CN105041396B - Combined cycle energy supplying system - Google Patents

Combined cycle energy supplying system Download PDF

Info

Publication number
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
Authority
CN
China
Prior art keywords
generator
heat exchanger
solution
absorber
condenser
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201510330916.8A
Other languages
Chinese (zh)
Other versions
CN105041396A (en
Inventor
李华玉
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CN201510330916.8A priority Critical patent/CN105041396B/en
Publication of CN105041396A publication Critical patent/CN105041396A/en
Application granted granted Critical
Publication of CN105041396B publication Critical patent/CN105041396B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Sorption Type Refrigeration Machines (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)

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

Combined cycle energy supplying system
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.
CN201510330916.8A 2014-06-09 2015-06-08 Combined cycle energy supplying system Active CN105041396B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510330916.8A CN105041396B (en) 2014-06-09 2015-06-08 Combined cycle energy supplying system

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
CN2014102686699 2014-06-09
CN201410268669 2014-06-09
CN201510330916.8A CN105041396B (en) 2014-06-09 2015-06-08 Combined cycle energy supplying system

Publications (2)

Publication Number Publication Date
CN105041396A CN105041396A (en) 2015-11-11
CN105041396B true CN105041396B (en) 2019-02-15

Family

ID=54448315

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510330916.8A Active CN105041396B (en) 2014-06-09 2015-06-08 Combined cycle energy supplying system

Country Status (1)

Country Link
CN (1) CN105041396B (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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)

* Cited by examiner, † Cited by third party
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

Patent Citations (4)

* Cited by examiner, † Cited by third party
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

Also Published As

Publication number Publication date
CN105041396A (en) 2015-11-11

Similar Documents

Publication Publication Date Title
CN104929706B (en) Combined cycle energy supplying system
CN104963732B (en) Combined cycle energy supplying system
CN104929704B (en) Combined cycle energy supplying system
CN108119194A (en) Triple combined circulation power apparatus
CN106016821A (en) First-class heat drive compression-absorption type heat pump
CN104948245A (en) Combined-cycle energy supply system
CN106895603A (en) Compression/absorb enclosed parallel connection composite fuel gas heat pump operation method
CN105041471A (en) Combined circulation energy supplying system
CN105041396B (en) Combined cycle energy supplying system
CN104748439B (en) The dynamic co-feeding system of heat
CN106225307A (en) First kind thermal drivers compression absorption heat pump
CN104833128B (en) 4th class absorption heat pump
CN105004095B (en) A kind of trans critical cycle and the combined heat-pump system of two-stage absorption heat pump coproduction
CN105019954B (en) Combined cycle energy supplying system
CN105953464A (en) Fourth kind thermal-driving compression-absorption type heat pump
CN105041472A (en) Combined cycle energy supply system
CN104963733B (en) Combined cycle energy supplying system
CN104989472B (en) Combined cycle energy supplying system
CN105953467A (en) Fourth kind thermal-driving compression-absorption type heat pump
CN107477912A (en) Heated type cooling cycle system
CN106225309A (en) First kind thermal drivers compression absorption heat pump
CN110307665A (en) Direct-fired lithium bromide absorption type cold water, heat pump unit
CN105953465A (en) Fourth kind thermal-driving compression-absorption type heat pump
CN110530058A (en) Combined cycle heat pump assembly
CN205383781U (en) Compression of driving vapour of gasengine and absorption combined type heat pump water heater group

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant