbine C, compressed air flow through air turbine C decompression work done, and the air after work done enters waste heat boiler E, combustion gas and air
Condensate liquid is heated in waste heat boiler E is supplied to generator 3 and second at the mixed gas that high steam, combustion gas and air are formed
Generator 4 makees driving thermal medium, and the high steam that waste heat boiler E is generated enters steam turbine D decompression work done, steam turbine E row
Low-pressure steam out enters heat exchanger G, heat release in heated medium into condensate liquid, and condensate liquid mentions after circulating pump F pressurization
Supply waste heat boiler E, heat absorption is provided at high steam and to steam turbine D;Compressor, the second condenser, steams the second compressor
Send out device, cryogenic throttle valve, the second cryogenic throttle valve and low temperature heat exchanger carry out compression reverse circulation --- refrigerant vapour into
Enter compressor H, the rear portion through being compressed into low pressure refrigerant vapour is supplied to the second compressor K, and another part flows through evaporator 6
And heat release, at low pressure cryogen liquid, low pressure cryogen liquid enters low temperature heat exchanger J, heat absorption through cryogenic throttle valve I throttling and steams at cryogen
Vapour is simultaneously provided to compressor H, and the high pressure refrigerant vapour that the second compressor K is generated flows through the second condenser L and heat release is in being heated
At high pressure cryogen liquid, high pressure cryogen liquid stream cools down through evaporator 6 and enters Low Temperature Thermal through the second cryogenic throttle valve N throttling to be handed over medium
Parallel operation J, heat absorption are provided at refrigerant vapour and to compressor H;Absorber, the second absorber, generator, the second generator, condensation
Device, evaporator, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger carry out absorption inverse
To circulation --- the weak solution of absorber 1 enters the second absorber 2 through solution pump 8 and solution heat exchanger 10, absorbs cryogen steaming
Simultaneously heat release enters in heated medium, the weak solution of the second absorber 2 through the second solution pump 9 and the second solution heat exchanger 11 vapour
Generator 3, heat absorption release refrigerant vapour are simultaneously provided to condenser 5, the concentrated solution of generator 3 through the second solution heat exchanger 11 into
Enter the second generator 4, heat absorption release refrigerant vapour and provided to the second absorber 2, the concentrated solution of the second generator 4 is through solution heat
Exchanger 10 enters absorber 1, absorbs refrigerant vapour and heat release in heated medium, and the refrigerant vapour heat release of condenser 5 is in quilt
For heat medium at cryogen liquid, the cryogen liquid of condenser 5 enters evaporator 6, heat absorption at refrigerant vapour and to suction through the throttling of throttle valve 7
Device 1 is received to provide;Air-steam forward circulation provides power to compression reverse circulation respectively and provides to absorption reverse circulation
Thermic load is driven, compression reverse circulation obtains low temperature thermic load and passes through the external heat supply of the second condenser respectively and pass through evaporation
Device passes through absorber, the second absorber and the external heat supply of condenser, shape to absorption reverse circulation heat supply, absorption reverse circulation
At combined cycle energy supplying system.
Combined cycle energy supplying system shown in Fig. 8 is achieved in that
(1) in structure, it is mainly handed over by compressor, boiler, air turbine, steam turbine, waste heat boiler, circulating pump, heat
Parallel operation, compressor, the second condenser, cryogenic throttle valve, the second cryogenic throttle valve, low temperature heat exchanger, evaporator, absorber,
Second absorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and
Two solution heat exchangers are formed;Compressor A has air duct to be connected to outside, and there are also compressed air channels and pot by compressor A
Boiler B has compressed air channel to be connected to air turbine C again after furnace B connection, and there are also fuel and air channels and outside by boiler B
Connection, there are also blast tubes to be connected to waste heat boiler E by boiler B, and there are also air ducts to be connected to waste heat boiler E by air turbine C, remaining
The second generator 4 has gaseous mixture again after heat boiler E is sequentially communicated generator 3 and the second generator 4 there are also mixed-gas channel
Body channel is connected to outside, and steam turbine D has low-pressure steam channel to be connected to heat exchanger G, and there are also condensate lines by heat exchanger G
Road is connected to through circulating pump F with waste heat boiler E, and there are also high steam channels to be connected to steam turbine D by waste heat boiler E, heat exchanger G
There are also heated medium pipelines to be connected to outside;Compressor H has low pressure refrigerant steam channel to be connected to evaporator 6, and evaporator 6 is also
Low temperature heat exchanger J has refrigerant vapour again after having low pressure cryogen liquid pipeline to be connected to through cryogenic throttle valve I with low temperature heat exchanger J
Channel is connected to compressor H, and there are also high pressure refrigerant steam channels to be connected to the second condenser L by compressor H, and the second condenser L is also
Low temperature heat exchanger after thering is high pressure cryogen liquid pipeline to be connected to through evaporator 6 and the second cryogenic throttle valve N with low temperature heat exchanger J
J has refrigerant steam channel to be connected to compressor H again, low temperature heat exchanger J there are also cryogenic media pipeline with outside be connected to, second is cold
Condenser L there are also heated medium pipeline with outside be connected to;Evaporator 6 is connected to there are also refrigerant steam channel with absorber 1, absorber
1 is connected to through solution pump 8 and solution heat exchanger 10 with the second absorber 2 there are also weak solution pipeline, and there are also dilute molten for the second absorber 2
Liquid pipeline is connected to through the second solution pump 9 and the second solution heat exchanger 11 with generator 3, and there are also concentrated solution pipelines to pass through for generator 3
Second solution heat exchanger 11 is connected to the second generator 4, and there are also concentrated solution pipelines through solution heat exchanger 10 for the second generator 4
It is connected to absorber 1, generator 3 is connected to there are also refrigerant steam channel with condenser 5, and there are also refrigerant vapours to lead to for the second generator 4
Road is connected to the second absorber 2, and condenser 5 is connected to through throttle valve 7 with evaporator 6 there are also cryogen liquid pipeline, absorber 1, second
Absorber 2 and condenser 5 also have heated medium pipeline to be connected to outside respectively;Compressor, boiler, air turbine, vapor wheel
Machine, waste heat boiler, circulating pump and heat exchanger constitute air-steam forward circulation system, compressor, the second condenser, evaporation
Device, cryogenic throttle valve, the second cryogenic throttle valve and low temperature heat exchanger constitute compression reverse circulation system, absorber, second
Absorber, generator, the second generator, condenser, evaporator, throttle valve, solution pump, the second solution pump, solution heat exchanger
Absorption reverse circulation system is constituted with the second solution heat exchanger.
(2) in process, compressor, boiler, air turbine, steam turbine, waste heat boiler, circulating pump and heat exchanger are carried out
Air-steam forward circulation --- fuel and air enter boiler B and burn, combustion gas in boiler B heat release in compressed air it
Enter waste heat boiler E afterwards, air flows through compressor A boosting heating, enters after compressed air flows through boiler B, heat absorption heats up empty
Gas-turbine C, compressed air flow through air turbine C decompression work done, and the air after work done enters waste heat boiler E, combustion gas and air
Condensate liquid is heated in waste heat boiler E is supplied to generator 3 and second at the mixed gas that high steam, combustion gas and air are formed
Generator 4 makees driving thermal medium, and the high steam that waste heat boiler E is generated enters steam turbine D decompression work done, steam turbine E row
Low-pressure steam out enters heat exchanger G, heat release in heated medium into condensate liquid, and condensate liquid mentions after circulating pump F pressurization
Supply waste heat boiler E, heat absorption is provided at high steam and to steam turbine D;Compressor, the second condenser, evaporator, low temperature section
Flowing valve, the second cryogenic throttle valve and low temperature heat exchanger progress, compression reverse circulation --- refrigerant vapour enters compressor H, warp
It is compressed into low pressure refrigerant vapour and is divided into two parts later, a portion continues to be compressed into high pressure refrigerant vapour, another part
Evaporator 6 and heat release are flowed through into low pressure cryogen liquid, low pressure cryogen liquid again through cryogenic throttle valve I throttling enter low temperature heat exchanger J,
It absorbs heat into refrigerant vapour and is provided to compressor H, the high pressure refrigerant vapour that compressor H is generated flows through the second condenser L and heat release
In heated medium at high pressure cryogen liquid, high pressure cryogen liquid stream, which cools down through evaporator 6 and throttles through the second cryogenic throttle valve N, to be entered
Low temperature heat exchanger J, heat absorption are provided at refrigerant vapour and to compressor H;Absorber, the second absorber, generator, second occur
Device, condenser, evaporator, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger carry out
The weak solution of absorption reverse circulation --- absorber 1 enters the second absorber 2 through solution pump 8 and solution heat exchanger 10, inhales
Refrigerant vapour and heat release are received in heated medium, the weak solution of the second absorber 2 is through the second solution pump 9 and the second solution heat exchange
Device 11 enters generator 3, heat absorption release refrigerant vapour and provides to condenser 5, and the concentrated solution of generator 3 is handed over through the second solution heat
Parallel operation 11 enters the second generator 4, heat absorption release refrigerant vapour and provides to the second absorber 2, the concentrated solution of the second generator 4
Enter absorber 1 through solution heat exchanger 10, absorb refrigerant vapour and heat release in heated medium, the refrigerant vapour of condenser 5
In heated medium at cryogen liquid, the cryogen liquid of condenser 5 enters evaporator 6, heat absorption through the throttling of throttle valve 7 and steams at cryogen for heat release
Vapour is simultaneously provided to absorber 1;Air-steam forward circulation provides power to compression reverse circulation respectively and to absorption reverse
Circulation provides driving thermic load, compression reverse circulation obtain low temperature thermic load and respectively by the external heat supply of the second condenser and
By evaporator to absorption reverse circulation heat supply, absorption reverse circulation passes through absorber, the second absorber and condenser pair
Outer heat supply forms combined cycle energy supplying system.
Combined cycle energy supplying system shown in Fig. 9 is achieved in that
(1) in structure, it is mainly handed over by compressor, boiler, air turbine, steam turbine, waste heat boiler, circulating pump, heat
It is parallel operation, compressor, expanding machine, low temperature heat exchanger, evaporator, absorber, the second absorber, generator, the second generator, cold
Condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger device and working machine are formed;
Compressor A has air duct to be connected to outside, and boiler B has pressure again after compressor A is connected to there are also compressed air channel with boiler B
Contracting air duct is connected to air turbine C, boiler B there are also fuel and air channel with outside be connected to, there are also blast tubes by boiler B
It is connected to waste heat boiler E, there are also air ducts to be connected to waste heat boiler E by air turbine C, and that there are also mixed gas is logical by waste heat boiler E
Second generator 4 has mixed-gas channel to be connected to outside again after road is sequentially communicated generator 3 and the second generator 4, steam
Turbine D has low-pressure steam channel to be connected to heat exchanger G, and there are also condensate liquid pipelines through circulating pump F and waste heat boiler by heat exchanger G
E connection, there are also high steam channels to be connected to steam turbine D by waste heat boiler E, heat exchanger G there are also heated medium pipeline and
Outside connection;The finisher 6 that compressor H has refrigerant gas channel to be connected to evaporator 6 has refrigerant gas channel and expansion again
Machine O connection, there are also refrigerant gas channels to be connected to through low temperature heat exchanger J with compressor H by expanding machine O, and low temperature heat exchanger J is also
Cryogenic media pipeline is connected to outside;Evaporator 6 is connected to there are also refrigerant steam channel with absorber 1, and there are also weak solutions for absorber 1
Pipeline is connected to through solution pump 8 and solution heat exchanger 10 with the second absorber 2, and there are also weak solution pipelines through for the second absorber 2
Two solution pumps 9 and the second solution heat exchanger 11 are connected to generator 3, and there are also concentrated solution pipelines through the second solution heat for generator 3
Exchanger 11 is connected to the second generator 4, and there are also concentrated solution pipelines through solution heat exchanger 10 and absorber 1 for the second generator 4
Connection, generator 3 are connected to there are also refrigerant steam channel with condenser 5, and there are also refrigerant steam channels and the second suction for the second generator 4
It receives device 2 to be connected to, condenser 5 is connected to there are also cryogen liquid pipeline with evaporator 6 through throttle valve 7, absorber 1, the second absorber 2 and cold
Condenser 5 also has heated medium pipeline to be connected to outside respectively;Compressor, boiler, air turbine, steam turbine, waste heat boiler,
Circulating pump, heat exchanger and operating mechanism are at air-steam forward circulation system, compressor, evaporator, expanding machine and Low Temperature Thermal
Exchanger constitutes compression reverse circulation system, absorber, the second absorber, generator, the second generator, condenser, evaporation
Device, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger constitute absorption reverse circulation
System.
(2) in process, compressor, boiler, air turbine, steam turbine, waste heat boiler, circulating pump and heat exchanger are carried out
Air-steam forward circulation --- fuel and air enter boiler B and burn, combustion gas in boiler B heat release in compressed air it
Enter waste heat boiler E afterwards, air flows through compressor A boosting heating, enters after compressed air flows through boiler B, heat absorption heats up empty
Gas-turbine C, compressed air flow through air turbine C decompression work done, and the air after work done enters waste heat boiler E, combustion gas and air
Condensate liquid is heated in waste heat boiler E is supplied to generator 3 and second at the mixed gas that high steam, combustion gas and air are formed
Generator 4 makees driving thermal medium, and the high steam that waste heat boiler E is generated enters steam turbine D decompression work done, steam turbine E row
Low-pressure steam out enters heat exchanger G, heat release in heated medium into condensate liquid, and condensate liquid mentions after circulating pump F pressurization
Supply waste heat boiler E, heat absorption is provided at high steam and to steam turbine D;Compressor, evaporator, expanding machine and Low Temperature Thermal are handed over
Parallel operation carries out compression reverse circulation --- and refrigerant gas enters compressor H, and evaporator 6 and heat release drop are flowed through after boosting heating
Temperature, refrigerant gas flow through expanding machine O decompression work done, and the refrigerant gas after work done flows through low temperature heat exchanger J, heat absorption heating
Backward compressor H is provided;Absorber, the second absorber, generator, the second generator, condenser, evaporator, throttle valve, solution
Pump, the second solution pump, solution heat exchanger and the second solution heat exchanger carry out absorption reverse circulation --- absorber 1 it is dilute
Solution enters the second absorber 2 through solution pump 8 and solution heat exchanger 10, absorbs refrigerant vapour and heat release is in heated medium,
The weak solution of second absorber 2 enters generator 3, heat absorption release cryogen through the second solution pump 9 and the second solution heat exchanger 11
Steam is simultaneously provided to condenser 5, and the concentrated solution of generator 3 enters the second generator 4 through the second solution heat exchanger 11, heat absorption is released
Put refrigerant vapour and provided to the second absorber 2, the concentrated solution of the second generator 4 through solution heat exchanger 10 enter absorber 1,
It absorbs refrigerant vapour and heat release is in heated medium, the refrigerant vapour heat release of condenser 5 is in heated medium at cryogen liquid, condensation
The cryogen liquid of device 5 enters evaporator 6 through the throttling of throttle valve 7, absorbs heat into refrigerant vapour and provides to absorber 1;Air-steam is just
Power is provided to working machine and compression reverse circulation respectively to circulation, and air-steam forward circulation is to absorption reverse circulation
Driving thermic load is provided, compression reverse circulation obtains low temperature thermic load and by evaporator to absorption reverse circulation heat supply,
Absorption reverse circulation forms combined cycle energy supplying system by absorber, the second absorber and the external heat supply of condenser.
Combined cycle energy supplying system shown in Figure 10 is achieved in that
In combined cycle energy supplying system shown in Fig. 9, increase the second compressor, by compressor H have refrigerant gas channel with
The finisher 6 of 6 connection of evaporator has refrigerant gas channel to be connected to expanding machine O to be adjusted to compressor H and have refrigerant gas logical again
The finisher 6 that road is connected to evaporator 6 has refrigerant gas channel to be connected to the second compressor K again, and there are also cold by the second compressor K
The finisher 6 that agent gas passage is connected to evaporator 6 has refrigerant gas channel to be connected to expanding machine O again;What compressor H was generated
Refrigerant gas is supplied to the second compressor K, the refrigerant gas stream that the second compressor K is generated after flowing through 6 heat release of evaporator cooling
It is supplied to expanding machine O after 6 heat release of evaporator cooling, forms combined cycle energy supplying system.
Combined cycle energy supplying system shown in Figure 11 is achieved in that
(1) in structure, it is mainly handed over by compressor, boiler, air turbine, steam turbine, waste heat boiler, circulating pump, heat
Parallel operation, compressor, expanding machine, low temperature heat exchanger, regenerator, evaporator, absorber, the second absorber, generator, the second hair
Raw device, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and working machine institute
Composition;Compressor A has air duct to be connected to outside, boiler B after compressor A is connected to there are also compressed air channel with boiler B
There is compressed air channel to be connected to air turbine C again, boiler B there are also fuel and air channel with outside be connected to, boiler B there are also combustion
Gas channel is connected to waste heat boiler E, and there are also air ducts to be connected to waste heat boiler E by air turbine C, and there are also mix by waste heat boiler E
Second generator 4 has mixed-gas channel to connect with outside again after gas passage is sequentially communicated generator 3 and the second generator 4
Logical, steam turbine D has low-pressure steam channel to be connected to heat exchanger G, heat exchanger G there are also condensate liquid pipelines through circulating pump F and
Waste heat boiler E connection, there are also high steam channels to be connected to steam turbine D by waste heat boiler E, and heat exchanger G is also heated Jie
Matter pipeline is connected to outside;The finisher 6 that compressor H has refrigerant gas channel to be connected to evaporator 6 has refrigerant gas logical again
Road is connected to through regenerator P with expanding machine O, and there are also refrigerant gas channels through low temperature heat exchanger J and regenerator P and pressure by expanding machine O
Contracting machine H connection, there are also cryogenic media pipelines to be connected to external by low temperature heat exchanger J;Evaporator 6 is there are also refrigerant steam channel and inhales
Device 1 to be received to be connected to, absorber 1 is connected to through solution pump 8 and solution heat exchanger 10 with the second absorber 2 there are also weak solution pipeline, the
Two absorbers 2 are connected to through the second solution pump 9 and the second solution heat exchanger 11 with generator 3 there are also weak solution pipeline, generator 3
There are also concentrated solution pipelines to be connected to through the second solution heat exchanger 11 with the second generator 4, and there are also concentrated solution pipelines for the second generator 4
It is connected to through solution heat exchanger 10 with absorber 1, generator 3 is connected to there are also refrigerant steam channel with condenser 5, the second generator
4 are connected to there are also refrigerant steam channel with the second absorber 2, and there are also cryogen liquid pipelines through throttle valve 7 and the company of evaporator 6 for condenser 5
Logical, absorber 1, the second absorber 2 and condenser 5 also have heated medium pipeline to be connected to outside respectively;Compressor, boiler,
Air turbine, steam turbine, waste heat boiler, circulating pump and heat exchanger constitute air-steam forward circulation system;Compressor,
Evaporator, expanding machine, low temperature heat exchanger and regenerator constitute compression reverse circulation system, absorber, the second absorber, hair
Raw device, the second generator, condenser, evaporator, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution
Heat exchanger constitutes absorption reverse circulation system.
(2) in process, compared with the combined cycle energy supplying system shown in Fig. 9, the difference is that: compressor H is generated cold
Agent gas is supplied to regenerator P after flowing through 6 heat release of evaporator cooling, and refrigerant gas mentions after flowing through regenerator P heat release cooling
Supply expanding machine O;Expanding machine O discharge refrigerant gas followed by low temperature heat exchanger J and regenerator P, gradually heat absorption heating
It is supplied to compressor H later.
Combined cycle energy supplying system shown in Figure 12 is achieved in that
In the combined cycle energy supplying system shown in Figure 11, increase the second compressor, by compressor H have refrigerant gas channel with
The finisher 6 of 6 connection of evaporator have again refrigerant gas channel be connected to through regenerator P with expanding machine O be adjusted to compressor H have it is cold
The finisher 6 that agent gas passage is connected to logical evaporator 6 has refrigerant gas channel to be connected to the second compressor K again, the second pressure
There are also the finishers 6 that refrigerant gas channel is connected to evaporator 6 to have refrigerant gas channel through regenerator P and expansion again by contracting machine K
Machine O connection;The refrigerant gas that compressor H is generated is supplied to the second compressor K, the second pressure after flowing through evaporator 6, heat release cooling
The refrigerant gas that contracting machine K is generated forms connection followed by expanding machine O is supplied to after evaporator 6 and regenerator P, heat release cooling
Close circulation energy supplying system.
Combined cycle energy supplying system shown in Figure 13 is achieved in that
(1) in structure, it is mainly handed over by compressor, boiler, air turbine, steam turbine, waste heat boiler, circulating pump, heat
Parallel operation, compressor, expanding machine, cooler, low temperature heat exchanger, evaporator, absorber, the second absorber, generator, the second hair
Raw device, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger are formed;Pressure
Mechanism of qi A has air duct to be connected to outside, and boiler B has compression again after compressor A is connected to there are also compressed air channel with boiler B
Air duct is connected to air turbine C, and there are also fuel and air channels be connected to outside by boiler B, boiler B there are also blast tube and
Waste heat boiler E connection, there are also air ducts to be connected to waste heat boiler E by air turbine C, and there are also mixed-gas channels by waste heat boiler E
Second generator 4 has mixed-gas channel to be connected to outside again after being sequentially communicated generator 3 and the second generator 4, vapor wheel
Machine D has low-pressure steam channel to be connected to heat exchanger G, and there are also condensate liquid pipelines through circulating pump F and waste heat boiler E by heat exchanger G
Connection, there are also high steam channels be connected to steam turbine D by waste heat boiler E, heat exchanger G there are also heated medium pipeline with outside
Portion's connection;Compressor H has refrigerant gas channel to be connected to through cooler M with expanding machine O, and there are also refrigerant gas channel warps by expanding machine O
Low temperature heat exchanger J is connected to compressor H, low temperature heat exchanger J there are also cryogenic media pipeline with outside be connected to, cooler M is also
There is heated medium pipeline to be connected to outside;Evaporator 6 has refrigerant steam channel to be connected to absorber 1, and there are also dilute molten for absorber 1
Liquid pipeline is connected to through solution pump 8 and solution heat exchanger 10 with the second absorber 2, and there are also weak solution pipelines to pass through for the second absorber 2
Second solution pump 9 and the second solution heat exchanger 11 are connected to generator 3, and there are also concentrated solution pipelines through the second solution for generator 3
Heat exchanger 11 is connected to the second generator 4, and there are also concentrated solution pipelines through solution heat exchanger 10 and absorber for the second generator 4
1 connection, generator 3 are connected to there are also refrigerant steam channel with condenser 5, and there are also refrigerant steam channels and second for the second generator 4
Absorber 2 is connected to, and condenser 5 is connected to through throttle valve 7 with evaporator 6 there are also cryogen liquid pipeline, and there are also cryogenic media pipes for evaporator 6
Road is connected to outside, and absorber 1, the second absorber 2 and condenser 5 also have heated medium pipeline to be connected to outside respectively;Pressure
Mechanism of qi, boiler, air turbine, steam turbine, waste heat boiler, circulating pump and heat exchanger constitute air-steam forward circulation system
System, compressor, cooler, expanding machine and low temperature heat exchanger constitute compression reverse circulation system, and absorber, second absorb
Device, generator, the second generator, condenser, evaporator, throttle valve, solution pump, the second solution pump, solution heat exchanger and
Two solution heat exchangers constitute absorption reverse circulation system.
(2) in process, compressor, boiler, air turbine, steam turbine, waste heat boiler, circulating pump and heat exchanger are carried out
Air-steam forward circulation --- fuel and air enter boiler B and burn, combustion gas in boiler B heat release in compressed air it
Enter waste heat boiler E afterwards, air flows through compressor A boosting heating, enters after compressed air flows through boiler B, heat absorption heats up empty
Gas-turbine C, compressed air flow through air turbine C decompression work done, and the air after work done enters waste heat boiler E, combustion gas and air
Condensate liquid is heated in waste heat boiler E is supplied to generator 3 and second at the mixed gas that high steam, combustion gas and air are formed
Generator 4 makees driving thermal medium, and the high steam that waste heat boiler E is generated enters steam turbine D decompression work done, steam turbine E row
Low-pressure steam out enters heat exchanger G, heat release in heated medium into condensate liquid, and condensate liquid mentions after circulating pump F pressurization
Supply waste heat boiler E, heat absorption is provided at high steam and to steam turbine D;Compressor, cooler, expanding machine and Low Temperature Thermal are handed over
Parallel operation carries out compression reverse circulation --- and refrigerant gas enters compressor H, and cooler M and heat release drop are flowed through after boosting heating
Temperature, refrigerant gas flow through expanding machine O decompression work done, and the refrigerant gas after decompression work done flows through low temperature heat exchanger J, heat absorption rises
Wen Bingxiang compressor H is provided;It is absorber, the second absorber, generator, the second generator, condenser, evaporator, throttle valve, molten
Liquid pump, the second solution pump, solution heat exchanger and the second solution heat exchanger carry out absorption reverse circulation --- absorber 1
Weak solution enters the second absorber 2 through solution pump 8 and solution heat exchanger 10, absorbs refrigerant vapour and heat release is situated between in being heated
The weak solution of matter, the second absorber 2 is cold into generator 3, heat absorption release through the second solution pump 9 and the second solution heat exchanger 11
Agent steam is simultaneously provided to condenser 5, and the concentrated solution of generator 3 enters the second generator 4, heat absorption through the second solution heat exchanger 11
It discharges refrigerant vapour and is provided to the second absorber 2, the concentrated solution of the second generator 4 enters absorber through solution heat exchanger 10
1, absorb refrigerant vapour and heat release in heated medium, the refrigerant vapour heat release of condenser 5 in heated medium at cryogen liquid, it is cold
The cryogen liquid of condenser 5 enters evaporator 6 through the throttling of throttle valve 7, absorbs heat into refrigerant vapour and provides to absorber 1;Air-steam
Forward circulation provides power to compression reverse circulation respectively and provides driving thermic load to absorption reverse circulation, and compression is inverse
Low temperature thermic load is obtained to circulation and passes through the external heat supply of cooler, and absorption reverse circulation obtains low temperature thermic load and simultaneously passes through suction
Device, the second absorber and the external heat supply of condenser are received, combined cycle energy supplying system is formed.
Combined cycle energy supplying system shown in Figure 14 is achieved in that
In the combined cycle energy supplying system shown in Figure 13, increase by the second compressor, compressor H is had into refrigerant gas channel warp
Cooler M is connected to expanding machine O to be adjusted to compressor H and has refrigerant gas channel to be connected to through cooler M with the second compressor K, and
There are also refrigerant gas channels to be connected to through cooler M with expanding machine O by two compressor K;The refrigerant gas that compressor H is generated flows through cooling
The second compressor K is supplied to after device M heat release cooling, the refrigerant gas that the second compressor K is generated flows through after cooler M heat release
It is supplied to expanding machine O, forms combined cycle energy supplying system.
Combined cycle energy supplying system shown in Figure 15 is achieved in that
(1) in structure, it is mainly handed over by compressor, boiler, air turbine, steam turbine, waste heat boiler, circulating pump, heat
Parallel operation, cooler, expanding machine, low temperature heat exchanger, regenerator, evaporator, absorber, the second absorber, occurs compressor
Device, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger
It is formed;Compressor A has air duct to be connected to outside, boiler after compressor A is connected to there are also compressed air channel with boiler B
B has compressed air channel to be connected to air turbine C again, boiler B there are also fuel and air channel with outside be connected to, boiler B is also
Blast tube is connected to waste heat boiler E, and there are also air ducts to be connected to waste heat boiler E by air turbine C, and there are also mixed by waste heat boiler E
Close the second generator 4 after gas passage is sequentially communicated generator 3 and the second generator 4 has mixed-gas channel to connect with outside again
Logical, steam turbine D has low-pressure steam channel to be connected to heat exchanger G, heat exchanger G there are also condensate liquid pipelines through circulating pump F and
Waste heat boiler E connection, there are also high steam channels to be connected to steam turbine D by waste heat boiler E, and heat exchanger G is also heated Jie
Matter pipeline is connected to outside;Compressor H has refrigerant gas channel to be connected to through cooler M and regenerator P with expanding machine O, expanding machine O
There are also refrigerant gas channels to be connected to through low temperature heat exchanger J and regenerator P with compressor H, and there are also low temperature Jie by low temperature heat exchanger J
Matter pipeline be connected to outside, and there are also heated medium pipelines to be connected to external by cooler M;Evaporator 6 have refrigerant steam channel with
Absorber 1 is connected to, and absorber 1 is connected to through solution pump 8 and solution heat exchanger 10 with the second absorber 2 there are also weak solution pipeline,
Second absorber 2 is connected to through the second solution pump 9 and the second solution heat exchanger 11 with generator 3 there are also weak solution pipeline, is occurred
Device 3 is connected to through the second solution heat exchanger 11 with the second generator 4 there are also concentrated solution pipeline, and there are also concentrated solutions for the second generator 4
Pipeline is connected to through solution heat exchanger 10 with absorber 1, and generator 3 is connected to there are also refrigerant steam channel with condenser 5, the second hair
Raw device 4 is connected to there are also refrigerant steam channel with the second absorber 2, and there are also cryogen liquid pipelines through throttle valve 7 and evaporator for condenser 5
6 connections, the also cryogenic media pipeline of evaporator 6 are connected to outside, and absorber 1, the second absorber 2 and condenser 5 also have respectively
Heated medium pipeline is connected to outside;Compressor, boiler, air turbine, steam turbine, waste heat boiler, circulating pump and Re Jiao
Parallel operation constitutes air-steam forward circulation system, and compressor, cooler, expanding machine, low temperature heat exchanger and regenerator constitute pressure
Contracting formula reverse circulation system, it is absorber, the second absorber, generator, the second generator, condenser, evaporator, throttle valve, molten
Liquid pump, the second solution pump, solution heat exchanger and the second solution heat exchanger constitute absorption reverse circulation system.
(2) in process, compared with the combined cycle energy supplying system shown in Figure 13, the difference is that: compressor, cooler,
Expanding machine, low temperature heat exchanger and regenerator carry out compression reverse circulation --- and the refrigerant gas that compressor H is generated successively flows
Expanding machine O is supplied to after cooler M and regenerator P, heat release cooling, refrigerant gas flows through expanding machine O decompression work done, expansion
The refrigerant gas of machine O discharge provides followed by the backward compressor H of low temperature heat exchanger J and regenerator P, heating of absorbing heat.
