CN105041472A

CN105041472A - Combined cycle energy supply system

Info

Publication number: CN105041472A
Application number: CN201510333662.5A
Authority: CN
Inventors: 李华玉
Original assignee: Individual
Current assignee: Individual
Priority date: 2014-06-09
Filing date: 2015-06-08
Publication date: 2015-11-11

Abstract

The invention provides a combined cycle energy supply system and belongs to the technical field of heat energy utilization and heat pumps. A gas-steam positive cycle system is formed by a gas compressor, a combustion chamber, a gas turbine, a steam turbine, a waste heat boiler, a circulating pump and a heat exchanger. A compression type reverse cycle system is formed by a compressor, a cooler, an evaporator, an expander and a low-temperature heat exchanger. An absorption type reverse cycle system is formed by an absorber, a second absorber, a generator, a second generator, a condenser, an evaporator, a throttling valve, a solution pump, a second solution pump, a solution heat exchanger and a second solution heat exchanger. The gas-steam positive cycle supplies power to the compression type reverse cycle and supplies drive heat loads to the absorption type reverse cycle. The compression type reverse cycle acquires low-temperature heat loads, supplies heat to the outside through the cooler and supplies heat to the absorption type reverse cycle through the corresponding evaporator. The absorption type reverse cycle supplies heat to the outside through the absorber, the second absorber and the condenser. The combined cycle energy supply system is formed.

Description

Combined cycle energy supplying system

Technical field:

The invention belongs to power, refrigeration and technical field of heat pumps.

Background technique:

Undertaken in the system of heat supply at fuel by burning, between the combustion gas that burning is formed and heated medium, there is the very large temperature difference; Passing through directly utilizing fuel burns carries out in the system of freezing, and the combustion gas that burning is formed is same with between refrigeration plant working medium exists the very large temperature difference; There is provided in the distributed energy resource system of power at employing gas turbine installation, power provides and is actually restricted supplementary condition, and many times still there is the situation that the temperature difference can not make full use of.These can not realize the situation of heat energy efficiency utilization, mainly can be summarized as six aspects: 1. not under drive load condition, there is the unserviceable large temperature difference, cannot realize heat energy efficiency utilization between combustion gas and heated medium; When 2. configuring absorption heat pump, by the restriction in absorption heat pump working medium operating temperature interval, drive between combustion gas and absorption heat pump working medium and there is the large temperature difference, the temperature difference utilizes unreasonable; 3. configure exhaust heat boiler, combustion gas provides sensible heat to exhaust heat boiler, produces link there is the larger temperature difference at steam; Like this, when adopting steam driven absorption heat pump, the temperature difference utilizes unreasonable; 4. Low Temperature Thermal resource shortage, is difficult to the heat energy utilized in environment; 5., when Low Temperature Thermal resource temperature is very low, the working medium that thermal performance and Safety performance are all satisfactory, be applicable to absorption heat pump unit cannot be found; 6. combustion gas low-temperature zone heat energy is difficult to realize efficient heat supply or highly effective refrigeration.

For above-mentioned Problems existing, and the efficient and deep exploitation of special consideration combustion gas low-temperature zone heat energy, inventor proposes combined cycle energy supplying system, by Gas-steam Combined Cycle device, the high temperature heat of combustion gas is converted into mechanical energy, mechanical energy drives compression type reverse circulation or externally provides power simultaneously, the waste heat load of Gas-steam Combined Cycle device drives absorption reverse circulation, obtained by compression type reverse circulation and absorption reverse circulation and promote the temperature of low-grade heat load, reduce the limiting factor of heat energy efficiency utilization, realize heating or freezing premised on heat energy efficiency utilization.

Summary of the invention:

Main purpose of the present invention to provide combined cycle energy supplying system, and concrete summary of the invention subitem is described below:

1. combined cycle energy supplying system, formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, vaporizer, cryogenic throttle valve, low temperature heat exchanger, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, gas compressor has air passageways and ft connection, gas compressor also has compressed air channel and combustion chamber, firing chamber also has fuel channel and ft connection, firing chamber also has blast tube to be communicated with gas turbine, gas turbine also has blast tube to be communicated with exhaust heat boiler, exhaust heat boiler also have blast tube be communicated with generator and the second generator successively after the second generator have blast tube and ft connection again, steam turbine has low pressure steam passage to be communicated with heat exchanger, heat exchanger also has condensed fluid pipeline to be communicated with exhaust heat boiler through recycle pump, exhaust heat boiler also has high pressure steam passage to be communicated with steam turbine, heat exchanger also has heated medium pipeline and ft connection, the finisher that compressor has refrigerant steam channel to be communicated with vaporizer has cryogen liquid pipeline to be communicated with low temperature heat exchanger through cryogenic throttle valve again, low temperature heat exchanger also has refrigerant steam channel to be communicated with compressor, and low temperature heat exchanger also has cryogenic media pipeline and ft connection, vaporizer also has refrigerant steam channel to be communicated with adsorber, adsorber also has dilute solution pipeline to be communicated with the second adsorber with solution heat exchanger through solution pump, second adsorber also has dilute solution pipeline to be communicated with generator with the second solution heat exchanger through the second solution pump, generator also has concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger, second generator also has concentrated solution pipeline to be communicated with adsorber through solution heat exchanger, generator also has refrigerant steam channel to be communicated with condenser, second generator also has refrigerant steam channel to be communicated with the second adsorber, condenser also has cryogen liquid pipeline to be communicated with vaporizer through throttle valve, adsorber, second adsorber and condenser also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger form fuel gas-steam forward circulation system, compressor, vaporizer, cryogenic throttle valve and low temperature heat exchanger form compression type reverse circulation system, and adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system, fuel gas-steam forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, fuel gas-steam forward circulation provides driving heat load to absorption reverse circulation, compression type reverse circulation obtains Low Temperature Thermal load by vaporizer to absorption reverse circulation heat supply, absorption reverse circulation, by adsorber, the second adsorber and the external heat supply of condenser, forms combined cycle energy supplying system.

2. combined cycle energy supplying system, in the combined cycle energy supplying system described in the 1st, increase by the second compressor, the finisher being had by compressor refrigerant steam channel to be communicated with vaporizer has cryogen liquid pipeline to be communicated with through cryogenic throttle valve the finisher being adjusted to compressor and having refrigerant steam channel to be communicated with vaporizer with low temperature heat exchanger again has refrigerant steam channel to be communicated with the second compressor again, the finisher that second compressor also has refrigerant steam channel to be communicated with vaporizer has cryogen liquid pipeline to be communicated with low temperature heat exchanger through cryogenic throttle valve again, form combined cycle energy supplying system.

3. combined cycle energy supplying system, formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, the second condenser, cryogenic throttle valve, low temperature heat exchanger, vaporizer, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, gas compressor has air passageways and ft connection, gas compressor also has compressed air channel and combustion chamber, firing chamber also has fuel channel and ft connection, firing chamber also has blast tube to be communicated with gas turbine, gas turbine also has blast tube to be communicated with exhaust heat boiler, exhaust heat boiler also have blast tube be communicated with generator and the second generator successively after the second generator have blast tube and ft connection again, steam turbine has low pressure steam passage to be communicated with heat exchanger, heat exchanger also has condensed fluid pipeline to be communicated with exhaust heat boiler through recycle pump, exhaust heat boiler also has high pressure steam passage to be communicated with steam turbine, heat exchanger also has heated medium pipeline and ft connection, compressor have refrigerant steam channel be communicated with the second condenser after the second condenser have cryogen liquid pipeline to be communicated with low temperature heat exchanger through cryogenic throttle valve again, low temperature heat exchanger also has refrigerant steam channel to be communicated with compressor, low temperature heat exchanger also has cryogenic media pipeline and ft connection, and the second condenser also has heated medium pipeline and ft connection, vaporizer also has refrigerant steam channel to be communicated with adsorber, adsorber also has dilute solution pipeline to be communicated with the second adsorber with solution heat exchanger through solution pump, second adsorber also has dilute solution pipeline to be communicated with generator with the second solution heat exchanger through the second solution pump, generator also has concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger, second generator also has concentrated solution pipeline to be communicated with adsorber through solution heat exchanger, generator also has refrigerant steam channel to be communicated with condenser, second generator also has refrigerant steam channel to be communicated with the second adsorber, condenser also has cryogen liquid pipeline to be communicated with vaporizer through throttle valve, vaporizer also has cryogenic media pipeline and ft connection, adsorber, second adsorber and condenser also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger form fuel gas-steam forward circulation system, compressor, the second condenser, cryogenic throttle valve and low temperature heat exchanger form compression type reverse circulation system, and adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system, fuel gas-steam forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, fuel gas-steam forward circulation provides driving heat load to absorption reverse circulation, compression type reverse circulation obtains Low Temperature Thermal load and passes through the external heat supply of the second condenser, absorption reverse circulation obtains Low Temperature Thermal load and by adsorber, the second adsorber and the external heat supply of condenser, forms combined cycle energy supplying system.

4. combined cycle energy supplying system, in the combined cycle energy supplying system described in the 3rd, increase by the second compressor, compressor is had refrigerant steam channel be communicated with the second condenser after the second condenser have again cryogen liquid pipeline through cryogenic throttle valve to be communicated with low temperature heat exchanger be adjusted to compressor have refrigerant steam channel to be communicated with the second condenser after the second condenser have refrigerant steam channel to be communicated with the second compressor again, second compressor also have refrigerant steam channel be communicated with the second condenser after the second condenser have cryogen liquid pipeline to be communicated with low temperature heat exchanger through cryogenic throttle valve again, form combined cycle energy supplying system.

5. combined cycle energy supplying system, formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, cooler, vaporizer, cryogenic throttle valve, low temperature heat exchanger, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, gas compressor has air passageways and ft connection, gas compressor also has compressed air channel and combustion chamber, firing chamber also has fuel channel and ft connection, firing chamber also has blast tube to be communicated with gas turbine, gas turbine also has blast tube to be communicated with exhaust heat boiler, exhaust heat boiler also have blast tube be communicated with generator and the second generator successively after the second generator have blast tube and ft connection again, steam turbine has low pressure steam passage to be communicated with heat exchanger, heat exchanger also has condensed fluid pipeline to be communicated with exhaust heat boiler through recycle pump, exhaust heat boiler also has high pressure steam passage to be communicated with steam turbine, heat exchanger also has heated medium pipeline and ft connection, the aftercooler that compressor has refrigerant steam channel to be communicated with cooler has refrigerant steam channel to be communicated with vaporizer again, vaporizer also has cryogen liquid pipeline to be communicated with low temperature heat exchanger through cryogenic throttle valve, low temperature heat exchanger also has refrigerant steam channel to be communicated with compressor, low temperature heat exchanger also has cryogenic media pipeline and ft connection, and cooler also has heated medium pipeline and ft connection, vaporizer also has refrigerant steam channel to be communicated with adsorber, adsorber also has dilute solution pipeline to be communicated with the second adsorber with solution heat exchanger through solution pump, second adsorber also has dilute solution pipeline to be communicated with generator with the second solution heat exchanger through the second solution pump, generator also has concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger, second generator also has concentrated solution pipeline to be communicated with adsorber through solution heat exchanger, generator also has refrigerant steam channel to be communicated with condenser, second generator also has refrigerant steam channel to be communicated with the second adsorber, condenser also has cryogen liquid pipeline to be communicated with vaporizer through throttle valve, adsorber, second adsorber and condenser also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger form fuel gas-steam forward circulation system, compressor, cooler, vaporizer, cryogenic throttle valve and low temperature heat exchanger form compression type reverse circulation system, and adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system, fuel gas-steam forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, fuel gas-steam forward circulation provides driving heat load to absorption reverse circulation, compression type reverse circulation obtain Low Temperature Thermal load and respectively by the external heat supply of cooler and by vaporizer to absorption reverse circulation heat supply, absorption reverse circulation, by adsorber, the second adsorber and the external heat supply of condenser, forms combined cycle energy supplying system.

6. combined cycle energy supplying system, in the combined cycle energy supplying system described in the 5th, increase by the second compressor, the aftercooler being had by compressor refrigerant steam channel to be communicated with cooler has refrigerant steam channel to be communicated with vaporizer to be adjusted to compressor the aftercooler having refrigerant steam channel to be communicated with cooler to have refrigerant steam channel to be communicated with the second compressor more again, the aftercooler that second compressor also has refrigerant steam channel to be communicated with cooler has refrigerant steam channel to be communicated with vaporizer again, forms combined cycle energy supplying system.

7. combined cycle energy supplying system, formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, the second compressor, the second condenser, vaporizer, cryogenic throttle valve, the second cryogenic throttle valve, low temperature heat exchanger, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, gas compressor has air passageways and ft connection, gas compressor also has compressed air channel and combustion chamber, firing chamber also has fuel channel and ft connection, firing chamber also has blast tube to be communicated with gas turbine, gas turbine also has blast tube to be communicated with exhaust heat boiler, exhaust heat boiler also have blast tube be communicated with generator and the second generator successively after the second generator have blast tube and ft connection again, steam turbine has low pressure steam passage to be communicated with heat exchanger, heat exchanger also has condensed fluid pipeline to be communicated with exhaust heat boiler through recycle pump, exhaust heat boiler also has high pressure steam passage to be communicated with steam turbine, heat exchanger also has heated medium pipeline and ft connection, compressor has low pressure refrigerant steam channel to be communicated with vaporizer, vaporizer also has low pressure cryogen liquid pipeline low temperature heat exchanger after cryogenic throttle valve is communicated with low temperature heat exchanger to have refrigerant steam channel to be communicated with compressor again, compressor also has low pressure refrigerant steam channel to be communicated with the second compressor, second compressor also has high pressure refrigerant steam channel to be communicated with the second condenser, second condenser also has high pressure cryogen liquid pipeline low temperature heat exchanger after vaporizer and the second cryogenic throttle valve are communicated with low temperature heat exchanger to have refrigerant steam channel to be communicated with compressor again, low temperature heat exchanger also has cryogenic media pipeline and ft connection, second condenser also has heated medium pipeline and ft connection, vaporizer also has refrigerant steam channel to be communicated with adsorber, adsorber also has dilute solution pipeline to be communicated with the second adsorber with solution heat exchanger through solution pump, second adsorber also has dilute solution pipeline to be communicated with generator with the second solution heat exchanger through the second solution pump, generator also has concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger, second generator also has concentrated solution pipeline to be communicated with adsorber through solution heat exchanger, generator also has refrigerant steam channel to be communicated with condenser, second generator also has refrigerant steam channel to be communicated with the second adsorber, condenser also has cryogen liquid pipeline to be communicated with vaporizer through throttle valve, adsorber, second adsorber and condenser also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger form fuel gas-steam forward circulation system, and compressor, the second compressor, the second condenser, vaporizer, cryogenic throttle valve, the second cryogenic throttle valve and low temperature heat exchanger form compression type reverse circulation system, adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system, fuel gas-steam forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, fuel gas-steam forward circulation provides driving heat load to absorption reverse circulation, compression type reverse circulation obtain Low Temperature Thermal load and respectively by the external heat supply of the second condenser and by vaporizer to absorption reverse circulation heat supply, absorption reverse circulation, by adsorber, the second adsorber and the external heat supply of condenser, forms combined cycle energy supplying system.

8. combined cycle energy supplying system, formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, the second condenser, vaporizer, cryogenic throttle valve, the second cryogenic throttle valve, low temperature heat exchanger, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, gas compressor has air passageways and ft connection, gas compressor also has compressed air channel and combustion chamber, firing chamber also has fuel channel and ft connection, firing chamber also has blast tube to be communicated with gas turbine, gas turbine also has blast tube to be communicated with exhaust heat boiler, exhaust heat boiler also have blast tube be communicated with generator and the second generator successively after the second generator have blast tube and ft connection again, steam turbine has low pressure steam passage to be communicated with heat exchanger, heat exchanger also has condensed fluid pipeline to be communicated with exhaust heat boiler through recycle pump, exhaust heat boiler also has high pressure steam passage to be communicated with steam turbine, heat exchanger also has heated medium pipeline and ft connection, compressor has low pressure refrigerant steam channel to be communicated with vaporizer, vaporizer also has low pressure cryogen liquid pipeline low temperature heat exchanger after cryogenic throttle valve is communicated with low temperature heat exchanger to have refrigerant steam channel to be communicated with compressor again, compressor also has high pressure refrigerant steam channel to be communicated with the second condenser, second condenser also has high pressure cryogen liquid pipeline low temperature heat exchanger after vaporizer and the second cryogenic throttle valve are communicated with low temperature heat exchanger to have refrigerant steam channel to be communicated with compressor again, low temperature heat exchanger also has cryogenic media pipeline and ft connection, second condenser also has heated medium pipeline and ft connection, vaporizer also has refrigerant steam channel to be communicated with adsorber, adsorber also has dilute solution pipeline to be communicated with the second adsorber with solution heat exchanger through solution pump, second adsorber also has dilute solution pipeline to be communicated with generator with the second solution heat exchanger through the second solution pump, generator also has concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger, second generator also has concentrated solution pipeline to be communicated with adsorber through solution heat exchanger, generator also has refrigerant steam channel to be communicated with condenser, second generator also has refrigerant steam channel to be communicated with the second adsorber, condenser also has cryogen liquid pipeline to be communicated with vaporizer through throttle valve, adsorber, second adsorber and condenser also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger form fuel gas-steam forward circulation system, compressor, the second condenser, vaporizer, cryogenic throttle valve, the second cryogenic throttle valve and low temperature heat exchanger form compression type reverse circulation system, and adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system, fuel gas-steam forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, fuel gas-steam forward circulation provides driving heat load to absorption reverse circulation, compression type reverse circulation obtain Low Temperature Thermal load and respectively by the external heat supply of the second condenser and by vaporizer to absorption reverse circulation heat supply, absorption reverse circulation, by adsorber, the second adsorber and the external heat supply of condenser, forms combined cycle energy supplying system.

9. combined cycle energy supplying system, formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, vaporizer, decompressor, low temperature heat exchanger, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, gas compressor has air passageways and ft connection, gas compressor also has compressed air channel and combustion chamber, firing chamber also has fuel channel and ft connection, firing chamber also has blast tube to be communicated with gas turbine, gas turbine also has blast tube to be communicated with exhaust heat boiler, exhaust heat boiler also have blast tube be communicated with generator and the second generator successively after the second generator have blast tube and ft connection again, steam turbine has low pressure steam passage to be communicated with heat exchanger, heat exchanger also has condensed fluid pipeline to be communicated with exhaust heat boiler through recycle pump, exhaust heat boiler also has high pressure steam passage to be communicated with steam turbine, heat exchanger also has heated medium pipeline and ft connection, the finisher that compressor has refrigerant gas passage to be communicated with vaporizer has refrigerant gas passage to be communicated with decompressor again, decompressor also has refrigerant gas passage to be communicated with compressor through low temperature heat exchanger, and low temperature heat exchanger also has cryogenic media pipeline and ft connection, vaporizer also has refrigerant steam channel to be communicated with adsorber, adsorber also has dilute solution pipeline to be communicated with the second adsorber with solution heat exchanger through solution pump, second adsorber also has dilute solution pipeline to be communicated with generator with the second solution heat exchanger through the second solution pump, generator also has concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger, second generator also has concentrated solution pipeline to be communicated with adsorber through solution heat exchanger, generator also has refrigerant steam channel to be communicated with condenser, second generator also has refrigerant steam channel to be communicated with the second adsorber, condenser also has cryogen liquid pipeline to be communicated with vaporizer through throttle valve, adsorber, second adsorber and condenser also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger form fuel gas-steam forward circulation system, compressor, vaporizer, decompressor and low temperature heat exchanger form compression type reverse circulation system, and adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system, fuel gas-steam forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, fuel gas-steam forward circulation provides driving heat load to absorption reverse circulation, compression type reverse circulation obtains Low Temperature Thermal load by vaporizer to absorption reverse circulation heat supply, absorption reverse circulation, by adsorber, the second adsorber and the external heat supply of condenser, forms combined cycle energy supplying system.

10. combined cycle energy supplying system, in the combined cycle energy supplying system described in the 9th, increase by the second compressor, the finisher being had by compressor refrigerant gas passage to be communicated with vaporizer has refrigerant gas passage to be communicated with decompressor to be adjusted to compressor the finisher having refrigerant gas passage to be communicated with vaporizer to have refrigerant gas passage to be communicated with the second compressor more again, the finisher that second compressor also has refrigerant gas passage to be communicated with vaporizer has refrigerant gas passage to be communicated with decompressor again, forms combined cycle energy supplying system.

11. combined cycle energy supplying systems, formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, vaporizer, decompressor, low temperature heat exchanger, regenerator, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, gas compressor has air passageways and ft connection, gas compressor also has compressed air channel and combustion chamber, firing chamber also has fuel channel and ft connection, firing chamber also has blast tube to be communicated with gas turbine, gas turbine also has blast tube to be communicated with exhaust heat boiler, exhaust heat boiler also have blast tube be communicated with generator and the second generator successively after the second generator have blast tube and ft connection again, steam turbine has low pressure steam passage to be communicated with heat exchanger, heat exchanger also has condensed fluid pipeline to be communicated with exhaust heat boiler through recycle pump, exhaust heat boiler also has high pressure steam passage to be communicated with steam turbine, heat exchanger also has heated medium pipeline and ft connection, the finisher that compressor has refrigerant gas passage to be communicated with vaporizer has refrigerant gas passage to be communicated with decompressor through regenerator again, decompressor also has refrigerant gas passage to be communicated with compressor with regenerator through low temperature heat exchanger, and low temperature heat exchanger also has cryogenic media pipeline and ft connection, vaporizer also has refrigerant steam channel to be communicated with adsorber, adsorber also has dilute solution pipeline to be communicated with the second adsorber with solution heat exchanger through solution pump, second adsorber also has dilute solution pipeline to be communicated with generator with the second solution heat exchanger through the second solution pump, generator also has concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger, second generator also has concentrated solution pipeline to be communicated with adsorber through solution heat exchanger, generator also has refrigerant steam channel to be communicated with condenser, second generator also has refrigerant steam channel to be communicated with the second adsorber, condenser also has cryogen liquid pipeline to be communicated with vaporizer through throttle valve, adsorber, second adsorber and condenser also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger form fuel gas-steam forward circulation system, compressor, vaporizer, decompressor, low temperature heat exchanger and regenerator form compression type reverse circulation system, and adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system, fuel gas-steam forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, fuel gas-steam forward circulation provides driving heat load to absorption reverse circulation, compression type reverse circulation obtains Low Temperature Thermal load by vaporizer to absorption reverse circulation heat supply, absorption reverse circulation, by adsorber, the second adsorber and the external heat supply of condenser, forms combined cycle energy supplying system.

12. combined cycle energy supplying systems, in the combined cycle energy supplying system described in the 11st, increase by the second compressor, the finisher being had by compressor refrigerant gas passage to be communicated with vaporizer has refrigerant gas passage to be communicated with through regenerator the finisher being adjusted to compressor and having refrigerant gas passage to be communicated with logical vaporizer with decompressor again has refrigerant gas passage to be communicated with the second compressor again, the finisher that second compressor also has refrigerant gas passage to be communicated with vaporizer has refrigerant gas passage to be communicated with decompressor through regenerator again, forms combined cycle energy supplying system.

13. combined cycle energy supplying systems, formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, decompressor, cooler, low temperature heat exchanger, vaporizer, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, gas compressor has air passageways and ft connection, gas compressor also has compressed air channel and combustion chamber, firing chamber also has fuel channel and ft connection, firing chamber also has blast tube to be communicated with gas turbine, gas turbine also has blast tube to be communicated with exhaust heat boiler, exhaust heat boiler also have blast tube be communicated with generator and the second generator successively after the second generator have blast tube and ft connection again, steam turbine has low pressure steam passage to be communicated with heat exchanger, heat exchanger also has condensed fluid pipeline to be communicated with exhaust heat boiler through recycle pump, exhaust heat boiler also has high pressure steam passage to be communicated with steam turbine, heat exchanger also has heated medium pipeline and ft connection, compressor has refrigerant gas passage to be communicated with decompressor through cooler, decompressor also has refrigerant gas passage to be communicated with compressor through low temperature heat exchanger, low temperature heat exchanger also has cryogenic media pipeline and ft connection, and cooler also has heated medium pipeline and ft connection, vaporizer has refrigerant steam channel to be communicated with adsorber, adsorber also has dilute solution pipeline to be communicated with the second adsorber with solution heat exchanger through solution pump, second adsorber also has dilute solution pipeline to be communicated with generator with the second solution heat exchanger through the second solution pump, generator also has concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger, second generator also has concentrated solution pipeline to be communicated with adsorber through solution heat exchanger, generator also has refrigerant steam channel to be communicated with condenser, second generator also has refrigerant steam channel to be communicated with the second adsorber, condenser also has cryogen liquid pipeline to be communicated with vaporizer through throttle valve, vaporizer also has cryogenic media pipeline and ft connection, adsorber, second adsorber and condenser also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger form fuel gas-steam forward circulation system, compressor, cooler, decompressor and low temperature heat exchanger form compression type reverse circulation system, and adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system, fuel gas-steam forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, fuel gas-steam forward circulation provides driving heat load to absorption reverse circulation, compression type reverse circulation obtains Low Temperature Thermal load and passes through the external heat supply of cooler, absorption reverse circulation obtains Low Temperature Thermal load and by adsorber, the second adsorber and the external heat supply of condenser, forms combined cycle energy supplying system.

14. combined cycle energy supplying systems, in the combined cycle energy supplying system described in the 13rd, increase by the second compressor, had by compressor refrigerant gas passage to be communicated with decompressor through cooler to be adjusted to compressor and to have refrigerant gas passage to be communicated with the second compressor through cooler, second compressor also has refrigerant gas passage to be communicated with decompressor through cooler, forms combined cycle energy supplying system.