Combined cycle energy supplying system shown in Figure 16 is achieved in that
In the combined cycle energy supplying system shown in Figure 15, increase by the second compressor, compressor H is had into refrigerant gas channel warp
Cooler M and regenerator P is connected to expanding machine O to be adjusted to compressor H and has refrigerant gas channel through cooler M and the second compressor
K connection, the second compressor K have refrigerant gas channel to be connected to through cooler M and regenerator P with expanding machine O again;Compressor H is generated
Refrigerant gas flow through cooler M heat release cooling after be supplied to the second compressor K, the refrigerant gas that the second compressor K is generated
Followed by expanding machine O is supplied to after cooler M and regenerator P, heat release cooling, combined cycle energy supplying system is formed.
Combined cycle energy supplying system shown in Figure 17 is achieved in that
(1) in structure, it is mainly handed over by compressor, boiler, air turbine, steam turbine, waste heat boiler, circulating pump, heat
Parallel operation, compressor, cooler, expanding machine, low temperature heat exchanger, evaporator, absorber, the second absorber, generator, the second hair
Raw device, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger are formed;Pressure
Mechanism of qi A has air duct to be connected to outside, and boiler B has compression again after compressor A is connected to there are also compressed air channel with boiler B
Air duct is connected to air turbine C, and there are also fuel and air channels be connected to outside by boiler B, boiler B there are also blast tube and
Waste heat boiler E connection, there are also air ducts to be connected to waste heat boiler E by air turbine C, and there are also mixed-gas channels by waste heat boiler E
Second generator 4 has mixed-gas channel to be connected to outside again after being sequentially communicated generator 3 and the second generator 4, vapor wheel
Machine D has low-pressure steam channel to be connected to heat exchanger G, and there are also condensate liquid pipelines through circulating pump F and waste heat boiler E by heat exchanger G
Connection, there are also high steam channels be connected to steam turbine D by waste heat boiler E, heat exchanger G there are also heated medium pipeline with outside
Portion's connection;The finisher 6 that compressor H has refrigerant gas channel to be connected to through cooler M with evaporator 6 has refrigerant gas channel again
It is connected to expanding machine O, there are also refrigerant gas channels to be connected to through low temperature heat exchanger J with compressor H by expanding machine O, low temperature heat exchange
There are also cryogenic media pipelines be connected to outside by device J, and there are also heated medium pipelines to be connected to external by cooler M;Evaporator 6 is also
Refrigerant steam channel is connected to absorber 1, and there are also weak solution pipelines through solution pump 8 and solution heat exchanger 10 and for absorber 1
The connection of two absorbers 2, there are also weak solution pipelines through the second solution pump 9 and the second solution heat exchanger 11 and hair for the second absorber 2
Raw device 3 is connected to, and generator 3 is connected to through the second solution heat exchanger 11 with the second generator 4 there are also concentrated solution pipeline, and second occurs
Device 4 is connected to through solution heat exchanger 10 with absorber 1 there are also concentrated solution pipeline, and there are also refrigerant steam channels and condensation for generator 3
Device 5 is connected to, and the second generator 4 is connected to there are also refrigerant steam channel with the second absorber 2, and there are also cryogen liquid pipelines to pass through for condenser 5
Throttle valve 7 is connected to evaporator 6, and absorber 1, the second absorber 2 and condenser 5 also have heated medium pipeline and outside respectively
Connection;It is positive that compressor, boiler, air turbine, steam turbine, waste heat boiler, circulating pump and heat exchanger constitute air-steam
The circulatory system, compressor, cooler, evaporator, expanding machine and low temperature heat exchanger constitute compression reverse circulation system, absorb
Device, the second absorber, generator, the second generator, condenser, evaporator, throttle valve, solution pump, the second solution pump, solution heat
Exchanger and the second solution heat exchanger constitute absorption reverse circulation system.
(2) in process, compared with the combined cycle energy supplying system shown in Fig. 9, in addition to no working machine, the difference is that:
The refrigerant gas that compressor H is generated is supplied to expanding machine O followed by cooler M and evaporator 6, gradually after heat release cooling,
Compression reverse circulation obtains low temperature thermic load and respectively by the external heat supply of cooler and by evaporator to absorption reverse
Circulation heating.
Combined cycle energy supplying system shown in Figure 18 is achieved in that
In the combined cycle energy supplying system shown in Figure 17, increase by the second compressor, compressor H is had into refrigerant gas channel warp
The finisher 6 that cooler M is connected to evaporator 6 have again refrigerant gas channel be connected to expanding machine O be adjusted to compressor H have it is cold
The finisher 6 that agent gas passage is connected to through cooler M with evaporator 6 has refrigerant gas channel to be connected to the second compressor K again,
There are also the finishers 6 that refrigerant gas channel is connected to through cooler M with evaporator 6 refrigerant gas channel again by second compressor K
It is connected to expanding machine O;The refrigerant gas that compressor H is generated is followed by offer after cooler M and evaporator 6, heat release cooling
To the second compressor K, after the refrigerant gas that the second compressor K is generated is followed by cooler M and evaporator 6, heat release cooling
It is supplied to expanding machine O, forms combined cycle energy supplying system.
Combined cycle energy supplying system shown in Figure 19 is achieved in that
(1) in structure, it is mainly handed over by compressor, boiler, air turbine, steam turbine, waste heat boiler, circulating pump, heat
Parallel operation, cooler, regenerator, expanding machine, low temperature heat exchanger, evaporator, absorber, the second absorber, occurs compressor
Device, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger
It is formed;Compressor A has air duct to be connected to outside, boiler after compressor A is connected to there are also compressed air channel with boiler B
B has compressed air channel to be connected to air turbine C again, boiler B there are also fuel and air channel with outside be connected to, boiler B is also
Blast tube is connected to waste heat boiler E, and there are also air ducts to be connected to waste heat boiler E by air turbine C, and there are also mixed by waste heat boiler E
Close the second generator 4 after gas passage is sequentially communicated generator 3 and the second generator 4 has mixed-gas channel to connect with outside again
Logical, steam turbine D has low-pressure steam channel to be connected to heat exchanger G, heat exchanger G there are also condensate liquid pipelines through circulating pump F and
Waste heat boiler E connection, there are also high steam channels to be connected to steam turbine D by waste heat boiler E, and heat exchanger G is also heated Jie
Matter pipeline is connected to outside;The finisher 6 that compressor H has refrigerant gas channel to be connected to through cooler M with evaporator 6 has cold again
Agent gas passage is connected to through regenerator P with expanding machine O, and there are also refrigerant gas channels through low temperature heat exchanger J and backheat by expanding machine O
Device P is connected to compressor H, low temperature heat exchanger J there are also cryogenic media pipeline with outside be connected to, cooler M is also heated Jie
Matter pipeline is connected to outside;Evaporator 6 is connected to there are also refrigerant steam channel with absorber 1, and there are also weak solution pipelines to pass through for absorber 1
Solution pump 8 and solution heat exchanger 10 are connected to the second absorber 2, and there are also weak solution pipelines through the second solution for the second absorber 2
Pump 9 and the second solution heat exchanger 11 are connected to generator 3, and there are also concentrated solution pipelines through the second solution heat exchanger for generator 3
11 are connected to the second generator 4, and the second generator 4 is connected to through solution heat exchanger 10 with absorber 1 there are also concentrated solution pipeline, send out
Raw device 3 is connected to there are also refrigerant steam channel with condenser 5, and there are also refrigerant steam channels and the second absorber 2 to connect for the second generator 4
Logical, condenser 5 is connected to through throttle valve 7 with evaporator 6 there are also cryogen liquid pipeline, and absorber 1, the second absorber 2 and condenser 5 are also
There is heated medium pipeline to be connected to outside respectively;Compressor, boiler, air turbine, steam turbine, waste heat boiler, circulating pump
Air-steam forward circulation system, compressor, cooler, evaporator, regenerator, expanding machine and low temperature are constituted with heat exchanger
Heat exchanger constitutes compression reverse circulation system, absorber, the second absorber, generator, the second generator, condenser, steaming
Hair device, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, which are constituted, absorption inversely to follow
Loop system.
(2) in process, compared with the combined cycle energy supplying system shown in Figure 17, the difference is that: compressor H is generated cold
Agent gas is supplied to expanding machine O followed by cooler M, evaporator 6 and regenerator P heat release cooling later, expanding machine O discharge
Refrigerant gas is supplied to compressor H followed by low temperature heat exchanger J and regenerator P heat absorption heating later.
Combined cycle energy supplying system shown in Figure 20 is achieved in that
In the combined cycle energy supplying system shown in Figure 19, increase by the second compressor, compressor H is had into refrigerant gas channel warp
The finisher 6 that cooler M is connected to evaporator 6 has refrigerant gas channel to be connected to through regenerator P with expanding machine O to be adjusted to press again
The finisher 6 that contracting machine H has refrigerant gas channel to be connected to through cooler M with evaporator 6 has refrigerant gas channel and the second pressure again
Contracting machine K connection, the second compressor K there are also the finisher 6 that refrigerant gas channel is connected to through cooler M with evaporator 6 have again it is cold
Agent gas passage is connected to through regenerator P with expanding machine O;The refrigerant gas that compressor H is generated is followed by cooler M and evaporator
6, the second compressor K is supplied to after heat release cooling, the refrigerant gas that the second compressor K is generated is followed by cooler M, evaporation
It is supplied to expanding machine O after device 6 and regenerator P heat release cooling, forms combined cycle energy supplying system.
Combined cycle energy supplying system shown in Figure 21 is achieved in that
(1) in structure, in combined cycle energy supplying system shown in Fig. 1, increase second heat exchanger, by the second generator 4
Have mixed-gas channel with outside be connected to be adjusted to the second generator 4 have mixed-gas channel through second heat exchanger 12 with outside
Connection, the also heated medium pipeline of second heat exchanger 12 are connected to outside;Increase third generator, second throttle, the
Three solution pumps and third solution heat exchanger, the second absorber 2 add weak solution pipeline through third solution pump 15 and third solution
Heat exchanger 16 is connected to third generator 13, third generator 13 there are also concentrated solution pipeline through third solution heat exchanger 16 with
Generator 3 is had refrigerant steam channel to be connected to condenser 5 and is adjusted to generator 3 and has refrigerant vapour to lead to by the connection of the second generator 4
Third generator 13 has cryogen liquid pipeline to connect through second throttle 14 and condenser 5 again after road is connected to third generator 13
Logical, third generator 13 is connected to there are also refrigerant steam channel with condenser 5.
(2) in process, the mixed gas of waste heat boiler E discharge is followed by generator 3, the second generator 4 and the second heat
Exchanger 12, externally discharge after heat release cooling;The refrigerant vapour that generator 3 generates is supplied to third generator 13 and makees driving heat
The part weak solution of medium, the second absorber 2 enters third generator through third solution pump 15 and third solution heat exchanger 16
13, the solution that refrigerant vapour flows through third generator 13, heating enters in it discharges refrigerant vapour and provides to condenser 5, the
The concentrated solution of three generators 13 enters the second generator 4 through third solution heat exchanger 16, flows through the cryogen of third generator 13
Steam heat release enters condenser 5 through the throttling of second throttle 14 at after cryogen liquid, forms combined cycle energy supplying system.
Combined cycle energy supplying system shown in Figure 22 is achieved in that
(1) in structure, in combined cycle energy supplying system shown in Fig. 1, increase second heat exchanger, by the second generator 4
Have mixed-gas channel with outside be connected to be adjusted to the second generator 4 have mixed-gas channel through second heat exchanger 12 and evaporate
Device 6 is connected to outside, and the also heated medium pipeline of second heat exchanger 12 is connected to outside;Increase third generator, second
Second absorber 2 is had weak solution pipeline to hand over through the second solution pump 9 and the second solution heat by throttle valve and third solution heat exchanger
Parallel operation 11 is connected to generator 3 to be adjusted to the second absorber 2 and has weak solution pipeline through the second solution pump 9, the second solution heat exchange
Device 11 and third solution heat exchanger 16 are connected to generator 3, have concentrated solution pipeline through the second solution heat exchanger in generator 3
11 are connected to the second generator 4 and are adjusted to generator 3 and have concentrated solution pipeline through third solution heat exchanger 16 and third generator
13 connections, third generator 13 have concentrated solution pipeline to be connected to through the second solution heat exchanger 11 with the second generator 4 again, will occur
Device 3 has refrigerant steam channel to be connected to condenser 5 to be adjusted to generator 3 and have refrigerant steam channel to be connected to it with third generator 13
Third generator 13 has cryogen liquid pipeline to be connected to through second throttle 14 with condenser 5 again afterwards, and there are also cryogens for third generator 13
Steam channel is connected to condenser 5.
(2) in process, the mixed gas of waste heat boiler E discharge is handed over followed by generator 3, second the 4, second heat of generator
Parallel operation 12 and evaporator 6, gradually externally discharge after heat release cooling;The refrigerant vapour that generator 3 generates is supplied to third
Device 13 makees driving thermal medium, and the weak solution of the second absorber 2 is molten through the second solution pump 9, the second solution heat exchanger 11 and third
Liquid heat exchanger 16 enters generator 3, and the concentrated solution of generator 3 enters third generator 13 through third solution heat exchanger 16,
The solution that refrigerant vapour flows through third generator 13, heating enters in it discharges refrigerant vapour and provides to condenser 5, third hair
The concentrated solution of raw device 13 enters the second generator 4 through the second solution heat exchanger 11, flows through the refrigerant vapour of third generator 13
Heat release enters condenser 5 through the throttling of second throttle 14 at after cryogen liquid, forms combined cycle energy supplying system.
Combined cycle energy supplying system shown in Figure 23 is achieved in that
(1) in structure, in combined cycle energy supplying system shown in Fig. 1, increase second heat exchanger, by the second generator 4
Have mixed-gas channel with outside be connected to be adjusted to the second generator 4 have mixed-gas channel through second heat exchanger 12, evaporate
Device 6 and low temperature heat exchanger J are connected to outside, and the also heated medium pipeline of second heat exchanger 12 is connected to outside;Increase
Second absorber 2 is had weak solution pipeline by third generator, second throttle, third solution pump and third solution heat exchanger
It is connected to through the second solution pump 9 and the second solution heat exchanger 11 with generator 3 and is adjusted to the second absorber 2 and has weak solution pipeline warp
Second solution pump 9 and the second solution heat exchanger 11 are connected to third generator 13, and third generator 13 has concentrated solution pipeline again
It is connected to through third solution pump 15 and third solution heat exchanger 16 with generator 3, has concentrated solution pipeline molten through second in generator 3
Liquid heat exchanger 11 be connected to the second generator 4 be adjusted to generator 3 have concentrated solution pipeline through third solution heat exchanger 16 and
Second solution heat exchanger 11 is connected to the second generator 4, has refrigerant steam channel to be connected to adjustment with condenser 5 in generator 3
Third generator 13 has cryogen liquid pipeline through second again after having refrigerant steam channel to be connected to third generator 13 for generator 3
Throttle valve 14 is connected to condenser 5, and third generator 13 is connected to there are also refrigerant steam channel with condenser 5.
(2) in process, the mixed gas of waste heat boiler E discharge is handed over followed by generator 3, second the 4, second heat of generator
Parallel operation 12, evaporator 6 and low temperature heat exchanger J, gradually externally discharge after heat release cooling;The refrigerant vapour that generator 3 generates
It is supplied to third generator 13 and makees driving thermal medium, the weak solution of the second absorber 2 is through solution pump 9 and the second solution heat exchanger
11 enter third generator 13, and refrigerant vapour flows through third generator 13, heating enters the solution release refrigerant vapour in it simultaneously
It is provided to condenser 5, the concentrated solution of third generator 13 enters through third solution pump 15 and third solution heat exchanger 16 to be occurred
The concentrated solution of device 3, generator 3 enters the second generator 4, stream through third solution heat exchanger 16 and the second solution heat exchanger 11
Enter condenser 5 through the throttling of second throttle 14 through the refrigerant vapour heat release of third generator 13 is at cryogen liquid after, forms connection
Close circulation energy supplying system.
Combined cycle energy supplying system shown in Figure 24 is achieved in that
In the combined cycle energy supplying system shown in Figure 22, there is mixed-gas channel to be connected to the second generator 4 in generator 3
The second generator 4 has mixed-gas channel to be adjusted to generator 3 with external be connected to through second heat exchanger 12 and evaporator 6 later
Second generator 4 has mixed gas logical again after having mixed-gas channel to be sequentially communicated third generator 13 and the second generator 4
Road is connected to through second heat exchanger 12 and evaporator 6 with outside;Waste heat boiler E discharge mixed gas followed by generator 3,
Third generator 13, the second generator 4, second heat exchanger 12 and 6 heat release of evaporator cooling form combined cycle energy supply system
System.
Combined cycle energy supplying system shown in Figure 25 is achieved in that
(1) in structure, in the combined cycle energy supplying system shown in Figure 21, increase the 4th generator, third throttle valve, the 4th
Solution pump and the 4th solution heat exchanger, the second absorber 2 add weak solution pipeline through the 4th solution pump 19 and the 4th solution heat
Exchanger 20 is connected to the 4th generator 17, and there are also concentrated solution pipelines through the 4th solution heat exchanger 20 and for the 4th generator 17
The connection of two generators 4, by third generator 13 have refrigerant steam channel be connected to condenser 5 be adjusted to third generator 13 have it is cold
After agent steam channel is connected to the 4th generator 17 the 4th generator 17 have again cryogen liquid pipeline through third throttle valve 18 with it is cold
Condenser 5 is connected to, and the 4th generator 17 is connected to there are also refrigerant steam channel with condenser 5.
(2) in process, the refrigerant vapour that third generator 13 generates is supplied to the 4th generator 17 and makees driving thermal medium, the
The part weak solution of two absorbers 2 enters the 4th generator 17, cryogen through the 4th solution pump 19 and the 4th solution heat exchanger 20
The solution that steam flows through the 4th generator 17, heating enters in it discharges refrigerant vapour and provides to condenser 5, the 4th generator
17 concentrated solution enters the second generator 4 through the 4th solution heat exchanger 20, flows through the refrigerant vapour heat release of the 4th generator 17
Enter condenser 5 through the throttling of third throttle valve 18 at after cryogen liquid, forms combined cycle energy supplying system.
Combined cycle energy supplying system shown in Figure 26 is achieved in that
(1) in structure, in the combined cycle energy supplying system shown in Figure 22, there is cryogen liquid pipeline through in third generator 13
Two throttle valves 14 are connected to condenser 5 to be adjusted to third generator 13 and has cryogen liquid pipeline through the 4th generator 17 and the second throttling
Valve 14 is connected to condenser 5;Increase the 4th generator, third throttle valve and the 4th solution heat exchanger, the second absorber 2 is had
Weak solution pipeline is connected to tune with generator 3 through the second solution pump 9, the second solution heat exchanger 11 and third solution heat exchanger 16
Whole is that the second absorber 2 has weak solution pipeline through the second solution pump 9, the second solution heat exchanger 11, the 4th solution heat exchanger
20 and third solution heat exchanger 16 be connected to generator 3, there is concentrated solution pipeline to hand over through the second solution heat in third generator 13
Parallel operation 11 is connected to the second generator 4 to be adjusted to third generator 13 and has concentrated solution pipeline through the 4th solution heat exchanger 20 and
The connection of four generators 17, the 4th generator 17 have concentrated solution pipeline to connect through the second solution heat exchanger 11 and the second generator 4 again
It is logical, there is refrigerant steam channel to be connected to condenser 5 in third generator 13 and is adjusted to third generator 13 and has refrigerant steam channel
The 4th generator 17 has cryogen liquid pipeline to be connected to through third throttle valve 18 with condenser 5 again after being connected to the 4th generator 17,
4th generator 17 is connected to there are also refrigerant steam channel with condenser 5.
(2) in process, the cryogen liquid and refrigerant vapour that third generator 13 generates are supplied to the 4th generator 17 and drive
Thermal medium, the weak solution of the second absorber 2 is through the second solution pump 9, the second solution heat exchanger 11, the 4th solution heat exchanger 20
Enter generator 3 with third solution heat exchanger 16, the concentrated solution of generator 3 enters third through third solution heat exchanger 16 and sends out
Raw device 13, the concentrated solution of third generator 13 enter the 4th generator 17 through the 4th solution heat exchanger 20, refrigerant vapour and cold
The solution that agent liquid stream enters in it through the 4th generator 17, heating discharges refrigerant vapour and provides to condenser 5, the 4th generator
17 concentrated solution enters the second generator 4 through the second solution heat exchanger 11, flows through the refrigerant vapour heat release of the 4th generator 17
Enter condenser 5 through the throttling of third throttle valve 18 at after cryogen liquid, the cryogen liquid heat release for flowing through the 4th generator 17 cools down it
Enter condenser 5 by the throttling of second throttle 14, forms combined cycle energy supplying system.
Combined cycle energy supplying system shown in Figure 27 is achieved in that
(1) in structure, in the combined cycle energy supplying system shown in Figure 23, increase the 4th generator, third throttle valve, the 4th
Second absorber 2 is had weak solution pipeline to hand over through the second solution pump 9 and the second solution heat by solution pump and the 4th solution heat exchanger
Parallel operation 11 is connected to third generator 13 to be adjusted to the second absorber 2 and has weak solution pipeline through the second solution pump 9 and the second solution
Heat exchanger 11 is connected to the 4th generator 17, and the 4th generator 17 has concentrated solution pipeline molten through the 4th solution pump 19 and the 4th again
Liquid heat exchanger 20 is connected to third generator 13, has concentrated solution pipeline through third solution heat exchanger 16 and in generator 3
Two solution heat exchangers 11 are connected to the second generator 4 to be adjusted to generator 3 and has concentrated solution pipeline through third solution heat exchanger
16, the 4th solution heat exchanger 20 and the second solution heat exchanger 11 are connected to the second generator 4, third generator 13 are had cold
Agent steam channel is connected to condenser 5 to be adjusted to after third generator 13 has refrigerant steam channel to be connected to the 4th generator 17
4th generator 17 has cryogen liquid pipeline to be connected to through third throttle valve 18 with condenser 5 again, and there are also cryogens to steam for the 4th generator 17
Vapour channel is connected to condenser 5.
(2) in process, the refrigerant vapour that third generator 13 generates is supplied to the 4th generator 17 and makees driving thermal medium, the
The weak solution of two absorbers 2 enters the 4th generator 17, refrigerant vapour stream through the second solution pump 9 and the second solution heat exchanger 11
Through the 4th generator 17, heating enter its in solution release refrigerant vapour and to condenser 5 provide, the 4th generator 17 it is dense
Solution enters third generator 13 through the 4th solution pump 19 and the 4th solution heat exchanger 20, and the concentrated solution of third generator 13 passes through
Third solution pump 15 and third solution heat exchanger 16 enter generator 3, and the concentrated solution of generator 3 is through third solution heat exchanger
16, the 4th solution heat exchanger 20 and the second solution heat exchanger 11 enter the second generator 4, flow through the cold of the 4th generator 17
The heat release of agent steam enters condenser 5 through the throttling of third throttle valve 18 at after cryogen liquid, forms combined cycle energy supplying system.
Combined cycle energy supplying system shown in Figure 28 is achieved in that
(1) in structure, in combined cycle energy supplying system shown in Fig. 1, increase third generator, third solution pump, third
Second generator 4 is had mixed-gas channel to be connected to outside and is adjusted to the second generation by solution heat exchanger and third absorber
Third generator 13 has mixed-gas channel to connect with outside again after device 4 has mixed-gas channel to be connected to third generator 13
It is logical, there is refrigerant steam channel be connected to absorber 1 evaporator 6 and is adjusted to evaporator 6 and has refrigerant steam channel and third absorption
Device 21 is connected to, and there are also weak solution pipelines through third solution pump 15 and third solution heat exchanger 16 and third hair for third absorber 21
Raw device 13 is connected to, and third generator 13 is connected to through third solution heat exchanger 16 with third absorber 21 there are also concentrated solution pipeline,
Third generator 13 is connected to there are also refrigerant steam channel with absorber 1, and third absorber 21 is there are also heated medium pipeline and outside
Portion's connection.
(2) in process, the mixed gas of waste heat boiler E discharge is followed by generator 3, the second generator 4 and third hair
Raw device 13 and gradually heat release, the refrigerant vapour that evaporator 6 generates enter third absorber 21, the weak solution warp of third absorber 21
Third solution pump 15 and third solution heat exchanger 16 enter third generator 13, heat absorption release refrigerant vapour and to absorber 1
It provides, the concentrated solution of third generator 13 enters third absorber 21 through third solution heat exchanger 16, absorbs refrigerant vapour simultaneously
Heat release forms combined cycle energy supplying system in heated medium.
Combined cycle energy supplying system shown in Figure 29 is achieved in that
(1) in structure, in combined cycle energy supplying system shown in Fig. 1, increase high-temperature heat exchanger and second circulation pump, it will
Second generator 4 has gaseous mixture again after waste heat boiler E has mixed-gas channel to be sequentially communicated generator 3 and the second generator 4
Body channel be connected to outside be adjusted to waste heat boiler E and there is mixed-gas channel be connected to high-temperature heat exchanger Q after height warm friendship
Parallel operation Q has mixed-gas channel be connected to outside again, and the is relied between high-temperature heat exchanger Q, generator 3 and the second generator 4
Two circulating pump R and circulating thermal medium pipeline constitute closed loop.
(2) in process, the mixed gas of waste heat boiler E discharge flows through high temperature heater (HTH) Q and heat release in circulating thermal medium, follows
Hair is supplied to after ring thermal medium flows through high-temperature heat exchanger Q after second circulation pump R pressurization, heat absorption heats up or heat absorption vaporization
Raw device 3 and the second generator 4 make driving thermal medium;Circulating thermal medium flows through generator 3 and the second generator 4 and heat release, then passes through
The backward high temperature heater (HTH) Q that second circulation pumps R pressurization is provided, and forms combined cycle energy supplying system.
Combined cycle energy supplying system shown in Figure 30 is achieved in that
(1) in structure, in combined cycle energy supplying system shown in Fig. 1, increase high-temperature heat exchanger, second circulation pump, the
Three generators, third solution pump, third solution heat exchanger and third absorber, by waste heat boiler E have mixed-gas channel according to
Second generator 4 has mixed-gas channel to be adjusted to waste heat with external be connected to again after secondary connection generator 3 and the second generator 4
High-temperature heat exchanger Q has mixed-gas channel and outside again after boiler E has mixed-gas channel to be connected to high-temperature heat exchanger Q
Connection, by second circulation pump R and circulation between high-temperature heat exchanger Q, generator 3, the second generator 4 and third generator 13
Heat medium pipeline constitutes closed loop;There is refrigerant steam channel to be connected to absorber 1 evaporator 6 and is adjusted to evaporator 6
There is refrigerant steam channel to be connected to third absorber 21, there are also weak solution pipelines through third solution pump 15 and for third absorber 21
Three solution heat exchangers 16 are connected to third generator 13, and there are also concentrated solution pipelines through third solution heat exchange for third generator 13
Device 16 is connected to third absorber 21, and third generator 13 is connected to there are also refrigerant steam channel with absorber 1, third absorber 21
There are also heated medium pipelines to be connected to outside.
(2) in process, the mixed gas of waste heat boiler E discharge flows through high-temperature heat exchanger Q and heat release in circulating thermal medium,
It is supplied to after circulating thermal medium flows through high-temperature heat exchanger Q after second circulation pump R pressurization, heat absorption heats up or heat absorption vaporization
Generator 3, the second generator 4 and the second generator 13 make driving thermal medium;Circulating thermal medium flows through the generation of generator 3, second
Device 4 and third generator 13 and gradually heat release, then the backward high-temperature heat exchanger Q through second circulation pump R pressurization are provided, and form connection
Close circulation energy supplying system.
Combined cycle energy supplying system shown in Figure 31 is achieved in that
(1) in structure, in combined cycle energy supplying system shown in Fig. 1, increase second heat exchanger, fuel and air are led to
Road is changed to high temperature heat source medium channel, and cancelling boiler B has blast tube to be connected to waste heat boiler E, and it is free to cancel air turbine C
Gas channel is connected to waste heat boiler E, and cancelling waste heat boiler E has mixed-gas channel to be sequentially communicated generator 3 and the second generator 4
The second generator 4 has mixed-gas channel to be connected to outside again later;Boiler B have low-temperature heat source medium channel through waste heat boiler E,
Generator 3, the second generator 4, second heat exchanger 12, evaporator 6 and low temperature heat exchanger J are connected to outside, air turbine C
There is air duct through waste heat boiler E, generator 3, the second generator 4, second heat exchanger 12, evaporator 6 and low temperature heat exchange
Device J is connected to outside.
(2) in process, high temperature heat source medium provides thermic load to compressed air by boiler B, and waste heat boiler E is discharged low
Temperature-heat-source medium followed by generator 3, the second generator 4, second heat exchanger 12, evaporator 6 and low temperature heat exchanger J simultaneously
Gradually heat release cools down, and the air of air turbine C discharge is followed by generator 3, the second generator 4, second heat exchanger 12, steaming
Send out device 6 and low temperature heat exchanger J and gradually heat release cool down, air-steam forward circulation respectively to working machine S offer power, to
Compression reverse circulation provide power and to absorption reverse circulation provide driving thermic load, formed simultaneously provide heat demand with
The combined cycle energy supplying system of power demand.
The effect that the technology of the present invention may be implemented --- combined cycle energy supplying system proposed by the invention has following effect
Fruit and advantage:
(1) different fuel or heat source medium are adapted to, and realizes efficient heat supply and highly effective refrigeration.
(2) it can preferably realize the utilization to such as low ambient temperature thermal resource, realize energy saving heating.
(3) high temperature heat of combustion gas is subject to benefit by air-steam forward circulation device and compression reverse circulation device
With promoting Low Temperature Thermal load temperature or externally provide power simultaneously, the high temperature section temperature difference rationally utilized, and irreversible damage is reduced
It loses.
(4) waste heat gas load is used by absorption reverse circulation device, obtains or further promoted Low Temperature Thermal
Load temperature realizes the reasonable utilization of the temperature difference, reduces irreversible loss.
(5) second generators and the second absorber combine, and realize the efficient and deep exploitation of gas thermal energy.
(6) a variety of specific technical solutions are provided, numerous different actual states is coped with, there is the wider scope of application.
(7) air-steam combined cycle, compression reverse circulation are played and absorbs the respective advantage of reverse circulation, it can
Farthest realize the efficient utilization of thermal energy.