15. combined cycle energy supplying systems, formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, cooler, decompressor, low temperature heat exchanger, regenerator, vaporizer, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, gas compressor has air passageways and ft connection, gas compressor also has compressed air channel and combustion chamber, firing chamber also has fuel channel and ft connection, firing chamber also has blast tube to be communicated with gas turbine, gas turbine also has blast tube to be communicated with exhaust heat boiler, exhaust heat boiler also have blast tube be communicated with generator and the second generator successively after the second generator have blast tube and ft connection again, steam turbine has low pressure steam passage to be communicated with heat exchanger, heat exchanger also has condensed fluid pipeline to be communicated with exhaust heat boiler through recycle pump, exhaust heat boiler also has high pressure steam passage to be communicated with steam turbine, heat exchanger also has heated medium pipeline and ft connection, compressor has refrigerant gas passage to be communicated with decompressor with regenerator through cooler, decompressor also has refrigerant gas passage to be communicated with compressor with regenerator through low temperature heat exchanger, low temperature heat exchanger also has cryogenic media pipeline and ft connection, and cooler also has heated medium pipeline and ft connection, vaporizer has refrigerant steam channel to be communicated with adsorber, adsorber also has dilute solution pipeline to be communicated with the second adsorber with solution heat exchanger through solution pump, second adsorber also has dilute solution pipeline to be communicated with generator with the second solution heat exchanger through the second solution pump, generator also has concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger, second generator also has concentrated solution pipeline to be communicated with adsorber through solution heat exchanger, generator also has refrigerant steam channel to be communicated with condenser, second generator also has refrigerant steam channel to be communicated with the second adsorber, condenser also has cryogen liquid pipeline to be communicated with vaporizer through throttle valve, vaporizer also has cryogenic media pipeline and ft connection, adsorber, second adsorber and condenser also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger form fuel gas-steam forward circulation system, compressor, cooler, decompressor, low temperature heat exchanger and regenerator form compression type reverse circulation system, and adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system, fuel gas-steam forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, fuel gas-steam forward circulation provides driving heat load to absorption reverse circulation, compression type reverse circulation obtains Low Temperature Thermal load and passes through the external heat supply of cooler, absorption reverse circulation obtains Low Temperature Thermal load and by adsorber, the second adsorber and the external heat supply of condenser, forms combined cycle energy supplying system.

16. combined cycle energy supplying systems, in the combined cycle energy supplying system described in the 15th, increase by the second compressor, had by compressor refrigerant gas passage to be communicated with decompressor through cooler and regenerator to be adjusted to compressor and to have refrigerant gas passage to be communicated with the second compressor through cooler, second compressor has refrigerant gas passage to be communicated with decompressor with regenerator through cooler again, forms combined cycle energy supplying system.

17. combined cycle energy supplying systems, formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, cooler, vaporizer, decompressor, low temperature heat exchanger, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, gas compressor has air passageways and ft connection, gas compressor also has compressed air channel and combustion chamber, firing chamber also has fuel channel and ft connection, firing chamber also has blast tube to be communicated with gas turbine, gas turbine also has blast tube to be communicated with exhaust heat boiler, exhaust heat boiler also have blast tube be communicated with generator and the second generator successively after the second generator have blast tube and ft connection again, steam turbine has low pressure steam passage to be communicated with heat exchanger, heat exchanger also has condensed fluid pipeline to be communicated with exhaust heat boiler through recycle pump, exhaust heat boiler also has high pressure steam passage to be communicated with steam turbine, heat exchanger also has heated medium pipeline and ft connection, compressor has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor again through the finisher that cooler is communicated with vaporizer, decompressor also has refrigerant gas passage to be communicated with compressor through low temperature heat exchanger, low temperature heat exchanger also has cryogenic media pipeline and ft connection, and cooler also has heated medium pipeline and ft connection, vaporizer also has refrigerant steam channel to be communicated with adsorber, adsorber also has dilute solution pipeline to be communicated with the second adsorber with solution heat exchanger through solution pump, second adsorber also has dilute solution pipeline to be communicated with generator with the second solution heat exchanger through the second solution pump, generator also has concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger, second generator also has concentrated solution pipeline to be communicated with adsorber through solution heat exchanger, generator also has refrigerant steam channel to be communicated with condenser, second generator also has refrigerant steam channel to be communicated with the second adsorber, condenser also has cryogen liquid pipeline to be communicated with vaporizer through throttle valve, adsorber, second adsorber and condenser also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger form fuel gas-steam forward circulation system, compressor, cooler, vaporizer, decompressor and low temperature heat exchanger form compression type reverse circulation system, and adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system, fuel gas-steam forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, fuel gas-steam forward circulation provides driving heat load to absorption reverse circulation, compression type reverse circulation obtain Low Temperature Thermal load and respectively by the external heat supply of cooler and by vaporizer to absorption reverse circulation heat supply, absorption reverse circulation, by adsorber, the second adsorber and the external heat supply of condenser, forms combined cycle energy supplying system.

18. combined cycle energy supplying systems, in the combined cycle energy supplying system described in the 17th, increase by the second compressor, refrigerant gas passage is had by compressor to have refrigerant gas passage to be communicated with decompressor to be again adjusted to compressor through the finisher that cooler is communicated with vaporizer and have refrigerant gas passage to have refrigerant gas passage to be communicated with the second compressor again through the finisher that cooler is communicated with vaporizer, second compressor also has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor again through the finisher that cooler is communicated with vaporizer, form combined cycle energy supplying system.

19. combined cycle energy supplying systems, formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, cooler, vaporizer, regenerator, decompressor, low temperature heat exchanger, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, gas compressor has air passageways and ft connection, gas compressor also has compressed air channel and combustion chamber, firing chamber also has fuel channel and ft connection, firing chamber also has blast tube to be communicated with gas turbine, gas turbine also has blast tube to be communicated with exhaust heat boiler, exhaust heat boiler also have blast tube be communicated with generator and the second generator successively after the second generator have blast tube and ft connection again, steam turbine has low pressure steam passage to be communicated with heat exchanger, heat exchanger also has condensed fluid pipeline to be communicated with exhaust heat boiler through recycle pump, exhaust heat boiler also has high pressure steam passage to be communicated with steam turbine, heat exchanger also has heated medium pipeline and ft connection, compressor has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor through regenerator again through the finisher that cooler is communicated with vaporizer, decompressor also has refrigerant gas passage to be communicated with compressor with regenerator through low temperature heat exchanger, low temperature heat exchanger also has cryogenic media pipeline and ft connection, and cooler also has heated medium pipeline and ft connection, vaporizer also has refrigerant steam channel to be communicated with adsorber, adsorber also has dilute solution pipeline to be communicated with the second adsorber with solution heat exchanger through solution pump, second adsorber also has dilute solution pipeline to be communicated with generator with the second solution heat exchanger through the second solution pump, generator also has concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger, second generator also has concentrated solution pipeline to be communicated with adsorber through solution heat exchanger, generator also has refrigerant steam channel to be communicated with condenser, second generator also has refrigerant steam channel to be communicated with the second adsorber, condenser also has cryogen liquid pipeline to be communicated with vaporizer through throttle valve, adsorber, second adsorber and condenser also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger form fuel gas-steam forward circulation system, compressor, cooler, vaporizer, regenerator, decompressor and low temperature heat exchanger form compression type reverse circulation system, and adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system, fuel gas-steam forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, fuel gas-steam forward circulation provides driving heat load to absorption reverse circulation, compression type reverse circulation obtain Low Temperature Thermal load and respectively by the external heat supply of cooler and by vaporizer to absorption reverse circulation heat supply, absorption reverse circulation, by adsorber, the second adsorber and the external heat supply of condenser, forms combined cycle energy supplying system.

20. combined cycle energy supplying systems, in the combined cycle energy supplying system described in the 19th, increase by the second compressor, had by compressor refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor through regenerator again through the finisher that cooler is communicated with vaporizer to be adjusted to compressor and to have refrigerant gas passage to have refrigerant gas passage to be communicated with the second compressor again through the finisher that cooler is communicated with vaporizer, second compressor also has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor through regenerator again through the finisher that cooler is communicated with vaporizer, form combined cycle energy supplying system.

21. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in 1-20 item, increase high temperature regenerator, there are by gas compressor compressed air channel and combustion chamber to be adjusted to gas compressor and have compressed air channel through high temperature regenerator and combustion chamber, being had by gas turbine blast tube to be communicated with exhaust heat boiler to be adjusted to gas turbine has blast tube to be communicated with exhaust heat boiler through high temperature regenerator, forms combined cycle energy supplying system.

22. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in 1-21 item, increase by the 3rd generator, second throttle, 3rd solution pump and the 3rd solution heat exchanger, second adsorber is set up dilute solution pipeline and is communicated with the 3rd generator with the 3rd solution heat exchanger through the 3rd solution pump, 3rd generator also has concentrated solution pipeline to be communicated with the second generator through the 3rd solution heat exchanger, had by generator refrigerant steam channel to be communicated with condenser to be adjusted to generator have refrigerant steam channel be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline to be communicated with condenser through second throttle again, 3rd generator also has refrigerant steam channel to be communicated with condenser, form combined cycle energy supplying system.

23. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in 1-21 item, increase by the 3rd generator, second throttle and the 3rd solution heat exchanger, had by second adsorber dilute solution pipeline to be communicated with generator through the second solution pump and the second solution heat exchanger to be adjusted to the second adsorber and to have dilute solution pipeline through the second solution pump, second solution heat exchanger is communicated with generator with the 3rd solution heat exchanger, had by generator concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger to be adjusted to generator and to have concentrated solution pipeline to be communicated with the 3rd generator through the 3rd solution heat exchanger, 3rd generator has concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger again, had by generator refrigerant steam channel to be communicated with condenser to be adjusted to generator have refrigerant steam channel be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline to be communicated with condenser through second throttle again, 3rd generator also has refrigerant steam channel to be communicated with condenser, form combined cycle energy supplying system.

24. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in 1-21 item, increase by the 3rd generator, second throttle, 3rd solution pump and the 3rd solution heat exchanger, had by second adsorber dilute solution pipeline to be communicated with generator through the second solution pump and the second solution heat exchanger to be adjusted to the second adsorber and to have dilute solution pipeline to be communicated with the 3rd generator with the second solution heat exchanger through the second solution pump, 3rd generator has concentrated solution pipeline to be communicated with generator with the 3rd solution heat exchanger through the 3rd solution pump again, had by generator concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger to be adjusted to generator and to have concentrated solution pipeline to be communicated with the second generator with the second solution heat exchanger through the 3rd solution heat exchanger, had by generator refrigerant steam channel to be communicated with condenser to be adjusted to generator have refrigerant steam channel be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline to be communicated with condenser through second throttle again, 3rd generator also has refrigerant steam channel to be communicated with condenser, form combined cycle energy supplying system.

25. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in 1-21 item, increase by the 3rd generator, second throttle, 3rd solution pump and the 3rd solution heat exchanger, generator is had blast tube be communicated with the second generator after the second generator have again blast tube and ft connection be adjusted to generator have blast tube be communicated with the 3rd generator and the second generator successively after the second generator have blast tube and ft connection again, second adsorber is set up dilute solution pipeline and is communicated with the 3rd generator with the 3rd solution heat exchanger through the 3rd solution pump, 3rd generator also has concentrated solution pipeline to be communicated with the second generator through the 3rd solution heat exchanger, had by generator refrigerant steam channel to be communicated with condenser to be adjusted to generator have refrigerant steam channel be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline to be communicated with condenser through second throttle again, 3rd generator also has refrigerant steam channel to be communicated with condenser, form combined cycle energy supplying system.

26. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in 1-21 item, increase by the 3rd generator, second throttle and the 3rd solution heat exchanger, generator is had blast tube be communicated with the second generator after the second generator have again blast tube and ft connection be adjusted to generator have blast tube be communicated with the 3rd generator and the second generator successively after the second generator have blast tube and ft connection again, had by second adsorber dilute solution pipeline to be communicated with generator through the second solution pump and the second solution heat exchanger to be adjusted to the second adsorber and to have dilute solution pipeline through the second solution pump, second solution heat exchanger is communicated with generator with the 3rd solution heat exchanger, had by generator concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger to be adjusted to generator and to have concentrated solution pipeline to be communicated with the 3rd generator through the 3rd solution heat exchanger, 3rd generator has concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger again, had by generator refrigerant steam channel to be communicated with condenser to be adjusted to generator have refrigerant steam channel be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline to be communicated with condenser through second throttle again, 3rd generator also has refrigerant steam channel to be communicated with condenser, form combined cycle energy supplying system.

27. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in 1-21 item, increase by the 3rd generator, second throttle, 3rd solution pump and the 3rd solution heat exchanger, generator is had blast tube be communicated with the second generator after the second generator have again blast tube and ft connection be adjusted to generator have blast tube be communicated with the 3rd generator and the second generator successively after the second generator have blast tube and ft connection again, had by second adsorber dilute solution pipeline to be communicated with generator through the second solution pump and the second solution heat exchanger to be adjusted to the second adsorber and to have dilute solution pipeline to be communicated with the 3rd generator with the second solution heat exchanger through the second solution pump, 3rd generator has concentrated solution pipeline to be communicated with generator with the 3rd solution heat exchanger through the 3rd solution pump again, had by generator concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger to be adjusted to generator and to have concentrated solution pipeline to be communicated with the second generator with the second solution heat exchanger through the 3rd solution heat exchanger, had by generator refrigerant steam channel to be communicated with condenser to be adjusted to generator have refrigerant steam channel be communicated with the 3rd generator after the 3rd generator have cryogen liquid pipeline to be communicated with condenser through second throttle again, 3rd generator also has refrigerant steam channel to be communicated with condenser, form combined cycle energy supplying system.

28. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in the 22nd, increase by the 4th generator, 3rd throttle valve, 4th solution pump and the 4th solution heat exchanger, second adsorber is set up dilute solution pipeline and is communicated with the 4th generator with the 4th solution heat exchanger through the 4th solution pump, 4th generator also has concentrated solution pipeline to be communicated with the second generator through the 4th solution heat exchanger, had by 3rd generator refrigerant steam channel to be communicated with condenser to be adjusted to the 3rd generator have refrigerant steam channel be communicated with the 4th generator after the 4th generator have cryogen liquid pipeline to be communicated with condenser through the 3rd throttle valve again, 4th generator also has refrigerant steam channel to be communicated with condenser, form combined cycle energy supplying system.

29. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in the 23rd, increase by the 4th generator, 3rd throttle valve and the 4th solution heat exchanger, second adsorber there is dilute solution pipeline through the second solution pump, second solution heat exchanger and the 3rd solution heat exchanger are communicated with generator and are adjusted to the second adsorber and have dilute solution pipeline through the second solution pump, second solution heat exchanger, 4th solution heat exchanger is communicated with generator with the 3rd solution heat exchanger, had by 3rd generator concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger to be adjusted to the 3rd generator and to have concentrated solution pipeline to be communicated with the 4th generator through the 4th solution heat exchanger, 4th generator has concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger again, had by 3rd generator refrigerant steam channel to be communicated with condenser to be adjusted to the 3rd generator have refrigerant steam channel be communicated with the 4th generator after the 4th generator have cryogen liquid pipeline to be communicated with condenser through the 3rd throttle valve again, 4th generator also has refrigerant steam channel to be communicated with condenser, form combined cycle energy supplying system.

30. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in the 24th, increase by the 4th generator, 3rd throttle valve, 4th solution pump and the 4th solution heat exchanger, had by second adsorber dilute solution pipeline to be communicated with the 3rd generator through the second solution pump and the second solution heat exchanger to be adjusted to the second adsorber and to have dilute solution pipeline to be communicated with the 4th generator with the second solution heat exchanger through the second solution pump, 4th generator has concentrated solution pipeline to be communicated with the 3rd generator with the 4th solution heat exchanger through the 4th solution pump again, had by generator concentrated solution pipeline to be communicated with the second generator through the 3rd solution heat exchanger and the second solution heat exchanger to be adjusted to generator and to have concentrated solution pipeline through the 3rd solution heat exchanger, 4th solution heat exchanger is communicated with the second generator with the second solution heat exchanger, had by 3rd generator refrigerant steam channel to be communicated with condenser to be adjusted to the 3rd generator have refrigerant steam channel be communicated with the 4th generator after the 4th generator have cryogen liquid pipeline to be communicated with condenser through the 3rd throttle valve again, 4th generator also has refrigerant steam channel to be communicated with condenser, form combined cycle energy supplying system.

31. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in the 22nd, increase by the 4th generator, 3rd throttle valve, 4th solution pump and the 4th solution heat exchanger, generator is had blast tube be communicated with the second generator after the second generator have blast tube and ft connection to be adjusted to generator again to have blast tube to be communicated with the 3rd generator successively, after 4th generator and the second generator, the second generator has blast tube and ft connection again, second adsorber is set up dilute solution pipeline and is communicated with the 4th generator with the 4th solution heat exchanger through the 4th solution pump, 4th generator also has concentrated solution pipeline to be communicated with the second generator through the 4th solution heat exchanger, had by 3rd generator refrigerant steam channel to be communicated with condenser to be adjusted to the 3rd generator have refrigerant steam channel be communicated with the 4th generator after the 4th generator have cryogen liquid pipeline to be communicated with condenser through the 3rd throttle valve again, 4th generator also has refrigerant steam channel to be communicated with condenser, form combined cycle energy supplying system.

32. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in the 23rd, increase by the 4th generator, 3rd throttle valve and the 4th solution heat exchanger, generator is had blast tube be communicated with the second generator after the second generator have blast tube and ft connection to be adjusted to generator again to have blast tube to be communicated with the 3rd generator successively, after 4th generator and the second generator, the second generator has blast tube and ft connection again, second adsorber there is dilute solution pipeline through the second solution pump, second solution heat exchanger and the 3rd solution heat exchanger are communicated with generator and are adjusted to the second adsorber and have dilute solution pipeline through the second solution pump, second solution heat exchanger, 4th solution heat exchanger is communicated with generator with the 3rd solution heat exchanger, had by 3rd generator concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger to be adjusted to the 3rd generator and to have concentrated solution pipeline to be communicated with the 4th generator through the 4th solution heat exchanger, 4th generator has concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger again, had by 3rd generator refrigerant steam channel to be communicated with condenser to be adjusted to the 3rd generator have refrigerant steam channel be communicated with the 4th generator after the 4th generator have cryogen liquid pipeline to be communicated with condenser through the 3rd throttle valve again, 4th generator also has refrigerant steam channel to be communicated with condenser, form combined cycle energy supplying system.

33. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in the 24th, increase by the 4th generator, 3rd throttle valve, 4th solution pump and the 4th solution heat exchanger, generator is had blast tube be communicated with the second generator after the second generator have blast tube and ft connection to be adjusted to generator again to have blast tube to be communicated with the 3rd generator successively, after 4th generator and the second generator, the second generator has blast tube and ft connection again, had by second adsorber dilute solution pipeline to be communicated with the 3rd generator through the second solution pump and the second solution heat exchanger to be adjusted to the second adsorber and to have dilute solution pipeline to be communicated with the 4th generator with the second solution heat exchanger through the second solution pump, 4th generator has concentrated solution pipeline to be communicated with the 3rd generator with the 4th solution heat exchanger through the 4th solution pump again, had by generator concentrated solution pipeline to be communicated with the second generator through the 3rd solution heat exchanger and the second solution heat exchanger to be adjusted to generator and to have concentrated solution pipeline through the 3rd solution heat exchanger, 4th solution heat exchanger is communicated with the second generator with the second solution heat exchanger, had by 3rd generator refrigerant steam channel to be communicated with condenser to be adjusted to the 3rd generator have refrigerant steam channel be communicated with the 4th generator after the 4th generator have cryogen liquid pipeline to be communicated with condenser through the 3rd throttle valve again, 4th generator also has refrigerant steam channel to be communicated with condenser, form combined cycle energy supplying system.

34. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in 28-33 item, there is by 3rd generator cryogen liquid pipeline to be communicated with condenser through second throttle to be adjusted to the 3rd generator and to have cryogen liquid pipeline to be communicated with condenser with second throttle through the 4th generator, form combined cycle energy supplying system.

35. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in 1-34 item, increase by the second heat exchanger, second heat exchanger has heated medium pipeline and ft connection, and takes following wherein arbitrary technical measures to form combined cycle energy supplying system: 1. had by the second generator blast tube and ft connection to be adjusted to the second generator and have blast tube through the second heat exchanger and ft connection; 2. there are by the second generator blast tube and ft connection to be adjusted to the second generator and have blast tube through the second heat exchanger and vaporizer and ft connection; 3. there are by the second generator blast tube and ft connection to be adjusted to the second generator and have blast tube through the second heat exchanger, vaporizer and low temperature heat exchanger and ft connection.

36. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in 1-21 item, increase by the 3rd generator, 3rd solution pump, 3rd solution heat exchanger and the 3rd adsorber, second generator is had blast tube and ft connection be adjusted to the second generator have blast tube be communicated with the 3rd generator after the 3rd generator have blast tube and ft connection again, being had by vaporizer refrigerant steam channel to be communicated with adsorber to be adjusted to vaporizer has refrigerant steam channel to be communicated with the 3rd adsorber, 3rd adsorber also has dilute solution pipeline to be communicated with the 3rd generator with the 3rd solution heat exchanger through the 3rd solution pump, 3rd generator also has concentrated solution pipeline to be communicated with the 3rd adsorber through the 3rd solution heat exchanger, 3rd generator also has refrigerant steam channel to be communicated with adsorber, 3rd adsorber also has heated medium pipeline and ft connection, form combined cycle energy supplying system.

37. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in the 36th, increase by the second heat exchanger, second heat exchanger has heated medium pipeline and ft connection, and takes following wherein arbitrary technical measures to form combined cycle energy supplying system: 1. had by the 3rd generator blast tube and ft connection to be adjusted to the 3rd generator and have blast tube through the second heat exchanger and ft connection; 2. there are by the 3rd generator blast tube and ft connection to be adjusted to the 3rd generator and have blast tube through the second heat exchanger and vaporizer and ft connection; 3. there are by the 3rd generator blast tube and ft connection to be adjusted to the 3rd generator and have blast tube through the second heat exchanger, vaporizer and low temperature heat exchanger and ft connection.

38. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in 1-21 item, increase high-temperature heat exchanger and the second recycle pump, exhaust heat boiler is had blast tube be communicated with successively generator and the second generator after the second generator have again blast tube and ft connection be adjusted to exhaust heat boiler have blast tube be communicated with high-temperature heat exchanger after high-temperature heat exchanger have blast tube and ft connection again, high-temperature heat exchanger, the second recycle pump and circulating thermal medium pipeline is relied on to form closed loop between generator and the second generator, form combined cycle energy supplying system.

39. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in the 38th, increase by the second heat exchanger, second heat exchanger has heated medium pipeline and ft connection, and take following wherein technical measures to form combined cycle energy supplying system: 1. by high-temperature heat exchanger, rely on the second recycle pump and circulating thermal medium pipeline to form closed loop between generator and the second generator and be adjusted to high-temperature heat exchanger, generator, the second recycle pump and circulating thermal medium pipeline is relied on to form closed loop between second generator and the second heat exchanger, 2. by high-temperature heat exchanger, rely on the second recycle pump and circulating thermal medium pipeline to form closed loop between generator and the second generator to be adjusted to high-temperature heat exchanger, generator, the second generator, between the second heat exchanger and vaporizer, to rely on the second recycle pump and circulating thermal medium pipeline to form closed loop, 3. by high-temperature heat exchanger, rely on the second recycle pump and circulating thermal medium pipeline to form closed loop between generator and the second generator to be adjusted to high-temperature heat exchanger, generator, the second generator, the second heat exchanger, between vaporizer and low temperature heat exchanger, to rely on the second recycle pump and circulating thermal medium pipeline to form closed loop.

40. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in 1-21 item, increase high-temperature heat exchanger, second recycle pump, 3rd generator, 3rd solution pump, 3rd solution heat exchanger and the 3rd adsorber, exhaust heat boiler is had blast tube be communicated with successively generator and the second generator after the second generator have again blast tube and ft connection be adjusted to exhaust heat boiler have blast tube be communicated with high-temperature heat exchanger after high-temperature heat exchanger have blast tube and ft connection again, high-temperature heat exchanger, generator, the second recycle pump and circulating thermal medium pipeline is relied on to form closed loop between second generator and the 3rd generator, being had by vaporizer refrigerant steam channel to be communicated with adsorber to be adjusted to vaporizer has refrigerant steam channel to be communicated with the 3rd adsorber, 3rd adsorber also has dilute solution pipeline to be communicated with the 3rd generator with the 3rd solution heat exchanger through the 3rd solution pump, 3rd generator also has concentrated solution pipeline to be communicated with the 3rd adsorber through the 3rd solution heat exchanger, 3rd generator also has refrigerant steam channel to be communicated with adsorber, 3rd adsorber also has heated medium pipeline and ft connection, forms combined cycle energy supplying system.

41. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in 1-40 item, increase working machine, fuel gas-steam forward circulation provides power respectively to working machine, provides power and provide driving heat load to absorption reverse circulation to compression type reverse circulation, forms combined cycle energy supplying system.

Accompanying drawing illustrates:

Fig. 1 is according to combined cycle energy supplying system provided by the present invention 1st kind of principled thermal system figure.

Fig. 2 is according to combined cycle energy supplying system provided by the present invention 2nd kind of principled thermal system figure.

Fig. 3 is according to combined cycle energy supplying system provided by the present invention 3rd kind of principled thermal system figure.

Fig. 4 is according to combined cycle energy supplying system provided by the present invention 4th kind of principled thermal system figure.

Fig. 5 is according to combined cycle energy supplying system provided by the present invention 5th kind of principled thermal system figure.

Fig. 6 is according to combined cycle energy supplying system provided by the present invention 6th kind of principled thermal system figure.

Fig. 7 is according to combined cycle energy supplying system provided by the present invention 7th kind of principled thermal system figure.

Fig. 8 is according to combined cycle energy supplying system provided by the present invention 8th kind of principled thermal system figure.

Fig. 9 is according to combined cycle energy supplying system provided by the present invention 9th kind of principled thermal system figure.

Figure 10 is according to combined cycle energy supplying system provided by the present invention 10th kind of principled thermal system figure.

Figure 11 is according to combined cycle energy supplying system provided by the present invention 11st kind of principled thermal system figure.

Figure 12 is according to combined cycle energy supplying system provided by the present invention 12nd kind of principled thermal system figure.

Figure 13 is according to combined cycle energy supplying system provided by the present invention 13rd kind of principled thermal system figure.

Figure 14 is according to combined cycle energy supplying system provided by the present invention 14th kind of principled thermal system figure.

Figure 15 is according to combined cycle energy supplying system provided by the present invention 15th kind of principled thermal system figure.

Figure 16 is according to combined cycle energy supplying system provided by the present invention 16th kind of principled thermal system figure.

Figure 17 is according to combined cycle energy supplying system provided by the present invention 17th kind of principled thermal system figure.

Figure 18 is according to combined cycle energy supplying system provided by the present invention 18th kind of principled thermal system figure.

Figure 19 is according to combined cycle energy supplying system provided by the present invention 19th kind of principled thermal system figure.

Figure 20 is according to combined cycle energy supplying system provided by the present invention 20th kind of principled thermal system figure.