Claims (41)
1. combined cycle energy supplying system, mainly by turbine, boiler, heat exchanger, circulating pump, compressor, cryogenic throttle valve, low
Temperature heat exchanger, absorber, the second absorber, generator, the second generator, condenser, evaporator, throttle valve, solution pump,
Two solution pumps, solution heat exchanger and the second solution heat exchanger are formed;Turbine (A) has low-pressure steam channel and heat exchange
Device (C) connection, heat exchanger (C) are connected to through circulating pump (D) with boiler (B) there are also condensate liquid pipeline, and there are also high pressures to steam for boiler (B)
Vapour channel is connected to turbine (A), boiler (B) have fuel and air channel with outside be connected to, boiler (B) also blast tube according to
The second generator (4) has blast tube to be connected to outside again after secondary connection generator (3) and the second generator (4);Compressor
(E) finisher (6) for thering is refrigerant steam channel to be connected to evaporator (6) have again cryogen liquid pipeline through cryogenic throttle valve (F) with
Low temperature heat exchanger (G) connection, low temperature heat exchanger (G) are connected to there are also refrigerant steam channel with compressor (E), low temperature heat exchange
Device (G) also cryogenic media pipeline is connected to outside;Evaporator (6) is connected to there are also refrigerant steam channel with absorber (1), is absorbed
Device (1) is connected to through solution pump (8) and solution heat exchanger (10) with the second absorber (2) there are also weak solution pipeline, and second absorbs
Device (2) is connected to through the second solution pump (9) and the second solution heat exchanger (11) with generator (3) there are also weak solution pipeline, is occurred
Device (3) is connected to through the second solution heat exchanger (11) with the second generator (4) there are also concentrated solution pipeline, and the second generator (4) is also
There is concentrated solution pipeline to be connected to through solution heat exchanger (10) with absorber (1), there are also refrigerant steam channels and condensation for generator (3)
Device (5) connection, the second generator (4) are connected to there are also refrigerant steam channel with the second absorber (2), and there are also cryogens for condenser (5)
Liquid pipeline is connected to through throttle valve (7) with evaporator (6), absorber (1), the second absorber (2) and condenser (5) also have respectively by
Heat medium pipeline is connected to outside;Turbine, boiler, heat exchanger and circulating pump constitute Steam Power Equipment forward circulation system
System, compressor, evaporator, cryogenic throttle valve and low temperature heat exchanger constitute compression reverse circulation system, and absorber, second inhale
Receive device, generator, the second generator, condenser, evaporator, throttle valve, solution pump, the second solution pump, solution heat exchanger and
Second solution heat exchanger constitutes absorption reverse circulation system;Steam Power Equipment forward circulation is mentioned to compression reverse circulation
Power is externally provided for power or simultaneously, Steam Power Equipment forward circulation provides driving thermic load to absorption reverse circulation,
Compression reverse circulation obtains low temperature thermic load and by evaporator to absorption reverse circulation heat supply, and absorption reverse circulation is logical
Absorber, the second absorber and the external heat supply of condenser are crossed, combined cycle energy supplying system is formed.
2. combined cycle energy supplying system is to increase by the second compressor in combined cycle energy supplying system described in claim 1,
There is cryogen liquid pipeline to throttle through low temperature again the finisher (6) that compressor (E) has refrigerant steam channel to be connected to evaporator (6)
Valve (F) be connected to low temperature heat exchanger (G) be adjusted to compressor (E) have refrigerant steam channel be connected to evaporator (6) after steam
Hair device (6) has refrigerant steam channel to be connected to the second compressor (H) again, and the second compressor (H) is there are also refrigerant steam channel and steams
The finisher (6) of hair device (6) connection has cryogen liquid pipeline to be connected to through cryogenic throttle valve (F) with low temperature heat exchanger (G) again, shape
At combined cycle energy supplying system.
3. combined cycle energy supplying system, mainly by turbine, boiler, heat exchanger, circulating pump, compressor, the second condenser, low
Warm throttle valve, low temperature heat exchanger, absorber, the second absorber, generator, the second generator, condenser, evaporator, throttling
Valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger are formed;Turbine (A) has low-pressure steam
Channel is connected to heat exchanger (C), and heat exchanger (C) is connected to through circulating pump (D) with boiler (B) there are also condensate liquid pipeline, boiler
(B) it is connected to there are also high steam channel with turbine (A), boiler (B) has fuel and air channel to be connected to outside, boiler (B)
Be sequentially communicated the second generator (4) after generator (3) and the second generator (4) there are also blast tube has blast tube and outer again
Portion's connection;The second condenser (I) has cryogen liquid again after compressor (E) has refrigerant steam channel to be connected to the second condenser (I)
Pipeline is connected to through cryogenic throttle valve (F) with low temperature heat exchanger (G), and there are also refrigerant steam channels and pressure for low temperature heat exchanger (G)
Contracting machine (E) connection, low temperature heat exchanger (G) also cryogenic media pipeline are connected to outside, and the second condenser (I) is also heated
Medium pipeline is connected to outside;Evaporator (6) has refrigerant steam channel to be connected to absorber (1), and there are also weak solutions for absorber (1)
Pipeline is connected to through solution pump (8) and solution heat exchanger (10) with the second absorber (2), and there are also weak solutions for the second absorber (2)
Pipeline is connected to through the second solution pump (9) and the second solution heat exchanger (11) with generator (3), and there are also concentrated solutions for generator (3)
Pipeline is connected to through the second solution heat exchanger (11) with the second generator (4), and there are also concentrated solution pipelines through molten for the second generator (4)
Liquid heat exchanger (10) is connected to absorber (1), and generator (3) is connected to there are also refrigerant steam channel with condenser (5), the second hair
Raw device (4) are connected to there are also refrigerant steam channel with the second absorber (2), and there are also cryogen liquid pipelines through throttle valve (7) for condenser (5)
Be connected to evaporator (6), there are also cryogenic media pipelines to be connected to external for evaporator (6), absorber (1), the second absorber (2) and
Condenser (5) also has heated medium pipeline to be connected to outside respectively;Turbine, boiler, heat exchanger and circulating pump, which are constituted, to be steamed
Vapour power device forward circulation system, it is inverse that compressor, the second condenser, cryogenic throttle valve and low temperature heat exchanger constitute compression
To the circulatory system, absorber, the second absorber, generator, the second generator, condenser, evaporator, throttle valve, solution pump,
Two solution pumps, solution heat exchanger and the second solution heat exchanger constitute absorption reverse circulation system;Steam Power Equipment is just
Power is provided to circulation to compression reverse circulation or power is externally provided simultaneously, and Steam Power Equipment forward circulation is to absorption
Reverse circulation provides driving thermic load, and compression reverse circulation obtains low temperature thermic load and passes through the external heat supply of the second condenser,
Absorption reverse circulation obtains low temperature thermic load and by absorber, the second absorber and the external heat supply of condenser, forms joint
Recycle energy supplying system.
4. combined cycle energy supplying system is to increase by the second compressor in combined cycle energy supplying system as claimed in claim 3,
The second condenser (I) has cryogen liquid pipeline warp again after having refrigerant steam channel to be connected to the second condenser (I) on compressor (E)
Cryogenic throttle valve (F) is connected to low temperature heat exchanger (G) to be adjusted to compressor (E) and has refrigerant steam channel and the second condenser
(I) the second condenser (I) has refrigerant steam channel to be connected to the second compressor (H) again after being connected to, and the second compressor (H) is also
The second condenser (I) has cryogen liquid pipeline through cryogenic throttle valve (F) again after refrigerant steam channel is connected to the second condenser (I)
It is connected to low temperature heat exchanger (G), forms combined cycle energy supplying system.
5. combined cycle energy supplying system, mainly by turbine, boiler, heat exchanger, circulating pump, compressor, cooler, low temperature section
Flow valve, low temperature heat exchanger, absorber, the second absorber, generator, the second generator, condenser, evaporator, throttle valve, molten
Liquid pump, the second solution pump, solution heat exchanger and the second solution heat exchanger are formed;Turbine (A) has low-pressure steam channel
It is connected to heat exchanger (C), heat exchanger (C) is connected to through circulating pump (D) with boiler (B) there are also condensate liquid pipeline, and boiler (B) is also
There is high steam channel to be connected to turbine (A), boiler (B) has fuel and air channel to be connected to outside, and there are also fire for boiler (B)
The second generator (4) has blast tube to connect with outside again after gas channel is sequentially communicated generator (3) and the second generator (4)
It is logical;The aftercooler (J) that compressor (E) has refrigerant steam channel to be connected to cooler (J) has refrigerant steam channel and evaporation again
Device (6) connection, evaporator (6) are connected to through cryogenic throttle valve (F) with low temperature heat exchanger (G) there are also cryogen liquid pipeline, Low Temperature Thermal
Exchanger (G) is connected to there are also refrigerant steam channel with compressor (E), and low temperature heat exchanger (G) is there are also cryogenic media pipeline and outside
Portion's connection, cooler (J) also heated medium pipeline are connected to outside;Evaporator (6) is there are also refrigerant steam channel and absorbs
Device (1) connection, there are also weak solution pipelines through solution pump (8) and solution heat exchanger (10) and the second absorber (2) for absorber (1)
Connection, there are also weak solution pipelines through the second solution pump (9) and the second solution heat exchanger (11) and generator for the second absorber (2)
(3) it being connected to, generator (3) is connected to through the second solution heat exchanger (11) with the second generator (4) there are also concentrated solution pipeline, and second
Generator (4) is connected to through solution heat exchanger (10) with absorber (1) there are also concentrated solution pipeline, and there are also cryogens to steam for generator (3)
Vapour channel is connected to condenser (5), and the second generator (4) is connected to there are also refrigerant steam channel with the second absorber (2), condenser
(5) it is connected to through throttle valve (7) with evaporator (6) there are also cryogen liquid pipeline, absorber (1), the second absorber (2) and condenser
(5) heated medium pipeline also is connected to outside respectively;Turbine, boiler, heat exchanger and circulating pump constitute steam power
Device forward circulation system, it is reverse that compressor, cooler, evaporator, cryogenic throttle valve and low temperature heat exchanger constitute compression
The circulatory system, absorber, the second absorber, generator, the second generator, condenser, evaporator, throttle valve, solution pump, second
Solution pump, solution heat exchanger and the second solution heat exchanger constitute absorption reverse circulation system;Steam Power Equipment is positive
It recycles and provides power to compression reverse circulation or power is externally provided simultaneously, Steam Power Equipment forward circulation is to absorption inverse
To circulation offer driving thermic load, compression reverse circulation obtains low temperature thermic load and passes through the external heat supply of cooler respectively and lead to
For pervaporation device to absorption reverse circulation heat supply, absorption reverse circulation is external by absorber, the second absorber and condenser
Heat supply forms combined cycle energy supplying system.
6. combined cycle energy supplying system is to increase by the second compressor in the combined cycle energy supplying system described in claim 5,
The aftercooler (J) that compressor (E) has refrigerant steam channel to be connected to cooler (J) there are into refrigerant steam channel and evaporator again
(6) aftercooler (J) that connection is adjusted to compressor (E) and has refrigerant steam channel to be connected to cooler (J) has refrigerant vapour again
Channel is connected to the second compressor (H), and the second compressor (H) is cooling after being connected to there are also refrigerant steam channel with cooler (J)
Device (J) has refrigerant steam channel to be connected to evaporator (6) again, forms combined cycle energy supplying system.
7. combined cycle energy supplying system, mainly by turbine, boiler, heat exchanger, circulating pump, compressor, the second compressor,
Two condensers, cryogenic throttle valve, the second cryogenic throttle valve, low temperature heat exchanger, absorber, the second absorber, generator, second
Generator, condenser, evaporator, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger
It is formed;Turbine (A) has low-pressure steam channel to be connected to heat exchanger (C), and there are also condensate liquid pipelines through following for heat exchanger (C)
Ring pump (D) is connected to boiler (B), and boiler (B) is connected to there are also high steam channel with turbine (A), and boiler (B) has fuel and sky
Gas channel be connected to outside, and there are also blast tubes to be sequentially communicated generator (3) and the second generator (4) later second for boiler (B)
Generator (4) has blast tube to be connected to outside again;Compressor (E) has low pressure refrigerant steam channel to be connected to evaporator (6), steams
Low temperature heat exchanger after hair device (6) is connected to through cryogenic throttle valve (F) with low temperature heat exchanger (G) there are also low pressure cryogen liquid pipeline
(G) refrigerant steam channel is connected to compressor (E) again, there are also low pressure refrigerant steam channel and the second compressors for compressor (E)
(H) it is connected to, the second compressor (H) is connected to there are also high pressure refrigerant steam channel with the second condenser (I), and the second condenser (I) is also
Low Temperature Thermal after thering is high pressure cryogen liquid pipeline to be connected to through evaporator (6) and the second cryogenic throttle valve (K) with low temperature heat exchanger (G)
Exchanger (G) has refrigerant steam channel to be connected to compressor (E) again, and low temperature heat exchanger (G) is there are also cryogenic media pipeline and outside
Portion's connection, the second condenser (I) also heated medium pipeline are connected to outside;Evaporator (6) there are also refrigerant steam channel with
Absorber (1) connection, there are also weak solution pipelines through solution pump (8) and solution heat exchanger (10) and the second absorption for absorber (1)
Device (2) connection, the second absorber (2) there are also weak solution pipelines through the second solution pump (9) and the second solution heat exchanger (11) and
Generator (3) connection, generator (3) also concentrated solution pipeline connect through the second solution heat exchanger (11) and the second generator (4)
Logical, the second generator (4) is connected to through solution heat exchanger (10) with absorber (1) there are also concentrated solution pipeline, and generator (3) is also
Refrigerant steam channel is connected to condenser (5), and the second generator (4) is connected to there are also refrigerant steam channel with the second absorber (2),
Condenser (5) is connected to there are also cryogen liquid pipeline with evaporator (6) through throttle valve (7), absorber (1), the second absorber (2) and cold
Condenser (5) also has heated medium pipeline to be connected to outside respectively;Turbine, boiler, heat exchanger and circulating pump constitute steam
Power device forward circulation system, compressor, the second compressor, the second condenser, evaporator, cryogenic throttle valve, the second low temperature
Throttle valve and low temperature heat exchanger constitute compression reverse circulation system, and absorber, the second absorber, generator, second occur
Device, condenser, evaporator, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger are constituted
Absorption reverse circulation system;Steam Power Equipment forward circulation provides power to compression reverse circulation or externally provides simultaneously
Power, Steam Power Equipment forward circulation provide driving thermic load to absorption reverse circulation, and compression reverse circulation obtains low
Warm load simultaneously passes through the external heat supply of the second condenser and by evaporator to absorption reverse circulation heat supply respectively, absorption inverse
To absorber, the second absorber and the external heat supply of condenser is cycled through, combined cycle energy supplying system is formed.