Figure 21 is according to combined cycle energy supplying system provided by the present invention 21st kind of principled thermal system figure.

Figure 22 is according to combined cycle energy supplying system provided by the present invention 22nd kind of principled thermal system figure.

Figure 23 is according to combined cycle energy supplying system provided by the present invention 23rd kind of principled thermal system figure.

Figure 24 is according to combined cycle energy supplying system provided by the present invention 24th kind of principled thermal system figure.

Figure 25 is according to combined cycle energy supplying system provided by the present invention 25th kind of principled thermal system figure.

Figure 26 is according to combined cycle energy supplying system provided by the present invention 26th kind of principled thermal system figure.

Figure 27 is according to combined cycle energy supplying system provided by the present invention 27th kind of principled thermal system figure.

Figure 28 is according to combined cycle energy supplying system provided by the present invention 28th kind of principled thermal system figure.

Figure 29 is according to combined cycle energy supplying system provided by the present invention 29th kind of principled thermal system figure.

Figure 30 is according to combined cycle energy supplying system provided by the present invention 30th kind of principled thermal system figure.

Figure 31 is according to combined cycle energy supplying system provided by the present invention 31st kind of principled thermal system figure.

In figure, A-gas compressor, B-firing chamber, C-gas turbine, D-steam turbine, E-exhaust heat boiler, F-recycle pump, G-heat exchanger, H-compressor, I-cryogenic throttle valve, J-low temperature heat exchanger, K-second compressor, L-second condenser, M-cooler, N-second cryogenic throttle valve, O-decompressor, P-regenerator, Q-high temperature regenerator, R-high-temperature heat exchanger, S-second recycle pump, T-working machine; 1-adsorber, 2-second adsorber, 3-generator, 4-second generator, 5-condenser, 6-vaporizer, 7-throttle valve, 8-solution pump, 9-second solution pump, 10-solution heat exchanger, 11-second solution heat exchanger, 12-heat exchanger, 13-the 3rd generator, 14-second throttle, 15-the 3rd solution pump, 16-the 3rd solution heat exchanger, 17-the 3rd generator, 18-the 3rd throttle valve, 19-the 4th solution pump, 20-the 4th solution heat exchanger, 21-the 3rd adsorber.

Here also following explanation to be provided:

(1) vaporizer---from absorption reverse circulation angle name, be vaporizer in absorption reverse circulation, in compression type reverse circulation, do condenser or cooler use.

(2) throttle valve---by called after cryogenic throttle valve and the second cryogenic throttle valve respectively of the throttle valve in compression type reverse circulation, by called after throttle valve, second throttle and the 3rd throttle valve respectively of the throttle valve in absorption reverse circulation.

(3) compressor and gas compressor---the compressor of the pressurized air in gas turbine installation is referred to as gas compressor, the compressor of compression work medium in reverse circulation is referred to as compressor.

(4) working medium---claim refrigerant vapour by the gaseous working medium in compressed steam circulation and Absorption heat-transformer, liquid refrigerant claims cryogen liquid, and the working medium in being circulated by pressurized gas claims refrigerant gas; Condensed fluid is claimed, as solidifying water or other liquid medium by the liquid refrigerant in Steam Power Circulation.

(5) regenerator---by the regenerator called after regenerator in compression type reverse circulation, by the regenerator called after high temperature regenerator in gas turbine installation.

(6) flow process and the structure of flesh and blood of the present invention is not related to, not in express ranges of the present invention.

(7) condenser and cooler---working medium release latent heat is that main heat exchanger claims condenser, and working medium release sensible heat is that main heat exchanger claims cooler.

Embodiment:

First be noted that in the statement of structure and flow process, do not repeat in inessential situation; Apparent flow process is not stated.The present invention is described in detail below in conjunction with accompanying drawing and example.

The energy supplying system of combined cycle shown in Fig. 1 is achieved in that

(1), in structure, it formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, vaporizer, cryogenic throttle valve, low temperature heat exchanger, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and working machine, gas compressor A has air passageways and ft connection, gas compressor A also has compressed air channel to be communicated with firing chamber B, firing chamber B also has fuel channel and ft connection, firing chamber B also has blast tube to be communicated with gas turbine C, gas turbine C also has blast tube to be communicated with exhaust heat boiler E, exhaust heat boiler E also have blast tube be communicated with generator 3 and the second generator 4 successively after the second generator 4 have blast tube and ft connection again, steam turbine D has low pressure steam passage to be communicated with heat exchanger G, heat exchanger G also has condensed fluid pipeline to be communicated with exhaust heat boiler E through recycle pump F, exhaust heat boiler E also has high pressure steam passage to be communicated with steam turbine D, heat exchanger G also has heated medium pipeline and ft connection, the finisher 6 that compressor H has refrigerant steam channel to be communicated with vaporizer 6 has cryogen liquid pipeline to be communicated with low temperature heat exchanger J through cryogenic throttle valve I again, low temperature heat exchanger J also has refrigerant steam channel to be communicated with compressor H, and low temperature heat exchanger J also has cryogenic media pipeline and ft connection, vaporizer 6 also has refrigerant steam channel to be communicated with adsorber 1, adsorber 1 also has dilute solution pipeline to be communicated with the second adsorber 2 with solution heat exchanger 10 through solution pump 8, second adsorber 2 also has dilute solution pipeline to be communicated with generator 3 with the second solution heat exchanger 11 through the second solution pump 9, generator 3 also has concentrated solution pipeline to be communicated with the second generator 4 through the second solution heat exchanger 11, second generator 4 also has concentrated solution pipeline to be communicated with adsorber 1 through solution heat exchanger 10, generator 3 also has refrigerant steam channel to be communicated with condenser 5, second generator 4 also has refrigerant steam channel to be communicated with the second adsorber 2, condenser 5 also has cryogen liquid pipeline to be communicated with vaporizer 6 through throttle valve 7, adsorber 1, second adsorber 2 and condenser 5 also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger and working machine form fuel gas-steam forward circulation system, compressor, vaporizer, cryogenic throttle valve and low temperature heat exchanger form compression type reverse circulation system, and adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system.

(2) in flow process, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger carry out fuel gas-steam forward circulation---and air enters gas compressor A, compressed boosting enters firing chamber B after heating up, fuel enters firing chamber and with pressurized air mixed combustion or carry out secondary with air more afterwards and mix, high-temperature fuel gas enters gas turbine C step-down work done, gas flow after work done is through exhaust heat boiler E, generator 3 and the second generator 4 do driving thermal medium is supplied to after heat release cooling, the high pressure steam that exhaust heat boiler E produces enters steam turbine D step-down work done, the low pressure steam that steam turbine E discharges enters heat exchanger G, heat release becomes condensed fluid in heated medium, condensed fluid is supplied to exhaust heat boiler E after recycle pump F pressurizes, absorb heat into high pressure steam and provide to steam turbine D, compressor, vaporizer, cryogenic throttle valve and low temperature heat exchanger carry out compression type reverse circulation---and refrigerant vapour enters compressor H, boosting flows through vaporizer 6 after heating up and heat release becomes cryogen liquid, and cryogen liquid enters low temperature heat exchanger J, absorbs heat into refrigerant vapour and provide to compressor H after cryogenic throttle valve I throttling, adsorber, second adsorber, generator, second generator, condenser, vaporizer, throttle valve, solution pump, second solution pump, solution heat exchanger and the second solution heat exchanger carry out absorption reverse circulation---and the dilute solution of adsorber 1 enters the second adsorber 2 through solution pump 8 and solution heat exchanger 10, absorb refrigerant vapour heat release in heated medium, the dilute solution of the second adsorber 2 enters generator 3 through the second solution pump 9 and the second solution heat exchanger 11, heat absorption release refrigerant vapour also provides to condenser 5, and the concentrated solution of generator 3 enters the second generator 4 through the second solution heat exchanger 11, heat absorption release refrigerant vapour also provides to the second adsorber 2, and the concentrated solution of the second generator 4 enters adsorber 1 through solution heat exchanger 10, absorb refrigerant vapour heat release in heated medium, the refrigerant vapour heat release of condenser 5 becomes cryogen liquid in heated medium, and the cryogen liquid of condenser 5 enters vaporizer 6 through throttle valve 7 throttling, absorb heat into refrigerant vapour and provide to adsorber 1, fuel gas-steam forward circulation provides power respectively to working machine and compression type reverse circulation, fuel gas-steam forward circulation provides driving heat load to absorption reverse circulation, compression type reverse circulation obtains Low Temperature Thermal load by vaporizer to absorption reverse circulation heat supply, absorption reverse circulation, by adsorber, the second adsorber and the external heat supply of condenser, forms combined cycle energy supplying system.

The energy supplying system of combined cycle shown in Fig. 2 is achieved in that

In the energy supplying system of combined cycle shown in Fig. 1, increase by the second compressor, the finisher 6 being had by compressor H refrigerant steam channel to be communicated with vaporizer 6 has cryogen liquid pipeline to be communicated with through cryogenic throttle valve I the finisher 6 being adjusted to compressor H and having refrigerant steam channel to be communicated with vaporizer 6 with low temperature heat exchanger J again has refrigerant steam channel to be communicated with the second compressor K again, and the finisher 6 that the second compressor K also has refrigerant steam channel to be communicated with vaporizer 6 has cryogen liquid pipeline to be communicated with low temperature heat exchanger J through cryogenic throttle valve I again; The refrigerant vapour that compressor H produces enters the second compressor K after flowing through vaporizer 6 heat release cooling, and the refrigerant vapour that the second compressor K produces provides to vaporizer 6, forms combined cycle energy supplying system.

The energy supplying system of combined cycle shown in Fig. 3 is achieved in that

(1), in structure, it formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, the second condenser, cryogenic throttle valve, low temperature heat exchanger, vaporizer, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, gas compressor A has air passageways and ft connection, gas compressor A also has compressed air channel to be communicated with firing chamber B, firing chamber B also has fuel channel and ft connection, firing chamber B also has blast tube to be communicated with gas turbine C, gas turbine C also has blast tube to be communicated with exhaust heat boiler E, exhaust heat boiler E also have blast tube be communicated with generator 3 and the second generator 4 successively after the second generator 4 have blast tube and ft connection again, steam turbine D has low pressure steam passage to be communicated with heat exchanger G, heat exchanger G also has condensed fluid pipeline to be communicated with exhaust heat boiler E through recycle pump F, exhaust heat boiler E also has high pressure steam passage to be communicated with steam turbine D, heat exchanger G also has heated medium pipeline and ft connection, compressor H have refrigerant steam channel be communicated with the second condenser L after the second condenser L have cryogen liquid pipeline to be communicated with low temperature heat exchanger J through cryogenic throttle valve I again, low temperature heat exchanger J also has refrigerant steam channel to be communicated with compressor H, low temperature heat exchanger J also has cryogenic media pipeline and ft connection, and the second condenser L also has heated medium pipeline and ft connection, vaporizer 6 has refrigerant steam channel to be communicated with adsorber 1, adsorber 1 also has dilute solution pipeline to be communicated with the second adsorber 2 with solution heat exchanger 10 through solution pump 8, second adsorber 2 also has dilute solution pipeline to be communicated with generator 3 with the second solution heat exchanger 11 through the second solution pump 9, generator 3 also has concentrated solution pipeline to be communicated with the second generator 4 through the second solution heat exchanger 11, second generator 4 also has concentrated solution pipeline to be communicated with adsorber 1 through solution heat exchanger 10, generator 3 also has refrigerant steam channel to be communicated with condenser 5, second generator 4 also has refrigerant steam channel to be communicated with the second adsorber 2, condenser 5 also has cryogen liquid pipeline to be communicated with vaporizer 6 through throttle valve 7, vaporizer 6 also has cryogenic media pipeline and ft connection, adsorber 1, second adsorber 2 and condenser 5 also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger form fuel gas-steam forward circulation system, compressor, the second condenser, cryogenic throttle valve and low temperature heat exchanger form compression type reverse circulation system, and adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system.

(2) in flow process, with the energy supplying system of combined cycle shown in Fig. 1, except without except working machine, difference is: compressor, the second condenser, cryogenic throttle valve and low temperature heat exchanger carry out compression type reverse circulation---refrigerant vapour enters compressor H, boosting flows through the second condenser L after heating up and heat release becomes cryogen liquid in heated medium, and cryogen liquid enters low temperature heat exchanger J, absorbs heat into refrigerant vapour and provide to compressor H after cryogenic throttle valve I throttling; Vaporizer 6 directly obtains Low Temperature Thermal load from cryogenic media.

The energy supplying system of combined cycle shown in Fig. 4 is achieved in that

In the energy supplying system of combined cycle shown in Fig. 3, increase by the second compressor, compressor H is had refrigerant steam channel be communicated with the second condenser L after the second condenser L have again cryogen liquid pipeline through cryogenic throttle valve I to be communicated with low temperature heat exchanger J be adjusted to compressor H have refrigerant steam channel to be communicated with the second condenser L after the second condenser L have refrigerant steam channel to be communicated with the second compressor K again, the second compressor K also have refrigerant steam channel be communicated with the second condenser L after the second condenser L have cryogen liquid pipeline to be communicated with low temperature heat exchanger J through cryogenic throttle valve I again; The refrigerant vapour that compressor H produces enters the second compressor K after flowing through the second condenser L heat release cooling, and the refrigerant vapour that the second compressor K produces provides to the second condenser L again, forms combined cycle energy supplying system.