8. combined cycle energy supplying system, mainly by turbine, boiler, heat exchanger, circulating pump, compressor, the second condenser, low
Warm throttle valve, the second cryogenic throttle valve, low temperature heat exchanger, absorber, the second absorber, generator, the second generator, condensation
Device, evaporator, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger are formed;Turbine
Machine (A) has low-pressure steam channel to be connected to heat exchanger (C), and there are also condensate liquid pipelines through circulating pump (D) and pot for heat exchanger (C)
Furnace (B) connection, boiler (B) be connected tos there are also high steam channel with turbine (A), boiler (B) have fuel and air channel with outside
Portion's connection, boiler (B) there are also blast tube is sequentially communicated generator (3) and the second generator (4), and the second generator (4) is again later
There is blast tube to be connected to outside;Compressor (E) has low pressure refrigerant steam channel to be connected to evaporator (6), and evaporator (6) is also
Low temperature heat exchanger (G) has cryogen again after low pressure cryogen liquid pipeline is connected to through cryogenic throttle valve (F) with low temperature heat exchanger (G)
Steam channel is connected to compressor (E), and compressor (E) is connected to there are also high pressure refrigerant steam channel with the second condenser (I), and second
Condenser (I) also high pressure cryogen liquid pipeline connects through evaporator (6) and the second cryogenic throttle valve (K) and low temperature heat exchanger (G)
Low temperature heat exchanger (G) has refrigerant steam channel to be connected to compressor (E) again after logical, and there are also low temperature for low temperature heat exchanger (G)
Medium pipeline is connected to outside, and the second condenser (I) also heated medium pipeline is connected to outside;There are also cold for evaporator (6)
Agent steam channel is connected to absorber (1), and there are also weak solution pipelines through solution pump (8) and solution heat exchanger for absorber (1)
(10) it is connected to the second absorber (2), there are also weak solution pipelines through the second solution pump (9) and the second solution for the second absorber (2)
Heat exchanger (11) is connected to generator (3), and there are also concentrated solution pipelines through the second solution heat exchanger (11) and for generator (3)
Two generators (4) connection, the second generator (4) are connected to through solution heat exchanger (10) with absorber (1) there are also concentrated solution pipeline,
Generator (3) is connected to there are also refrigerant steam channel with condenser (5), and there are also refrigerant steam channels and second for the second generator (4)
Absorber (2) connection, condenser (5) are connected to there are also cryogen liquid pipeline with evaporator (6) through throttle valve (7), absorber (1), the
Two absorbers (2) and condenser (5) also have heated medium pipeline to be connected to outside respectively;Turbine, boiler, heat exchanger and
Circulating pump constitutes Steam Power Equipment forward circulation system, compressor, the second condenser, evaporator, cryogenic throttle valve, second low
Warm throttle valve and low temperature heat exchanger constitute compression reverse circulation system, absorber, the second absorber, generator, the second hair
Raw device, condenser, evaporator, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger structure
At absorption reverse circulation system;Steam Power Equipment forward circulation provides power to compression reverse circulation or externally mentions simultaneously
For power, Steam Power Equipment forward circulation provides driving thermic load to absorption reverse circulation, and compression reverse circulation obtains
Low temperature thermic load simultaneously passes through the external heat supply of the second condenser and by evaporator to absorption reverse circulation heat supply respectively, absorption
Reverse circulation forms combined cycle energy supplying system by absorber, the second absorber and the external heat supply of condenser.
9. combined cycle energy supplying system, mainly by turbine, boiler, heat exchanger, circulating pump, compressor, expanding machine, evaporation
Device, low temperature heat exchanger, absorber, the second absorber, generator, the second generator, condenser, throttle valve, solution pump, second
Solution pump, solution heat exchanger and the second solution heat exchanger are formed;Turbine (A) has low-pressure steam channel and heat exchanger
(C) it is connected to, heat exchanger (C) is connected to through circulating pump (D) with boiler (B) there are also condensate liquid pipeline, and there are also high steams for boiler (B)
Channel is connected to turbine (A), and boiler (B) has fuel and air channel to be connected to outside, and there are also blast tubes for boiler (B) successively
The second generator (4) has blast tube to be connected to outside again after connection generator (3) and the second generator (4);Compressor (E)
The finisher (6) for having refrigerant gas channel to be connected to evaporator (6) has refrigerant gas channel to be connected to expanding machine (L) again, swollen
Swollen machine (L) is connected to through low temperature heat exchanger (G) with compressor (E) there are also refrigerant gas channel, and there are also low for low temperature heat exchanger (G)
Warm medium pipeline is connected to outside;Evaporator (6) is connected to there are also refrigerant steam channel with absorber (1), and there are also dilute for absorber (1)
Solution line is connected to through solution pump (8) and solution heat exchanger (10) with the second absorber (2), and there are also dilute for the second absorber (2)
Solution line is connected to through the second solution pump (9) and the second solution heat exchanger (11) with generator (3), and there are also dense for generator (3)
Solution line is connected to through the second solution heat exchanger (11) with the second generator (4), and there are also concentrated solution pipelines for the second generator (4)
It being connected to through solution heat exchanger (10) with absorber (1), generator (3) is connected to there are also refrigerant steam channel with condenser (5), the
Two generators (4) are connected to there are also refrigerant steam channel with the second absorber (2), and there are also cryogen liquid pipelines through throttling for condenser (5)
Valve (7) is connected to evaporator (6), and absorber (1), the second absorber (2) and condenser (5) also have heated medium pipeline respectively
It is connected to outside;Turbine, boiler, heat exchanger and circulating pump constitute Steam Power Equipment forward circulation system, compressor, steaming
It sends out device, expanding machine and low temperature heat exchanger and constitutes compression reverse circulation system, absorber, the second absorber, generator, second
Generator, condenser, evaporator, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger
Constitute absorption reverse circulation system;Steam Power Equipment forward circulation to compression reverse circulation provide power or simultaneously externally
Power is provided, Steam Power Equipment forward circulation provides driving thermic load to absorption reverse circulation, and compression reverse circulation obtains
Take low temperature thermic load and by evaporator to absorption reverse circulation heat supply, absorption reverse circulation is inhaled by absorber, second
Device and the external heat supply of condenser are received, combined cycle energy supplying system is formed.
10. combined cycle energy supplying system is to increase by the second compressor in combined cycle energy supplying system as claimed in claim 9,
The finisher (6) that compressor (E) has refrigerant gas channel to be connected to evaporator (6) there are into refrigerant gas channel and expanding machine again
(L) finisher (6) that connection is adjusted to compressor (E) and has refrigerant gas channel to be connected to evaporator (6) has refrigerant gas again
Channel is connected to the second compressor (H), and the second compressor (H) evaporates after being connected to there are also refrigerant gas channel with evaporator (6)
Device (6) has refrigerant gas channel to be connected to expanding machine (L) again, forms combined cycle energy supplying system.
11. combined cycle energy supplying system, mainly by turbine, boiler, heat exchanger, circulating pump, compressor, evaporator, expansion
Machine, low temperature heat exchanger, regenerator, absorber, the second absorber, generator, the second generator, condenser, throttle valve, solution
Pump, the second solution pump, solution heat exchanger and the second solution heat exchanger are formed;Turbine (A) have low-pressure steam channel with
Heat exchanger (C) connection, heat exchanger (C) are connected to through circulating pump (D) with boiler (B) there are also condensate liquid pipeline, and boiler (B) is also
High steam channel is connected to turbine (A), and boiler (B) has fuel and air channel to be connected to outside, and there are also combustion gas for boiler (B)
The second generator (4) has blast tube to be connected to outside again after channel is sequentially communicated generator (3) and the second generator (4);
The finisher (6) that compressor (E) has refrigerant gas channel to be connected to evaporator (6) has refrigerant gas channel through regenerator again
(M) it is connected to expanding machine (L), there are also refrigerant gas channels through low temperature heat exchanger (G) and regenerator (M) and pressure for expanding machine (L)
Contracting machine (E) connection, low temperature heat exchanger (G) also cryogenic media pipeline are connected to outside;There are also refrigerant vapours to lead to for evaporator (6)
Road is connected to absorber (1), and there are also weak solution pipelines through solution pump (8) and solution heat exchanger (10) and second for absorber (1)
Absorber (2) connection, there are also weak solution pipelines through the second solution pump (9) and the second solution heat exchanger for the second absorber (2)
(11) it is connected to generator (3), there are also concentrated solution pipelines through the second solution heat exchanger (11) and the second generator for generator (3)
(4) it is connected to, the second generator (4) is connected to through solution heat exchanger (10) with absorber (1) there are also concentrated solution pipeline, generator
(3) it is connected to there are also refrigerant steam channel with condenser (5), there are also refrigerant steam channel and the second absorbers for the second generator (4)
(2) it is connected to, condenser (5) is connected to through throttle valve (7) with evaporator (6) there are also cryogen liquid pipeline, and absorber (1), second absorb
Device (2) and condenser (5) also have heated medium pipeline to be connected to outside respectively;Turbine, boiler, heat exchanger and circulating pump
Steam Power Equipment forward circulation system is constituted, compressor, evaporator, expanding machine, low temperature heat exchanger and regenerator constitute pressure
Contracting formula reverse circulation system, it is absorber, the second absorber, generator, the second generator, condenser, evaporator, throttle valve, molten
Liquid pump, the second solution pump, solution heat exchanger and the second solution heat exchanger constitute absorption reverse circulation system;Steam power
Device forward circulation to compression reverse circulation provide power or simultaneously externally provide power, Steam Power Equipment forward circulation to
Absorption reverse circulation provides driving thermic load, and compression reverse circulation obtains low temperature thermic load and by evaporator to absorption
Reverse circulation heat supply, absorption reverse circulation form combined cycle by absorber, the second absorber and the external heat supply of condenser
Energy supplying system.
12. combined cycle energy supplying system is to increase by the second compression in the combined cycle energy supplying system described in claim 11
The finisher (6) that compressor (E) has refrigerant gas channel to be connected to evaporator (6) is had refrigerant gas channel to pass through back by machine again
Hot device (M) be connected to expanding machine (L) be adjusted to compressor (E) have refrigerant gas channel be connected to logical evaporator (6) after evaporate
Device (6) has refrigerant gas channel to be connected to the second compressor (H) again, and there are also refrigerant gas channels and evaporation for the second compressor (H)
The finisher (6) of device (6) connection has refrigerant gas channel to be connected to through regenerator (M) with expanding machine (L) again, forms combined cycle
Energy supplying system.
13. combined cycle energy supplying system, mainly by turbine, boiler, heat exchanger, circulating pump, compressor, expanding machine, cooling
Device, low temperature heat exchanger, evaporator, absorber, the second absorber, generator, the second generator, condenser, throttle valve, solution
Pump, the second solution pump, solution heat exchanger and the second solution heat exchanger are formed;Turbine (A) have low-pressure steam channel with
Heat exchanger (C) connection, heat exchanger (C) are connected to through circulating pump (D) with boiler (B) there are also condensate liquid pipeline, and boiler (B) is also
High steam channel is connected to turbine (A), and boiler (B) has fuel and air channel to be connected to outside, and there are also combustion gas for boiler (B)
The second generator (4) has blast tube to be connected to outside again after channel is sequentially communicated generator (3) and the second generator (4);
Compressor (E) has refrigerant gas channel to be connected to through cooler (J) with expanding machine (L), and there are also refrigerant gas channels to pass through for expanding machine (L)
Low temperature heat exchanger (G) is connected to compressor (E), and low temperature heat exchanger (G) also cryogenic media pipeline is connected to outside, cooling
Device (J) also heated medium pipeline is connected to outside;Evaporator (6) has refrigerant steam channel to be connected to absorber (1), absorbs
Device (1) is connected to through solution pump (8) and solution heat exchanger (10) with the second absorber (2) there are also weak solution pipeline, and second absorbs
Device (2) is connected to through the second solution pump (9) and the second solution heat exchanger (11) with generator (3) there are also weak solution pipeline, is occurred
Device (3) is connected to through the second solution heat exchanger (11) with the second generator (4) there are also concentrated solution pipeline, and the second generator (4) is also
There is concentrated solution pipeline to be connected to through solution heat exchanger (10) with absorber (1), there are also refrigerant steam channels and condensation for generator (3)
Device (5) connection, the second generator (4) are connected to there are also refrigerant steam channel with the second absorber (2), and there are also cryogens for condenser (5)
Liquid pipeline is connected to through throttle valve (7) with evaporator (6), and evaporator (6) also cryogenic media pipeline is connected to outside, absorber
(1), the second absorber (2) and condenser (5) also have heated medium pipeline to be connected to outside respectively;Turbine, boiler, heat are handed over
Parallel operation and circulating pump constitute Steam Power Equipment forward circulation system, compressor, cooler, expanding machine and low temperature heat exchanger structure
At compression reverse circulation system, absorber, the second absorber, generator, the second generator, condenser, evaporator, throttling
Valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger constitute the absorption reverse circulation system of row;
Steam Power Equipment forward circulation provides power to compression reverse circulation or externally provides power simultaneously, and Steam Power Equipment is just
Driving thermic load is provided to circulation to absorption reverse circulation, compression reverse circulation obtains low temperature thermic load and passes through cooler
External heat supply, absorption reverse circulation obtain low temperature thermic load and pass through absorber, the second absorber and the external heat supply of condenser,
Form combined cycle energy supplying system.
14. combined cycle energy supplying system is to increase by the second compression in the combined cycle energy supplying system described in claim 13
Compressor (E) is had refrigerant gas channel to be connected to expanding machine (L) through cooler (J) and is adjusted to compressor (E) and has cryogen gas by machine
Body channel is connected to through cooler (J) with the second compressor (H), and there are also refrigerant gas channels through cooler (J) for the second compressor (H)
It is connected to expanding machine (L), forms combined cycle energy supplying system.
15. combined cycle energy supplying system, mainly by turbine, boiler, heat exchanger, circulating pump, compressor, cooler, expansion
Machine, low temperature heat exchanger, regenerator, evaporator, absorber, the second absorber, generator, the second generator, condenser, throttling
Valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger are formed;Turbine (A) has low-pressure steam
Channel is connected to heat exchanger (C), and heat exchanger (C) is connected to through circulating pump (D) with boiler (B) there are also condensate liquid pipeline, boiler
(B) it is connected to there are also high steam channel with turbine (A), boiler (B) has fuel and air channel to be connected to outside, boiler (B)
Be sequentially communicated the second generator (4) after generator (3) and the second generator (4) there are also blast tube has blast tube and outer again
Portion's connection;Compressor (E) has refrigerant gas channel to be connected to through cooler (J) and regenerator (M) with expanding machine (L), expanding machine (L)
There are also refrigerant gas channels to be connected to through low temperature heat exchanger (G) and regenerator (M) with compressor (E), and low temperature heat exchanger (G) is also
There is cryogenic media pipeline to be connected to outside, cooler (J) also heated medium pipeline is connected to outside;Evaporator (6) has cold
Agent steam channel is connected to absorber (1), and there are also weak solution pipelines through solution pump (8) and solution heat exchanger for absorber (1)
(10) it is connected to the second absorber (2), there are also weak solution pipelines through the second solution pump (9) and the second solution for the second absorber (2)
Heat exchanger (11) is connected to generator (3), and there are also concentrated solution pipelines through the second solution heat exchanger (11) and for generator (3)
Two generators (4) connection, the second generator (4) are connected to through solution heat exchanger (10) with absorber (1) there are also concentrated solution pipeline,
Generator (3) is connected to there are also refrigerant steam channel with condenser (5), and there are also refrigerant steam channels and second for the second generator (4)
Absorber (2) connection, condenser (5) are connected to through throttle valve (7) with evaporator (6) there are also cryogen liquid pipeline, and evaporator (6) is also
Cryogenic media pipeline is connected to outside, and absorber (1), the second absorber (2) and condenser (5) also have heated medium pipe respectively
Road is connected to outside;Turbine, boiler, heat exchanger and circulating pump composition Steam Power Equipment forward circulation system, compressor,
Cooler, expanding machine, low temperature heat exchanger and regenerator constitute compression reverse circulation system, absorber, the second absorber, hair
Raw device, the second generator, condenser, evaporator, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution
Heat exchanger constitutes absorption reverse circulation system;Steam Power Equipment forward circulation to compression reverse circulation provide power or
Power is externally provided simultaneously, and Steam Power Equipment forward circulation provides driving thermic load to absorption reverse circulation, and compression is inverse
Low temperature thermic load is obtained to circulation and passes through the external heat supply of cooler, and absorption reverse circulation obtains low temperature thermic load and simultaneously passes through suction
Device, the second absorber and the external heat supply of condenser are received, combined cycle energy supplying system is formed.
16. combined cycle energy supplying system is to increase by the second compression in the combined cycle energy supplying system described in claim 15
Compressor (E) is had refrigerant gas channel to be connected to through cooler (J) and regenerator (M) with expanding machine (L) and is adjusted to compressor by machine
(E) refrigerant gas channel is connected to through cooler (J) with the second compressor (H), the second compressor (H) has refrigerant gas channel again
It is connected to through cooler (J) and regenerator (M) with expanding machine (L), forms combined cycle energy supplying system.
17. combined cycle energy supplying system, mainly by turbine, boiler, heat exchanger, circulating pump, compressor, cooler, evaporation
Device, expanding machine, low temperature heat exchanger, absorber, the second absorber, generator, the second generator, condenser, throttle valve, solution
Pump, the second solution pump, solution heat exchanger and the second solution heat exchanger are formed;Turbine (A) have low-pressure steam channel with
Heat exchanger (C) connection, heat exchanger (C) are connected to through circulating pump (D) with boiler (B) there are also condensate liquid pipeline, and boiler (B) is also
High steam channel is connected to turbine (A), and boiler (B) has fuel and air channel to be connected to outside, and there are also combustion gas for boiler (B)
The second generator (4) has blast tube to be connected to outside again after channel is sequentially communicated generator (3) and the second generator (4);
The finisher (6) that compressor (E) has refrigerant gas channel to be connected to through cooler (J) with evaporator (6) has refrigerant gas logical again
Road is connected to expanding machine (L), and expanding machine (L) is connected to through low temperature heat exchanger (G) with compressor (E) there are also refrigerant gas channel,
Low temperature heat exchanger (G) also cryogenic media pipeline is connected to outside, and cooler (J) connects there are also heated medium pipeline with outside
It is logical;Evaporator (6) is connected to there are also refrigerant steam channel with absorber (1), and there are also weak solution pipelines through solution pump for absorber (1)
(8) it is connected to solution heat exchanger (10) with the second absorber (2), there are also weak solution pipeline is molten through second for the second absorber (2)
Liquid pump (9) and the second solution heat exchanger (11) are connected to generator (3), and there are also concentrated solution pipeline is molten through second for generator (3)
Liquid heat exchanger (11) is connected to the second generator (4), and there are also concentrated solution pipelines through solution heat exchanger for the second generator (4)
(10) it is connected to absorber (1), generator (3) is connected to there are also refrigerant steam channel with condenser (5), and the second generator (4) is also
There is refrigerant steam channel to be connected to the second absorber (2), there are also cryogen liquid pipelines through throttle valve (7) and evaporator for condenser (5)
(6) it is connected to, absorber (1), the second absorber (2) and condenser (5) also have heated medium pipeline to be connected to outside respectively;Whirlpool
Turbine, boiler, heat exchanger and circulating pump constitute Steam Power Equipment forward circulation system, compressor, cooler, evaporator,
Expanding machine and low temperature heat exchanger constitute compression reverse circulation system, and absorber, the second absorber, generator, second occur
Device, condenser, evaporator, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger are constituted
Absorption reverse circulation system;Steam Power Equipment forward circulation provides power to compression reverse circulation or externally provides simultaneously
Power, Steam Power Equipment forward circulation provide driving thermic load to absorption reverse circulation, and compression reverse circulation obtains low
Warm load simultaneously passes through the external heat supply of cooler and by evaporator to absorption reverse circulation heat supply respectively, absorption inversely to follow
Ring forms combined cycle energy supplying system by absorber, the second absorber and the external heat supply of condenser.
18. combined cycle energy supplying system is to increase by the second compression in the combined cycle energy supplying system described in claim 17
The finisher (6) that compressor (E) has refrigerant gas channel to be connected to through cooler (J) with evaporator (6) is had cryogen gas by machine again
Body channel is connected to expanding machine (L) to be adjusted to compressor (E) and has refrigerant gas channel to be connected to through cooler (J) with evaporator (6)
Finisher (6) there is refrigerant gas channel to be connected to the second compressor (H) again, there are also refrigerant gas is logical for the second compressor (H)
The finisher (6) that road is connected to through cooler (J) with evaporator (6) has refrigerant gas channel to be connected to expanding machine (L) again, is formed
Combined cycle energy supplying system.
19. combined cycle energy supplying system, mainly by turbine, boiler, heat exchanger, circulating pump, compressor, cooler, evaporation
Device, regenerator, expanding machine, low temperature heat exchanger, absorber, the second absorber, generator, the second generator, condenser, throttling
Valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger are formed;Turbine (A) has low-pressure steam
Channel is connected to heat exchanger (C), and heat exchanger (C) is connected to through circulating pump (D) with boiler (B) there are also condensate liquid pipeline, boiler
(B) it is connected to there are also high steam channel with turbine (A), boiler (B) has fuel and air channel to be connected to outside, boiler (B)
Be sequentially communicated the second generator (4) after generator (3) and the second generator (4) there are also blast tube has blast tube and outer again
Portion's connection;The finisher (6) that compressor (E) has refrigerant gas channel to be connected to through cooler (J) with evaporator (6) has cryogen again
Gas passage is connected to through regenerator (M) with expanding machine (L), and there are also refrigerant gas channels through low temperature heat exchanger (G) for expanding machine (L)
It is connected to regenerator (M) with compressor (E), low temperature heat exchanger (G) also cryogenic media pipeline is connected to outside, cooler
(J) there are also heated medium pipelines is connected to outside;Evaporator (6) is connected to there are also refrigerant steam channel with absorber (1), is absorbed
Device (1) is connected to through solution pump (8) and solution heat exchanger (10) with the second absorber (2) there are also weak solution pipeline, and second absorbs
Device (2) is connected to through the second solution pump (9) and the second solution heat exchanger (11) with generator (3) there are also weak solution pipeline, is occurred
Device (3) is connected to through the second solution heat exchanger (11) with the second generator (4) there are also concentrated solution pipeline, and the second generator (4) is also
There is concentrated solution pipeline to be connected to through solution heat exchanger (10) with absorber (1), there are also refrigerant steam channels and condensation for generator (3)
Device (5) connection, the second generator (4) are connected to there are also refrigerant steam channel with the second absorber (2), and there are also cryogens for condenser (5)
Liquid pipeline is connected to through throttle valve (7) with evaporator (6), absorber (1), the second absorber (2) and condenser (5) also have respectively by
Heat medium pipeline is connected to outside;Turbine, boiler, heat exchanger and circulating pump constitute Steam Power Equipment forward circulation system
System, compressor, cooler, evaporator, regenerator, expanding machine and low temperature heat exchanger constitute compression reverse circulation system, inhale
Receive device, the second absorber, generator, the second generator, condenser, evaporator, throttle valve, solution pump, the second solution pump, solution
Heat exchanger and the second solution heat exchanger constitute absorption reverse circulation system;Steam Power Equipment forward circulation is to compression
Reverse circulation provides power or externally provides power simultaneously, and Steam Power Equipment forward circulation provides drive to absorption reverse circulation
Dynamic thermic load, compression reverse circulation obtain low temperature thermic load and pass through the external heat supply of cooler respectively and pass through evaporator to suction
Receipts formula reverse circulation heat supply, absorption reverse circulation form joint by absorber, the second absorber and the external heat supply of condenser
Recycle energy supplying system.
20. combined cycle energy supplying system is to increase by the second compression in the combined cycle energy supplying system described in claim 19
The finisher (6) that compressor (E) has refrigerant gas channel to be connected to through cooler (J) with evaporator (6) is had cryogen gas by machine again
Body channel be connected to through regenerator (M) with expanding machine (L) be adjusted to compressor (E) have refrigerant gas channel through cooler (J) and steam
The finisher (6) of hair device (6) connection has refrigerant gas channel to be connected to the second compressor (H) again, and the second compressor (H) is also
The finisher (6) that refrigerant gas channel is connected to through cooler (J) with evaporator (6) has refrigerant gas channel through regenerator again
(M) it is connected to expanding machine (L), forms combined cycle energy supplying system.
21. combined cycle energy supplying system is to increase third in any combined cycle energy supplying system described in claim 1-20
Generator, second throttle, third solution pump and third solution heat exchanger, the second absorber (2) add weak solution pipeline warp
Third solution pump (15) and third solution heat exchanger (16) are connected to third generator (13), and there are also dense for third generator (13)
Solution line is connected to through third solution heat exchanger (16) with the second generator (4), by generator (3) have refrigerant steam channel with
Third generator after condenser (5) connection is adjusted to generator (3) and has refrigerant steam channel to be connected to third generator (13)
(13) cryogen liquid pipeline is connected to through second throttle (14) with condenser (5) again, there are also refrigerant vapours for third generator (13)
Channel is connected to condenser (5), forms combined cycle energy supplying system.
22. combined cycle energy supplying system is to increase third in any combined cycle energy supplying system described in claim 1-20
Second absorber (2) is had weak solution pipeline through the second solution pump by generator, second throttle and third solution heat exchanger
(9) it is connected to generator (3) with the second solution heat exchanger (11) and is adjusted to the second absorber (2) and has weak solution pipeline through second
Solution pump (9), the second solution heat exchanger (11) and third solution heat exchanger (16) are connected to generator (3), by generator
(3) have concentrated solution pipeline be connected to through the second solution heat exchanger (11) with the second generator (4) be adjusted to generator (3) have it is dense molten
Liquid pipeline is connected to through third solution heat exchanger (16) with third generator (13), and third generator (13) has concentrated solution pipeline again
It is connected to through the second solution heat exchanger (11) with the second generator (4), generator (3) is had into refrigerant steam channel and condenser
(5) third generator (13) is again after connection is adjusted to generator (3) and has refrigerant steam channel to be connected to third generator (13)
There is cryogen liquid pipeline to be connected to through second throttle (14) with condenser (5), third generator (13) there are also refrigerant steam channel with
Condenser (5) connection, forms combined cycle energy supplying system.
23. combined cycle energy supplying system is to increase third in any combined cycle energy supplying system described in claim 1-20
Second absorber (2) is had weak solution pipeline warp by generator, second throttle, third solution pump and third solution heat exchanger
Second solution pump (9) and the second solution heat exchanger (11) are connected to generator (3) to be adjusted to the second absorber (2) and has weak solution
Pipeline is connected to through the second solution pump (9) and the second solution heat exchanger (11) with third generator (13), third generator (13)
There is concentrated solution pipeline to be connected to through third solution pump (15) and third solution heat exchanger (16) with generator (3) again, by generator
(3) have concentrated solution pipeline be connected to through the second solution heat exchanger (11) with the second generator (4) be adjusted to generator (3) have it is dense molten
Liquid pipeline is connected to through third solution heat exchanger (16) and the second solution heat exchanger (11) with the second generator (4), will be occurred
Device (3) has refrigerant steam channel to be connected to condenser (5) to be adjusted to generator (3) and have refrigerant steam channel and third generator
(13) third generator (13) has cryogen liquid pipeline to be connected to through second throttle (14) with condenser (5) again after being connected to, third
Generator (13) is connected to there are also refrigerant steam channel with condenser (5), forms combined cycle energy supplying system.
24. combined cycle energy supplying system is to increase third in any combined cycle energy supplying system described in claim 1-20
Generator (3) is had blast tube and the second hair by generator, second throttle, third solution pump and third solution heat exchanger
After raw device (4) connection the second generator (4) have again blast tube with it is external be connected to be adjusted to generator (3) have blast tube according to
The second generator (4) has blast tube to be connected to outside again after secondary connection third generator (13) and the second generator (4), the
Two absorbers (2) add weak solution pipeline through third solution pump (15) and third solution heat exchanger (16) and third generator
(13) it is connected to, third generator (13) also concentrated solution pipeline connects through third solution heat exchanger (16) and the second generator (4)
It is logical, there is refrigerant steam channel to be connected to condenser (5) in generator (3) and is adjusted to generator (3) and has refrigerant steam channel and the
Third generator (13) has cryogen liquid pipeline to connect through second throttle (14) and condenser (5) again after three generators (13) connection
Logical, third generator (13) is connected to there are also refrigerant steam channel with condenser (5), forms combined cycle energy supplying system.
25. combined cycle energy supplying system is to increase third in any combined cycle energy supplying system described in claim 1-20
Generator (3) is had blast tube to be connected to the second generator (4) by generator, second throttle and third solution heat exchanger
The second generator (4) has blast tube to be connected to outside again and is adjusted to generator (3) and has blast tube to be sequentially communicated third later
The second generator (4) has blast tube to be connected to outside again after generator (13) and the second generator (4), by the second absorber
(2) there is weak solution pipeline to be connected to through the second solution pump (9) and the second solution heat exchanger (11) with generator (3) and be adjusted to second
Absorber (2) has weak solution pipeline through the second solution pump (9), the second solution heat exchanger (11) and third solution heat exchanger
(16) it is connected to generator (3), has concentrated solution pipeline through the second solution heat exchanger (11) and the second generator in generator (3)
(4) connection, which is adjusted to generator (3), has concentrated solution pipeline to be connected to through third solution heat exchanger (16) with third generator (13),
Third generator (13) has concentrated solution pipeline to be connected to through the second solution heat exchanger (11) with the second generator (4) again, will occur
Device (3) has refrigerant steam channel to be connected to condenser (5) to be adjusted to generator (3) and have refrigerant steam channel and third generator
(13) third generator (13) has cryogen liquid pipeline to be connected to through second throttle (14) with condenser (5) again after being connected to, third
Generator (13) is connected to there are also refrigerant steam channel with condenser (5), forms combined cycle energy supplying system.
26. combined cycle energy supplying system is to increase third in any combined cycle energy supplying system described in claim 1-20
Generator (3) is had blast tube and the second hair by generator, second throttle, third solution pump and third solution heat exchanger
After raw device (4) connection the second generator (4) have again blast tube with it is external be connected to be adjusted to generator (3) have blast tube according to
The second generator (4) has blast tube to be connected to outside again after secondary connection third generator (13) and the second generator (4), will
Second absorber (2) has weak solution pipeline to connect through the second solution pump (9) and the second solution heat exchanger (11) and generator (3)
It is logical to be adjusted to the second absorber (2) and have weak solution pipeline through the second solution pump (9) and the second solution heat exchanger (11) and third
Generator (13) connection, third generator (13) have concentrated solution pipeline through third solution pump (15) and third solution heat exchanger again
(16) it is connected to generator (3), has concentrated solution pipeline through the second solution heat exchanger (11) and the second generator in generator (3)
(4) connection, which is adjusted to generator (3), has concentrated solution pipeline through third solution heat exchanger (16) and the second solution heat exchanger
(11) it is connected to the second generator (4), there is refrigerant steam channel to be connected to condenser (5) in generator (3) and be adjusted to generator
(3) third generator (13) has cryogen liquid pipeline through the second section again after having refrigerant steam channel to be connected to third generator (13)
Stream valve (14) is connected to condenser (5), and third generator (13) is connected to there are also refrigerant steam channel with condenser (5), forms connection
Close circulation energy supplying system.
27. combined cycle energy supplying system is to increase by the 4th hair in any combined cycle energy supplying system described in claim 21
Raw device, third throttle valve, the 4th solution pump and the 4th solution heat exchanger, the second absorber (2) add weak solution pipeline through the
Four solution pumps (19) and the 4th solution heat exchanger (20) are connected to the 4th generator (17), and there are also dense molten for the 4th generator (17)
Liquid pipeline is connected to through the 4th solution heat exchanger (20) with the second generator (4), has refrigerant vapour logical in third generator (13)
Road is connected to condenser (5) be adjusted to third generator (13) and there is refrigerant steam channel to be connected to the 4th generator (17) after
Four generators (17) have cryogen liquid pipeline to be connected to through third throttle valve (18) with condenser (5) again, and the 4th generator (17) is also
Refrigerant steam channel is connected to condenser (5), forms combined cycle energy supplying system.