The energy supplying system of combined cycle shown in Fig. 5 is achieved in that

(1), in structure, it formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, cooler, vaporizer, cryogenic throttle valve, low temperature heat exchanger, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and working machine, gas compressor A has air passageways and ft connection, gas compressor A also has compressed air channel to be communicated with firing chamber B, firing chamber B also has fuel channel and ft connection, firing chamber B also has blast tube to be communicated with gas turbine C, gas turbine C also has blast tube to be communicated with exhaust heat boiler E, exhaust heat boiler E also have blast tube be communicated with generator 3 and the second generator 4 successively after the second generator 4 have blast tube and ft connection again, steam turbine D has low pressure steam passage to be communicated with heat exchanger G, heat exchanger G also has condensed fluid pipeline to be communicated with exhaust heat boiler E through recycle pump F, exhaust heat boiler E also has high pressure steam passage to be communicated with steam turbine D, heat exchanger G also has heated medium pipeline and ft connection, the aftercooler M that compressor H has refrigerant steam channel to be communicated with cooler M has refrigerant steam channel to be communicated with vaporizer 6 again, vaporizer 6 also has cryogen liquid pipeline to be communicated with low temperature heat exchanger J through cryogenic throttle valve I, low temperature heat exchanger J also has refrigerant steam channel to be communicated with compressor H, low temperature heat exchanger J also has cryogenic media pipeline and ft connection, and cooler M also has heated medium pipeline and ft connection, vaporizer 6 also has refrigerant steam channel to be communicated with adsorber 1, adsorber 1 also has dilute solution pipeline to be communicated with the second adsorber 2 with solution heat exchanger 10 through solution pump 8, second adsorber 2 also has dilute solution pipeline to be communicated with generator 3 with the second solution heat exchanger 11 through the second solution pump 9, generator 3 also has concentrated solution pipeline to be communicated with the second generator 4 through the second solution heat exchanger 11, second generator 4 also has concentrated solution pipeline to be communicated with adsorber 1 through solution heat exchanger 10, generator 3 also has refrigerant steam channel to be communicated with condenser 5, second generator 4 also has refrigerant steam channel to be communicated with the second adsorber 2, condenser 5 also has cryogen liquid pipeline to be communicated with vaporizer 6 through throttle valve 7, adsorber 1, second adsorber 2 and condenser 5 also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger and working machine form fuel gas-steam forward circulation system, compressor, cooler, vaporizer, cryogenic throttle valve and low temperature heat exchanger form compression type reverse circulation system, and adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system.

(2) in flow process, compared with the energy supplying system of combined cycle shown in Fig. 1, except without except working machine, difference is: compressor, cooler, vaporizer, cryogenic throttle valve and low temperature heat exchanger carry out compression type reverse circulation---refrigerant vapour enters compressor H, boosting flows through cooler M after heating up and heat release cooling, refrigerant vapour after cooling flows through vaporizer 6 heat release and becomes cryogen liquid, and cryogen liquid enters low temperature heat exchanger J, absorbs heat into refrigerant vapour and provide to compressor H after cryogenic throttle valve I throttling.

The energy supplying system of combined cycle shown in Fig. 6 is achieved in that

In the energy supplying system of combined cycle shown in Fig. 5, increase by the second compressor, the aftercooler M being had by compressor H refrigerant steam channel to be communicated with cooler M has refrigerant steam channel to be communicated with vaporizer 6 to be adjusted to compressor H the aftercooler M having refrigerant steam channel to be communicated with cooler M to have refrigerant steam channel to be communicated with the second compressor K more again, and the aftercooler M that the second compressor K also has refrigerant steam channel to be communicated with cooler M has refrigerant steam channel to be communicated with vaporizer 6 again; The refrigerant vapour that compressor H produces is supplied to the second compressor K after flowing through cooler M heat release cooling, and the refrigerant vapour that the second compressor K produces is supplied to vaporizer 6 after flowing through cooler M heat release cooling, forms combined cycle energy supplying system.

The energy supplying system of combined cycle shown in Fig. 7 is achieved in that

(1), in structure, it formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, the second compressor, the second condenser, vaporizer, cryogenic throttle valve, the second cryogenic throttle valve, low temperature heat exchanger, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, gas compressor A has air passageways and ft connection, gas compressor A also has compressed air channel to be communicated with firing chamber B, firing chamber B also has fuel channel and ft connection, firing chamber B also has blast tube to be communicated with gas turbine C, gas turbine C also has blast tube to be communicated with exhaust heat boiler E, exhaust heat boiler E also have blast tube be communicated with generator 3 and the second generator 4 successively after the second generator 4 have blast tube and ft connection again, steam turbine D has low pressure steam passage to be communicated with heat exchanger G, heat exchanger G also has condensed fluid pipeline to be communicated with exhaust heat boiler E through recycle pump F, exhaust heat boiler E also has high pressure steam passage to be communicated with steam turbine D, heat exchanger G also has heated medium pipeline and ft connection, compressor H has low pressure refrigerant steam channel to be communicated with vaporizer 6, vaporizer 6 also has low pressure cryogen liquid pipeline low temperature heat exchanger J after cryogenic throttle valve I is communicated with low temperature heat exchanger J to have refrigerant steam channel to be communicated with compressor H again, compressor H also has low pressure refrigerant steam channel to be communicated with the second compressor K, second compressor K also has high pressure refrigerant steam channel to be communicated with the second condenser L, second condenser L also has high pressure cryogen liquid pipeline low temperature heat exchanger J after vaporizer 6 and the second cryogenic throttle valve N are communicated with low temperature heat exchanger J to have refrigerant steam channel to be communicated with compressor H again, low temperature heat exchanger J also has cryogenic media pipeline and ft connection, second condenser L also has heated medium pipeline and ft connection, vaporizer 6 also has refrigerant steam channel to be communicated with adsorber 1, adsorber 1 also has dilute solution pipeline to be communicated with the second adsorber 2 with solution heat exchanger 10 through solution pump 8, second adsorber 2 also has dilute solution pipeline to be communicated with generator 3 with the second solution heat exchanger 11 through the second solution pump 9, generator 3 also has concentrated solution pipeline to be communicated with the second generator 4 through the second solution heat exchanger 11, second generator 4 also has concentrated solution pipeline to be communicated with adsorber 1 through solution heat exchanger 10, generator 3 also has refrigerant steam channel to be communicated with condenser 5, second generator 4 also has refrigerant steam channel to be communicated with the second adsorber 2, condenser 5 also has cryogen liquid pipeline to be communicated with vaporizer 6 through throttle valve 7, adsorber 1, second adsorber 2 and condenser 5 also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger form fuel gas-steam forward circulation system, and compressor, the second compressor, the second condenser, vaporizer, cryogenic throttle valve, the second cryogenic throttle valve and low temperature heat exchanger form compression type reverse circulation system, adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system.

(2) in flow process, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger carry out fuel gas-steam forward circulation---and air enters gas compressor A, compressed boosting enters firing chamber B after heating up, fuel enters firing chamber and with pressurized air mixed combustion or carry out secondary with air more afterwards and mix, high-temperature fuel gas enters gas turbine C step-down work done, gas flow after work done is through exhaust heat boiler E, generator 3 and the second generator 4 do driving thermal medium is supplied to after heat release cooling, the high pressure steam that exhaust heat boiler E produces enters steam turbine D step-down work done, the low pressure steam that steam turbine E discharges enters heat exchanger G, heat release becomes condensed fluid in heated medium, condensed fluid is supplied to exhaust heat boiler E after recycle pump F pressurizes, absorb heat into high pressure steam and provide to steam turbine D, compressor, second compressor, second condenser, vaporizer, cryogenic throttle valve, second cryogenic throttle valve and low temperature heat exchanger carry out compression type reverse circulation---and refrigerant vapour enters compressor H, the rear portion of compressed one-tenth low pressure refrigerant vapour is supplied to the second compressor K, another part flows through vaporizer 6 and heat release enters low temperature heat exchanger J through cryogenic throttle valve I throttling after becoming low pressure cryogen liquid again, absorb heat into refrigerant vapour and provide to compressor H, the high pressure refrigerant vapour that second compressor K produces flows through the second condenser L and heat release becomes high pressure cryogen liquid in heated medium, high pressure cryogen liquid flows through after vaporizer 6 is lowered the temperature and enters low temperature heat exchanger J through the second cryogenic throttle valve N throttling again, absorb heat into refrigerant vapour and provide to compressor H, adsorber, second adsorber, generator, second generator, condenser, vaporizer, throttle valve, solution pump, second solution pump, solution heat exchanger and the second solution heat exchanger carry out absorption reverse circulation---and the dilute solution of adsorber 1 enters the second adsorber 2 through solution pump 8 and solution heat exchanger 10, absorb refrigerant vapour heat release in heated medium, the dilute solution of the second adsorber 2 enters generator 3 through the second solution pump 9 and the second solution heat exchanger 11, heat absorption release refrigerant vapour also provides to condenser 5, and the concentrated solution of generator 3 enters the second generator 4 through the second solution heat exchanger 11, heat absorption release refrigerant vapour also provides to the second adsorber 2, and the concentrated solution of the second generator 4 enters adsorber 1 through solution heat exchanger 10, absorb refrigerant vapour heat release in heated medium, the refrigerant vapour heat release of condenser 5 becomes cryogen liquid in heated medium, and the cryogen liquid of condenser 5 enters vaporizer 6 through throttle valve 7 throttling, absorb heat into refrigerant vapour and provide to adsorber 1, fuel gas-steam forward circulation provides power respectively to compression type reverse circulation and provides driving heat load to absorption reverse circulation, compression type reverse circulation obtain Low Temperature Thermal load and respectively by the external heat supply of the second condenser and by vaporizer to absorption reverse circulation heat supply, absorption reverse circulation, by adsorber, the second adsorber and the external heat supply of condenser, forms combined cycle energy supplying system.

The energy supplying system of combined cycle shown in Fig. 8 is achieved in that

(1), in structure, it formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, the second condenser, vaporizer, cryogenic throttle valve, the second cryogenic throttle valve, low temperature heat exchanger, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, gas compressor A has air passageways and ft connection, gas compressor A also has compressed air channel to be communicated with firing chamber B, firing chamber B also has fuel channel and ft connection, firing chamber B also has blast tube to be communicated with gas turbine C, gas turbine C also has blast tube to be communicated with exhaust heat boiler E, exhaust heat boiler E also have blast tube be communicated with generator 3 and the second generator 4 successively after the second generator 4 have blast tube and ft connection again, steam turbine D has low pressure steam passage to be communicated with heat exchanger G, heat exchanger G also has condensed fluid pipeline to be communicated with exhaust heat boiler E through recycle pump F, exhaust heat boiler E also has high pressure steam passage to be communicated with steam turbine D, heat exchanger G also has heated medium pipeline and ft connection, compressor H has low pressure refrigerant steam channel to be communicated with vaporizer 6, vaporizer 6 also has low pressure cryogen liquid pipeline low temperature heat exchanger J after cryogenic throttle valve I is communicated with low temperature heat exchanger J to have refrigerant steam channel to be communicated with compressor H again, compressor H also has high pressure refrigerant steam channel to be communicated with the second condenser L, second condenser L also has high pressure cryogen liquid pipeline low temperature heat exchanger J after vaporizer 6 and the second cryogenic throttle valve N are communicated with low temperature heat exchanger J to have refrigerant steam channel to be communicated with compressor H again, low temperature heat exchanger J also has cryogenic media pipeline and ft connection, second condenser L also has heated medium pipeline and ft connection, vaporizer 6 also has refrigerant steam channel to be communicated with adsorber 1, adsorber 1 also has dilute solution pipeline to be communicated with the second adsorber 2 with solution heat exchanger 10 through solution pump 8, second adsorber 2 also has dilute solution pipeline to be communicated with generator 3 with the second solution heat exchanger 11 through the second solution pump 9, generator 3 also has concentrated solution pipeline to be communicated with the second generator 4 through the second solution heat exchanger 11, second generator 4 also has concentrated solution pipeline to be communicated with adsorber 1 through solution heat exchanger 10, generator 3 also has refrigerant steam channel to be communicated with condenser 5, second generator 4 also has refrigerant steam channel to be communicated with the second adsorber 2, condenser 5 also has cryogen liquid pipeline to be communicated with vaporizer 6 through throttle valve 7, adsorber 1, second adsorber 2 and condenser 5 also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger form fuel gas-steam forward circulation system, compressor, the second condenser, vaporizer, cryogenic throttle valve, the second cryogenic throttle valve and low temperature heat exchanger form compression type reverse circulation system, and adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system.

(2) in flow process, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger carry out fuel gas-steam forward circulation---and air enters gas compressor A, compressed boosting enters firing chamber B after heating up, fuel enters firing chamber and with pressurized air mixed combustion or carry out secondary with air more afterwards and mix, high-temperature fuel gas enters gas turbine C step-down work done, gas flow after work done is through exhaust heat boiler E, generator 3 and the second generator 4 do driving thermal medium is supplied to after heat release cooling, the high pressure steam that exhaust heat boiler E produces enters steam turbine D step-down work done, the low pressure steam that steam turbine E discharges enters heat exchanger G, heat release becomes condensed fluid in heated medium, condensed fluid is supplied to exhaust heat boiler E after recycle pump F pressurizes, absorb heat into high pressure steam and provide to steam turbine D, compressor, second condenser, vaporizer, cryogenic throttle valve, second cryogenic throttle valve and low temperature heat exchanger carry out compression type reverse circulation---and refrigerant vapour enters compressor H, two-part are divided into after compressed one-tenth low pressure refrigerant vapour, wherein a part continues to be compressed into high pressure refrigerant vapour, another part flows through vaporizer 6 and heat release becomes low pressure cryogen liquid, low pressure cryogen liquid enters low temperature heat exchanger J through cryogenic throttle valve I throttling again, absorb heat into refrigerant vapour and provide to compressor H, the high pressure refrigerant vapour that compressor H produces flows through the second condenser L and heat release becomes high pressure cryogen liquid in heated medium, high pressure cryogen liquid flows through after vaporizer 6 is lowered the temperature and enters low temperature heat exchanger J through the second cryogenic throttle valve N throttling again, absorb heat into refrigerant vapour and provide to compressor H, adsorber, second adsorber, generator, second generator, condenser, vaporizer, throttle valve, solution pump, second solution pump, solution heat exchanger and the second solution heat exchanger carry out absorption reverse circulation---and the dilute solution of adsorber 1 enters the second adsorber 2 through solution pump 8 and solution heat exchanger 10, absorb refrigerant vapour heat release in heated medium, the dilute solution of the second adsorber 2 enters generator 3 through the second solution pump 9 and the second solution heat exchanger 11, heat absorption release refrigerant vapour also provides to condenser 5, and the concentrated solution of generator 3 enters the second generator 4 through the second solution heat exchanger 11, heat absorption release refrigerant vapour also provides to the second adsorber 2, and the concentrated solution of the second generator 4 enters adsorber 1 through solution heat exchanger 10, absorb refrigerant vapour heat release in heated medium, the refrigerant vapour heat release of condenser 5 becomes cryogen liquid in heated medium, and the cryogen liquid of condenser 5 enters vaporizer 6 through throttle valve 7 throttling, absorb heat into refrigerant vapour and provide to adsorber 1, fuel gas-steam forward circulation provides power respectively to compression type reverse circulation and provides driving heat load to absorption reverse circulation, compression type reverse circulation obtain Low Temperature Thermal load and respectively by the external heat supply of the second condenser and by vaporizer to absorption reverse circulation heat supply, absorption reverse circulation, by adsorber, the second adsorber and the external heat supply of condenser, forms combined cycle energy supplying system.

The energy supplying system of combined cycle shown in Fig. 9 is achieved in that

(1), in structure, it formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, vaporizer, decompressor, low temperature heat exchanger, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and working machine, gas compressor A has air passageways and ft connection, gas compressor A also has compressed air channel to be communicated with firing chamber B, firing chamber B also has fuel channel and ft connection, firing chamber B also has blast tube to be communicated with gas turbine C, gas turbine C also has blast tube to be communicated with exhaust heat boiler E, exhaust heat boiler E also have blast tube be communicated with generator 3 and the second generator 4 successively after the second generator 4 have blast tube and ft connection again, steam turbine D has low pressure steam passage to be communicated with heat exchanger G, heat exchanger G also has condensed fluid pipeline to be communicated with exhaust heat boiler E through recycle pump F, exhaust heat boiler E also has high pressure steam passage to be communicated with steam turbine D, heat exchanger G also has heated medium pipeline and ft connection, the finisher 6 that compressor H has refrigerant gas passage to be communicated with vaporizer 6 has refrigerant gas passage to be communicated with decompressor O again, decompressor O also has refrigerant gas passage to be communicated with compressor H through low temperature heat exchanger J, and low temperature heat exchanger J also has cryogenic media pipeline and ft connection, vaporizer 6 also has refrigerant steam channel to be communicated with adsorber 1, adsorber 1 also has dilute solution pipeline to be communicated with the second adsorber 2 with solution heat exchanger 10 through solution pump 8, second adsorber 2 also has dilute solution pipeline to be communicated with generator 3 with the second solution heat exchanger 11 through the second solution pump 9, generator 3 also has concentrated solution pipeline to be communicated with the second generator 4 through the second solution heat exchanger 11, second generator 4 also has concentrated solution pipeline to be communicated with adsorber 1 through solution heat exchanger 10, generator 3 also has refrigerant steam channel to be communicated with condenser 5, second generator 4 also has refrigerant steam channel to be communicated with the second adsorber 2, condenser 5 also has cryogen liquid pipeline to be communicated with vaporizer 6 through throttle valve 7, adsorber 1, second adsorber 2 and condenser 5 also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger and working machine form fuel gas-steam forward circulation system, compressor, vaporizer, decompressor and low temperature heat exchanger form compression type reverse circulation system, and adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system.

(2) in flow process, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger carry out fuel gas-steam forward circulation---and air enters gas compressor A, compressed boosting enters firing chamber B after heating up, fuel enters firing chamber and with pressurized air mixed combustion or carry out secondary with air more afterwards and mix, high-temperature fuel gas enters gas turbine C step-down work done, gas flow after work done is through exhaust heat boiler E, generator 3 and the second generator 4 do driving thermal medium is supplied to after heat release cooling, the high pressure steam that exhaust heat boiler E produces enters steam turbine D step-down work done, the low pressure steam that steam turbine E discharges enters heat exchanger G, heat release becomes condensed fluid in heated medium, condensed fluid is supplied to exhaust heat boiler E after recycle pump F pressurizes, absorb heat into high pressure steam and provide to steam turbine D, compressor, vaporizer, decompressor and low temperature heat exchanger carry out compression type reverse circulation---and refrigerant gas enters compressor H, boosting flows through vaporizer 6 after heating up and heat release cooling, and refrigerant gas flows through low temperature heat exchanger J after flowing through decompressor O step-down work done, heat absorption heats up and provides to compressor H, adsorber, second adsorber, generator, second generator, condenser, vaporizer, throttle valve, solution pump, second solution pump, solution heat exchanger and the second solution heat exchanger carry out absorption reverse circulation---and the dilute solution of adsorber 1 enters the second adsorber 2 through solution pump 8 and solution heat exchanger 10, absorb refrigerant vapour heat release in heated medium, the dilute solution of the second adsorber 2 enters generator 3 through the second solution pump 9 and the second solution heat exchanger 11, heat absorption release refrigerant vapour also provides to condenser 5, and the concentrated solution of generator 3 enters the second generator 4 through the second solution heat exchanger 11, heat absorption release refrigerant vapour also provides to the second adsorber 2, and the concentrated solution of the second generator 4 enters adsorber 1 through solution heat exchanger 10, absorb refrigerant vapour heat release in heated medium, the refrigerant vapour heat release of condenser 5 becomes cryogen liquid in heated medium, and the cryogen liquid of condenser 5 enters vaporizer 6 through throttle valve 7 throttling, absorb heat into refrigerant vapour and provide to adsorber 1, fuel gas-steam forward circulation provides power respectively to working machine and compression type reverse circulation, fuel gas-steam forward circulation provides driving heat load to absorption reverse circulation, compression type reverse circulation obtains Low Temperature Thermal load by vaporizer to absorption reverse circulation heat supply, absorption reverse circulation, by adsorber, the second adsorber and the external heat supply of condenser, forms combined cycle energy supplying system.

The energy supplying system of combined cycle shown in Figure 10 is achieved in that

In the energy supplying system of combined cycle shown in Fig. 9, increase by the second compressor, the finisher 6 being had by compressor H refrigerant gas passage to be communicated with vaporizer 6 has refrigerant gas passage to be communicated with decompressor O to be adjusted to compressor H the finisher 6 having refrigerant gas passage to be communicated with vaporizer 6 to have refrigerant gas passage to be communicated with the second compressor K more again, and the finisher 6 that the second compressor K also has refrigerant gas passage to be communicated with vaporizer 6 has refrigerant gas passage to be communicated with decompressor O again; The refrigerant gas that compressor H produces is supplied to the second compressor K after flowing through vaporizer 6 heat release cooling, and the refrigerant gas that the second compressor K produces is supplied to decompressor O after flowing through vaporizer 6 heat release cooling, forms combined cycle energy supplying system.

The energy supplying system of combined cycle shown in Figure 11 is achieved in that

(1), in structure, it formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, vaporizer, decompressor, low temperature heat exchanger, regenerator, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and working machine, gas compressor A has air passageways and ft connection, gas compressor A also has compressed air channel to be communicated with firing chamber B, firing chamber B also has fuel channel and ft connection, firing chamber B also has blast tube to be communicated with gas turbine C, gas turbine C also has blast tube to be communicated with exhaust heat boiler E, exhaust heat boiler E also have blast tube be communicated with generator 3 and the second generator 4 successively after the second generator 4 have blast tube and ft connection again, steam turbine D has low pressure steam passage to be communicated with heat exchanger G, heat exchanger G also has condensed fluid pipeline to be communicated with exhaust heat boiler E through recycle pump F, exhaust heat boiler E also has high pressure steam passage to be communicated with steam turbine D, heat exchanger G also has heated medium pipeline and ft connection, the finisher 6 that compressor H has refrigerant gas passage to be communicated with vaporizer 6 has refrigerant gas passage to be communicated with decompressor O through regenerator P again, decompressor O also has refrigerant gas passage to be communicated with compressor H with regenerator P through low temperature heat exchanger J, and low temperature heat exchanger J also has cryogenic media pipeline and ft connection, vaporizer 6 also has refrigerant steam channel to be communicated with adsorber 1, adsorber 1 also has dilute solution pipeline to be communicated with the second adsorber 2 with solution heat exchanger 10 through solution pump 8, second adsorber 2 also has dilute solution pipeline to be communicated with generator 3 with the second solution heat exchanger 11 through the second solution pump 9, generator 3 also has concentrated solution pipeline to be communicated with the second generator 4 through the second solution heat exchanger 11, second generator 4 also has concentrated solution pipeline to be communicated with adsorber 1 through solution heat exchanger 10, generator 3 also has refrigerant steam channel to be communicated with condenser 5, second generator 4 also has refrigerant steam channel to be communicated with the second adsorber 2, condenser 5 also has cryogen liquid pipeline to be communicated with vaporizer 6 through throttle valve 7, adsorber 1, second adsorber 2 and condenser 5 also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger and working machine form fuel gas-steam forward circulation system, compressor, vaporizer, decompressor, low temperature heat exchanger and regenerator form compression type reverse circulation system, adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump,

Second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system.

(2) in flow process, compared with the energy supplying system of combined cycle shown in Fig. 9, difference is: the refrigerant gas that compressor H produces is supplied to regenerator P after flowing through vaporizer 6 heat release cooling, and refrigerant gas is supplied to decompressor O after flowing through regenerator P heat release cooling; The refrigerant gas that decompressor O discharges flows through low temperature heat exchanger J and regenerator P, progressively heat absorption successively and is supplied to compressor H after heating up.

The energy supplying system of combined cycle shown in Figure 12 is achieved in that

In the energy supplying system of combined cycle shown in Figure 11, increase by the second compressor, the finisher 6 being had by compressor H refrigerant gas passage to be communicated with vaporizer 6 has refrigerant gas passage to be communicated with through regenerator P the finisher 6 being adjusted to compressor H and having refrigerant gas passage to be communicated with logical vaporizer 6 with decompressor O again has refrigerant gas passage to be communicated with the second compressor K again, and the finisher 6 that the second compressor K also has refrigerant gas passage to be communicated with vaporizer 6 has refrigerant gas passage to be communicated with decompressor O through regenerator P again; The refrigerant gas that compressor H produces is supplied to the second compressor K after flowing through vaporizer 6, heat release cooling, the refrigerant gas that second compressor K produces is supplied to decompressor O after flowing through vaporizer 6 and regenerator P heat release cooling successively, forms combined cycle energy supplying system.

The energy supplying system of combined cycle shown in Figure 13 is achieved in that

(1), in structure, it formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, decompressor, cooler, low temperature heat exchanger, vaporizer, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, gas compressor A has air passageways and ft connection, gas compressor A also has compressed air channel to be communicated with firing chamber B, firing chamber B also has fuel channel and ft connection, firing chamber B also has blast tube to be communicated with gas turbine C, gas turbine C also has blast tube to be communicated with exhaust heat boiler E, exhaust heat boiler E also have blast tube be communicated with generator 3 and the second generator 4 successively after the second generator 4 have blast tube and ft connection again, steam turbine D has low pressure steam passage to be communicated with heat exchanger G, heat exchanger G also has condensed fluid pipeline to be communicated with exhaust heat boiler E through recycle pump F, exhaust heat boiler E also has high pressure steam passage to be communicated with steam turbine D, heat exchanger G also has heated medium pipeline and ft connection, compressor H has refrigerant gas passage to be communicated with decompressor O through cooler M, decompressor O also has refrigerant gas passage to be communicated with compressor H through low temperature heat exchanger J, low temperature heat exchanger J also has cryogenic media pipeline and ft connection, and cooler M also has heated medium pipeline and ft connection, vaporizer 6 has refrigerant steam channel to be communicated with adsorber 1, adsorber 1 also has dilute solution pipeline to be communicated with the second adsorber 2 with solution heat exchanger 10 through solution pump 8, second adsorber 2 also has dilute solution pipeline to be communicated with generator 3 with the second solution heat exchanger 11 through the second solution pump 9, generator 3 also has concentrated solution pipeline to be communicated with the second generator 4 through the second solution heat exchanger 11, second generator 4 also has concentrated solution pipeline to be communicated with adsorber 1 through solution heat exchanger 10, generator 3 also has refrigerant steam channel to be communicated with condenser 5, second generator 4 also has refrigerant steam channel to be communicated with the second adsorber 2, condenser 5 also has cryogen liquid pipeline to be communicated with vaporizer 6 through throttle valve 7, vaporizer 6 also has cryogenic media pipeline and ft connection, adsorber 1, second adsorber 2 and condenser 5 also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger form fuel gas-steam forward circulation system, compressor, cooler, decompressor and low temperature heat exchanger form compression type reverse circulation system, and adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system.