28. combined cycle energy supplying system is to increase by the 4th hair in any combined cycle energy supplying system described in claim 22
Raw device, third throttle valve and the 4th solution heat exchanger, by the second absorber (2) have weak solution pipeline through the second solution pump (9),
Second solution heat exchanger (11) and third solution heat exchanger (16) are connected to generator (3) is adjusted to the second absorber (2)
There is weak solution pipeline molten through the second solution pump (9), the second solution heat exchanger (11), the 4th solution heat exchanger (20) and third
Liquid heat exchanger (16) is connected to generator (3), has concentrated solution pipeline through the second solution heat exchanger in third generator (13)
(11) it is connected to the second generator (4) and is adjusted to third generator (13) and has concentrated solution pipeline through the 4th solution heat exchanger (20)
It is connected to the 4th generator (17), the 4th generator (17) has concentrated solution pipeline through the second solution heat exchanger (11) and second again
Generator (4) connection, has refrigerant steam channel to be connected to condenser (5) in third generator (13) and is adjusted to third generator
(13) the 4th generator (17) has cryogen liquid pipeline through third again after having refrigerant steam channel to be connected to the 4th generator (17)
Throttle valve (18) is connected to condenser (5), and the 4th generator (17) is connected to there are also refrigerant steam channel with condenser (5), is formed
Combined cycle energy supplying system.
29. combined cycle energy supplying system is to increase by the 4th hair in any combined cycle energy supplying system described in claim 23
Second absorber (2) is had weak solution pipeline through the by raw device, third throttle valve, the 4th solution pump and the 4th solution heat exchanger
Two solution pumps (9) and the second solution heat exchanger (11) be connected to third generator (13) be adjusted to the second absorber (2) have it is dilute
Solution line is connected to through the second solution pump (9) and the second solution heat exchanger (11) with the 4th generator (17), the 4th generator
(17) concentrated solution pipeline is connected to through the 4th solution pump (19) and the 4th solution heat exchanger (20) with third generator (13) again,
There is concentrated solution pipeline to occur through third solution heat exchanger (16) and the second solution heat exchanger (11) with second in generator (3)
Device (4) connection, which is adjusted to generator (3), has concentrated solution pipeline through third solution heat exchanger (16), the 4th solution heat exchanger
(20) it is connected to the second solution heat exchanger (11) with the second generator (4), third generator (13) is had into refrigerant steam channel
It is connected to condenser (5) the 4th after being adjusted to third generator (13) and thering is refrigerant steam channel to be connected to the 4th generator (17)
Generator (17) has cryogen liquid pipeline to be connected to through third throttle valve (18) with condenser (5) again, and there are also cold for the 4th generator (17)
Agent steam channel is connected to condenser (5), forms combined cycle energy supplying system.
30. combined cycle energy supplying system is to increase by the 4th hair in any combined cycle energy supplying system described in claim 21
Generator (3) is had blast tube and second to occur by raw device, third throttle valve, the 4th solution pump and the 4th solution heat exchanger
The second generator (4) has blast tube to be adjusted to generator (3) with external be connected to and have blast tube successively again after device (4) connection
The second generator (4) has blast tube again after connection third generator (13), the 4th generator (17) and the second generator (4)
It is connected to outside, the second absorber (2) adds weak solution pipeline through the 4th solution pump (19) and the 4th solution heat exchanger (20)
It is connected to the 4th generator (17), there are also concentrated solution pipelines through the 4th solution heat exchanger (20) and second for the 4th generator (17)
Generator (4) connection, has refrigerant steam channel to be connected to condenser (5) in third generator (13) and is adjusted to third generator
(13) the 4th generator (17) has cryogen liquid pipeline through third again after having refrigerant steam channel to be connected to the 4th generator (17)
Throttle valve (18) is connected to condenser (5), and the 4th generator (17) is connected to there are also refrigerant steam channel with condenser (5), is formed
Combined cycle energy supplying system.
31. combined cycle energy supplying system is to increase by the 4th hair in any combined cycle energy supplying system described in claim 22
Raw device, third throttle valve and the 4th solution heat exchanger, have blast tube to be connected to it with the second generator (4) in generator (3)
Afterwards the second generator (4) have again blast tube with outside be connected to be adjusted to generator (3) have blast tube be sequentially communicated third send out
The second generator (4) has blast tube and outside to connect again after raw device (13), the 4th generator (17) and the second generator (4)
It is logical, there is weak solution pipeline through the second solution pump (9), the second solution heat exchanger (11) and third solution the second absorber (2)
Heat exchanger (16) is connected to generator (3) to be adjusted to the second absorber (2) and has weak solution pipeline through the second solution pump (9),
Two solution heat exchangers (11), the 4th solution heat exchanger (20) and third solution heat exchanger (16) are connected to generator (3),
There is concentrated solution pipeline to be connected to through the second solution heat exchanger (11) with the second generator (4) in third generator (13) and is adjusted to
Three generators (13) have concentrated solution pipeline to be connected to through the 4th solution heat exchanger (20) with the 4th generator (17), the 4th generator
(17) concentrated solution pipeline is connected to through the second solution heat exchanger (11) with the second generator (4) again, by third generator (13)
There is refrigerant steam channel to be connected to condenser (5) to be adjusted to third generator (13) and have refrigerant steam channel and the 4th generator
(17) the 4th generator (17) has cryogen liquid pipeline to be connected to through third throttle valve (18) with condenser (5) again after being connected to, and the 4th
Generator (17) is connected to there are also refrigerant steam channel with condenser (5), forms combined cycle energy supplying system.
32. combined cycle energy supplying system is to increase by the 4th hair in any combined cycle energy supplying system described in claim 23
Generator (3) is had blast tube and second to occur by raw device, third throttle valve, the 4th solution pump and the 4th solution heat exchanger
The second generator (4) has blast tube to be adjusted to generator (3) with external be connected to and have blast tube successively again after device (4) connection
The second generator (4) has blast tube again after connection third generator (13), the 4th generator (17) and the second generator (4)
Be connected to outside, have weak solution pipeline through the second solution pump (9) and the second solution heat exchanger (11) the second absorber (2) and
Third generator (13) connection, which is adjusted to the second absorber (2), has weak solution pipeline through the second solution pump (9) and the second solution heat
Exchanger (11) is connected to the 4th generator (17), the 4th generator (17) have concentrated solution pipeline through the 4th solution pump (19) again and
4th solution heat exchanger (20) is connected to third generator (13), has concentrated solution pipeline through third solution heat in generator (3)
Exchanger (16) and the second solution heat exchanger (11) are connected to the second generator (4) to be adjusted to generator (3) and has concentrated solution pipe
Road occurs through third solution heat exchanger (16), the 4th solution heat exchanger (20) and the second solution heat exchanger (11) with second
Third generator (13) is had refrigerant steam channel to be connected to condenser (5) and is adjusted to third generator (13) and has by device (4) connection
The 4th generator (17) has cryogen liquid pipeline through third throttle valve again after refrigerant steam channel is connected to the 4th generator (17)
(18) it is connected to condenser (5), the 4th generator (17) is connected to there are also refrigerant steam channel with condenser (5), and formation, which is combined, to follow
Ring energy supplying system.
33. combined cycle energy supplying system is in any combined cycle energy supplying system described in claim 27-32, by third
Generator (13) have cryogen liquid pipeline be connected to through second throttle (14) with condenser (5) be adjusted to third generator (13) have it is cold
Agent liquid pipeline is connected to through the 4th generator (17) and second throttle (14) with condenser (5), forms combined cycle energy supplying system.
34. combined cycle energy supplying system is to increase by second in any combined cycle energy supplying system described in claim 1-33
Heat exchanger, second heat exchanger (12) has heated medium pipeline to be connected to outside, and takes following any skill
Art measure is to form combined cycle energy supplying system: 1. having blast tube to be connected to outside in the second generator (4) and is adjusted to second
Generator (4) has blast tube to be connected to through second heat exchanger (12) with outside;2. by the second generator (4) have blast tube with
Outside connection, which is adjusted to the second generator (4), has blast tube to be connected to through second heat exchanger (12) and evaporator (6) with outside;
3. by the second generator (4) have blast tube with outside be connected to be adjusted to the second generator (4) have blast tube through second heat friendship
Parallel operation (12), evaporator (6) and low temperature heat exchanger (F) are connected to outside.
35. combined cycle energy supplying system is to increase third in any combined cycle energy supplying system described in claim 1-20
Second generator (4) is had blast tube and outer by generator, third solution pump, third solution heat exchanger and third absorber
There is again third generator (13) after portion's connection is adjusted to the second generator (4) and has blast tube to be connected to third generator (13)
Blast tube is connected to outside, is had refrigerant steam channel to be connected to absorber (1) evaporator (6) and is adjusted to evaporator (6) and has
Refrigerant steam channel is connected to third absorber (21), and there are also weak solution pipelines through third solution pump (15) for third absorber (21)
It is connected to third solution heat exchanger (16) with third generator (13), there are also concentrated solution pipelines through third for third generator (13)
Solution heat exchanger (16) is connected to third absorber (21), and there are also refrigerant steam channel and absorbers for third generator (13)
(1) it is connected to, third absorber (21) also heated medium pipeline is connected to outside, forms combined cycle energy supplying system.
36. combined cycle energy supplying system is to increase by the second heat in any combined cycle energy supplying system described in claim 35
Exchanger, second heat exchanger (12) has heated medium pipeline to be connected to outside, and takes following any technology
Measure is to form combined cycle energy supplying system: 1. having blast tube to be connected to outside in third generator (13) and is adjusted to third hair
Raw device (13) have blast tube to be connected to through second heat exchanger (12) with outside;2. by third generator (13) have blast tube with
Outside connection, which is adjusted to third generator (13), has blast tube to connect through second heat exchanger (12) and evaporator (6) with outside
It is logical;3. thering is blast tube to be connected to outside in third generator (13) to be adjusted to third generator (13) and have blast tube through second
Heat exchanger (12), evaporator (6) and low temperature heat exchanger (F) are connected to outside.
37. combined cycle energy supplying system is to increase waste heat in any combined cycle energy supplying system described in claim 1-20
Boiler and second circulation pump, second after thering is blast tube to be sequentially communicated generator (3) and the second generator (4) in boiler (B)
Generator (4) have again blast tube be connected to outside be adjusted to boiler (B) have blast tube be connected to waste heat boiler (N) later more than
Heat boiler (N) has blast tube to be connected to outside again, relies between waste heat boiler (N), generator (3) and the second generator (4)
Second circulation pumps (O) and circulating thermal medium pipeline constitutes closed loop, forms combined cycle energy supplying system.
38. combined cycle energy supplying system is to increase by the second heat in any combined cycle energy supplying system described in claim 37
Exchanger, second heat exchanger (12) has heated medium pipeline to be connected to outside, and takes following any technology
Measure is to form combined cycle energy supplying system: 1. will be between waste heat boiler (N), generator (3) and the second generator (4) by the
Two circulating pumps (O) and circulating thermal medium pipeline constitute closed loop and are adjusted to waste heat boiler (N), generator (3), the second hair
Closed circulation is constituted by second circulation pump (O) and circulating thermal medium pipeline between raw device (4) and second heat exchanger (12) to return
Road;2. second circulation pump (O) and circulating thermal medium will be relied between waste heat boiler (N), generator (3) and the second generator (4)
Pipeline constitutes closed loop and is adjusted to waste heat boiler (N), generator (3), the second generator (4), second heat exchanger
(12) closed loop is constituted by second circulation pump (O) and circulating thermal medium pipeline between evaporator (6);3. by waste heat
Closure is constituted by second circulation pump (O) and circulating thermal medium pipeline between boiler (N), generator (3) and the second generator (4)
Circulation loop is adjusted to waste heat boiler (N), generator (3), the second generator (4), second heat exchanger (12), evaporator (6)
Closed loop is constituted by second circulation pump (O) and circulating thermal medium pipeline between low temperature heat exchanger (F).
39. combined cycle energy supplying system is to increase waste heat in any combined cycle energy supplying system described in claim 1-20
Boiler, second circulation pump, third generator, third solution pump, third solution heat exchanger and third absorber, by boiler (B)
The second generator (4) has blast tube and outside again after having blast tube to be sequentially communicated generator (3) and the second generator (4)
Waste heat boiler (N) has blast tube and outside again after connection is adjusted to boiler (B) and has blast tube be connected to waste heat boiler (N)
Connection, by second circulation pump (O) between waste heat boiler (N), generator (3), the second generator (4) and third generator (13)
Closed loop is constituted with circulating thermal medium pipeline;There is refrigerant steam channel to be connected to adjustment with absorber (1) evaporator (6)
There is refrigerant steam channel to be connected to third absorber (21) for evaporator (6), there are also weak solution pipelines to pass through for third absorber (21)
Third solution pump (15) and third solution heat exchanger (16) are connected to third generator (13), and there are also dense for third generator (13)
Solution line is connected to through third solution heat exchanger (16) with third absorber (21), and there are also refrigerant vapours for third generator (13)
Channel is connected to absorber (1), and third absorber (21) also heated medium pipeline is connected to outside, is formed combined cycle and is supplied
It can system.
40. combined cycle energy supplying system is to increase work in any combined cycle energy supplying system described in claim 1-39
Machine, Steam Power Equipment forward circulation provide power to working machine (P) respectively, provide power to compression reverse circulation and to suction
Receipts formula reverse circulation provides driving thermic load, forms combined cycle energy supplying system.
41. combined cycle energy supplying system, be in any combined cycle energy supplying system described in claim 1-40, by fuel and
Air duct is changed to high temperature heat source medium channel, and blast tube is changed to low-temperature heat source medium channel, forms combined cycle
Energy supplying system.
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CN106352595B (en) * | 2015-12-30 | 2020-01-31 | 李华玉 | Class thermally driven compression-absorption heat pump |
CN106440471B (en) * | 2016-05-30 | 2020-01-31 | 李华玉 | Combined heat and power system |
WO2022161112A1 (en) * | 2021-01-27 | 2022-08-04 | 李华玉 | Dual-fuel combined cycle steam power device |
WO2022166504A1 (en) * | 2021-02-07 | 2022-08-11 | 李华玉 | Dual-fuel combined cycle steam power plant |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1804511A (en) * | 2006-01-23 | 2006-07-19 | 李华玉 | Compression-absorption combined heat pump heating system |
CN201181133Y (en) * | 2008-03-03 | 2009-01-14 | 清华大学 | Combined cooling, heating and power supplying system |
CN102419026A (en) * | 2011-07-27 | 2012-04-18 | 李华玉 | Absorption-type heat source temperature changer |
CN102635970A (en) * | 2012-04-09 | 2012-08-15 | 李华玉 | Grading condensation third-type absorption heat pump |
-
2015
- 2015-06-08 CN CN201510330916.8A patent/CN105041396B/en active Active
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1804511A (en) * | 2006-01-23 | 2006-07-19 | 李华玉 | Compression-absorption combined heat pump heating system |
CN201181133Y (en) * | 2008-03-03 | 2009-01-14 | 清华大学 | Combined cooling, heating and power supplying system |
CN102419026A (en) * | 2011-07-27 | 2012-04-18 | 李华玉 | Absorption-type heat source temperature changer |
CN102635970A (en) * | 2012-04-09 | 2012-08-15 | 李华玉 | Grading condensation third-type absorption heat pump |
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