(2) in flow process, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger carry out fuel gas-steam forward circulation---and air enters gas compressor A, compressed boosting enters firing chamber B after heating up, fuel enters firing chamber and with pressurized air mixed combustion or carry out secondary with air more afterwards and mix, high-temperature fuel gas enters gas turbine C step-down work done, gas flow after work done is through exhaust heat boiler E, generator 3 and the second generator 4 do driving thermal medium is supplied to after heat release cooling, the high pressure steam that exhaust heat boiler E produces enters steam turbine D step-down work done, the low pressure steam that steam turbine E discharges enters heat exchanger G, heat release becomes condensed fluid in heated medium, condensed fluid is supplied to exhaust heat boiler E after recycle pump F pressurizes, absorb heat into high pressure steam and provide to steam turbine D, compressor, cooler, decompressor and low temperature heat exchanger carry out compression type reverse circulation---and refrigerant gas enters compressor H, boosting flows through cooler M after heating up and heat release cooling, and refrigerant gas flows through low temperature heat exchanger J after flowing through decompressor O step-down work done, heat absorption heats up and provides to compressor H, adsorber, second adsorber, generator, second generator, condenser, vaporizer, throttle valve, solution pump, second solution pump, solution heat exchanger and the second solution heat exchanger carry out absorption reverse circulation---and the dilute solution of adsorber 1 enters the second adsorber 2 through solution pump 8 and solution heat exchanger 10, absorb refrigerant vapour heat release in heated medium, the dilute solution of the second adsorber 2 enters generator 3 through the second solution pump 9 and the second solution heat exchanger 11, heat absorption release refrigerant vapour also provides to condenser 5, and the concentrated solution of generator 3 enters the second generator 4 through the second solution heat exchanger 11, heat absorption release refrigerant vapour also provides to the second adsorber 2, and the concentrated solution of the second generator 4 enters adsorber 1 through solution heat exchanger 10, absorb refrigerant vapour heat release in heated medium, the refrigerant vapour heat release of condenser 5 becomes cryogen liquid in heated medium, and the cryogen liquid of condenser 5 enters vaporizer 6 through throttle valve 7 throttling, absorb heat into refrigerant vapour and provide to adsorber 1, fuel gas-steam forward circulation provides power respectively to compression type reverse circulation and provides driving heat load to absorption reverse circulation, compression type reverse circulation obtains Low Temperature Thermal load and passes through the external heat supply of cooler, absorption reverse circulation obtains Low Temperature Thermal load and by adsorber, the second adsorber and the external heat supply of condenser, forms combined cycle energy supplying system.

The energy supplying system of combined cycle shown in Figure 14 is achieved in that

In the energy supplying system of combined cycle shown in Figure 13, increase by the second compressor, had by compressor H refrigerant gas passage to be communicated with decompressor O through cooler M to be adjusted to compressor H and to have refrigerant gas passage to be communicated with the second compressor K through cooler M, the second compressor K also has refrigerant gas passage to be communicated with decompressor O through cooler M; The refrigerant gas that compressor H produces is supplied to the second compressor K after flowing through cooler M heat release cooling, and the refrigerant gas that the second compressor K produces is supplied to decompressor O after flowing through cooler M heat release, forms combined cycle energy supplying system.

The energy supplying system of combined cycle shown in Figure 15 is achieved in that

(1), in structure, it formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, cooler, decompressor, low temperature heat exchanger, regenerator, vaporizer, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, gas compressor A has air passageways and ft connection, gas compressor A also has compressed air channel to be communicated with firing chamber B, firing chamber B also has fuel channel and ft connection, firing chamber B also has blast tube to be communicated with gas turbine C, gas turbine C also has blast tube to be communicated with exhaust heat boiler E, exhaust heat boiler E also have blast tube be communicated with generator 3 and the second generator 4 successively after the second generator 4 have blast tube and ft connection again, steam turbine D has low pressure steam passage to be communicated with heat exchanger G, heat exchanger G also has condensed fluid pipeline to be communicated with exhaust heat boiler E through recycle pump F, exhaust heat boiler E also has high pressure steam passage to be communicated with steam turbine D, heat exchanger G also has heated medium pipeline and ft connection, compressor H has refrigerant gas passage to be communicated with decompressor O with regenerator P through cooler M, decompressor O also has refrigerant gas passage to be communicated with compressor H with regenerator P through low temperature heat exchanger J, low temperature heat exchanger J also has cryogenic media pipeline and ft connection, and cooler M also has heated medium pipeline and ft connection, vaporizer 6 has refrigerant steam channel to be communicated with adsorber 1, adsorber 1 also has dilute solution pipeline to be communicated with the second adsorber 2 with solution heat exchanger 10 through solution pump 8, second adsorber 2 also has dilute solution pipeline to be communicated with generator 3 with the second solution heat exchanger 11 through the second solution pump 9, generator 3 also has concentrated solution pipeline to be communicated with the second generator 4 through the second solution heat exchanger 11, second generator 4 also has concentrated solution pipeline to be communicated with adsorber 1 through solution heat exchanger 10, generator 3 also has refrigerant steam channel to be communicated with condenser 5, second generator 4 also has refrigerant steam channel to be communicated with the second adsorber 2, condenser 5 also has cryogen liquid pipeline to be communicated with vaporizer 6 through throttle valve 7, vaporizer 6 also has cryogenic media pipeline and ft connection, adsorber 1, second adsorber 2 and condenser 5 also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger form fuel gas-steam forward circulation system, compressor, cooler, decompressor, low temperature heat exchanger and regenerator form compression type reverse circulation system, and adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system.

(2) in flow process, compared with the energy supplying system of combined cycle shown in Figure 13, difference is: compressor, cooler, decompressor, low temperature heat exchanger and regenerator carry out compression type reverse circulation---the refrigerant gas that compressor H produces is supplied to decompressor O after flowing through cooler M and regenerator P, heat release cooling successively, refrigerant gas flows through decompressor O step-down work done, and the refrigerant gas that decompressor O discharges flows through low temperature heat exchanger J and regenerator P successively, the backward compressor H of heat absorption intensification provides.

The energy supplying system of combined cycle shown in Figure 16 is achieved in that

In the energy supplying system of combined cycle shown in Figure 15, increase by the second compressor, had by compressor H refrigerant gas passage to be communicated with decompressor O through cooler M and regenerator P to be adjusted to compressor H and to have refrigerant gas passage to be communicated with the second compressor K through cooler M, the second compressor K has refrigerant gas passage to be communicated with decompressor O with regenerator P through cooler M again; The refrigerant gas that compressor H produces is supplied to the second compressor K after flowing through cooler M heat release cooling, the refrigerant gas that second compressor K produces is supplied to decompressor O after flowing through cooler M and regenerator P, heat release cooling successively, forms combined cycle energy supplying system.

The energy supplying system of combined cycle shown in Figure 17 is achieved in that

(1), in structure, it formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, cooler, vaporizer, decompressor, low temperature heat exchanger, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, gas compressor A has air passageways and ft connection, gas compressor A also has compressed air channel to be communicated with firing chamber B, firing chamber B also has fuel channel and ft connection, firing chamber B also has blast tube to be communicated with gas turbine C, gas turbine C also has blast tube to be communicated with exhaust heat boiler E, exhaust heat boiler E also have blast tube be communicated with generator 3 and the second generator 4 successively after the second generator 4 have blast tube and ft connection again, steam turbine D has low pressure steam passage to be communicated with heat exchanger G, heat exchanger G also has condensed fluid pipeline to be communicated with exhaust heat boiler E through recycle pump F, exhaust heat boiler E also has high pressure steam passage to be communicated with steam turbine D, heat exchanger G also has heated medium pipeline and ft connection, compressor H has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor O again through the finisher 6 that cooler M is communicated with vaporizer 6, decompressor O also has refrigerant gas passage to be communicated with compressor H through low temperature heat exchanger J, low temperature heat exchanger J also has cryogenic media pipeline and ft connection, and cooler M also has heated medium pipeline and ft connection, vaporizer 6 also has refrigerant steam channel to be communicated with adsorber 1, adsorber 1 also has dilute solution pipeline to be communicated with the second adsorber 2 with solution heat exchanger 10 through solution pump 8, second adsorber 2 also has dilute solution pipeline to be communicated with generator 3 with the second solution heat exchanger 11 through the second solution pump 9, generator 3 also has concentrated solution pipeline to be communicated with the second generator 4 through the second solution heat exchanger 11, second generator 4 also has concentrated solution pipeline to be communicated with adsorber 1 through solution heat exchanger 10, generator 3 also has refrigerant steam channel to be communicated with condenser 5, second generator 4 also has refrigerant steam channel to be communicated with the second adsorber 2, condenser 5 also has cryogen liquid pipeline to be communicated with vaporizer 6 through throttle valve 7, adsorber 1, second adsorber 2 and condenser 5 also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger form fuel gas-steam forward circulation system, compressor, cooler, vaporizer, decompressor and low temperature heat exchanger form compression type reverse circulation system, and adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system.

(2) in flow process, compared with the energy supplying system of combined cycle shown in Fig. 9, except without except working machine, main difference part is: the refrigerant gas that compressor H produces is supplied to decompressor O after flowing through cooler M and vaporizer 6, heat release cooling successively, compression type reverse circulation obtain Low Temperature Thermal load and respectively by the external heat supply of cooler and by vaporizer to absorption reverse circulation heat supply.

The energy supplying system of combined cycle shown in Figure 18 is achieved in that

In the energy supplying system of combined cycle shown in Figure 17, increase by the second compressor, had by compressor H refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor O to be again adjusted to compressor H through the finisher 6 that cooler M is communicated with vaporizer 6 and have refrigerant gas passage to have refrigerant gas passage to be communicated with the second compressor K again through the finisher 6 that cooler M is communicated with vaporizer 6, the second compressor K also has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor O again through the finisher 6 that cooler M is communicated with vaporizer 6; The refrigerant gas that compressor H produces flows through cooler M successively and vaporizer 6, heat release are supplied to the second compressor K after lowering the temperature, the refrigerant gas that second compressor K produces flows through cooler M successively and vaporizer 6, heat release are supplied to decompressor O after lowering the temperature, and forms combined cycle energy supplying system.

The energy supplying system of combined cycle shown in Figure 19 is achieved in that

(1), in structure, it formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, cooler, vaporizer, regenerator, decompressor, low temperature heat exchanger, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, gas compressor A has air passageways and ft connection, gas compressor A also has compressed air channel to be communicated with firing chamber B, firing chamber B also has fuel channel and ft connection, firing chamber B also has blast tube to be communicated with gas turbine C, gas turbine C also has blast tube to be communicated with exhaust heat boiler E, exhaust heat boiler E also have blast tube be communicated with generator 3 and the second generator 4 successively after the second generator 4 have blast tube and ft connection again, steam turbine D has low pressure steam passage to be communicated with heat exchanger G, heat exchanger G also has condensed fluid pipeline to be communicated with exhaust heat boiler E through recycle pump F, exhaust heat boiler E also has high pressure steam passage to be communicated with steam turbine D, heat exchanger G also has heated medium pipeline and ft connection, compressor H has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor O through regenerator P again through the finisher 6 that cooler M is communicated with vaporizer 6, decompressor O also has refrigerant gas passage to be communicated with compressor H with regenerator P through low temperature heat exchanger J, low temperature heat exchanger J also has cryogenic media pipeline and ft connection, and cooler M also has heated medium pipeline and ft connection, vaporizer 6 also has refrigerant steam channel to be communicated with adsorber 1, adsorber 1 also has dilute solution pipeline to be communicated with the second adsorber 2 with solution heat exchanger 10 through solution pump 8, second adsorber 2 also has dilute solution pipeline to be communicated with generator 3 with the second solution heat exchanger 11 through the second solution pump 9, generator 3 also has concentrated solution pipeline to be communicated with the second generator 4 through the second solution heat exchanger 11, second generator 4 also has concentrated solution pipeline to be communicated with adsorber 1 through solution heat exchanger 10, generator 3 also has refrigerant steam channel to be communicated with condenser 5, second generator 4 also has refrigerant steam channel to be communicated with the second adsorber 2, condenser 5 also has cryogen liquid pipeline to be communicated with vaporizer 6 through throttle valve 7, adsorber 1, second adsorber 2 and condenser 5 also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger form fuel gas-steam forward circulation system, compressor, cooler, vaporizer, regenerator, decompressor and low temperature heat exchanger form compression type reverse circulation system, and adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system.

(2) in flow process, compared with the energy supplying system of combined cycle shown in Figure 17, difference is: the refrigerant gas that compressor H produces is supplied to decompressor O after flowing through cooler M, vaporizer 6 and regenerator P heat release cooling successively, and the refrigerant gas that decompressor O discharges flows through successively after low temperature heat exchanger J and regenerator P heat absorption heats up and is supplied to compressor H.

The energy supplying system of combined cycle shown in Figure 20 is achieved in that

In the energy supplying system of combined cycle shown in Figure 19, increase by the second compressor, had by compressor H refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor O through regenerator P again through the finisher 6 that cooler M is communicated with vaporizer 6 to be adjusted to compressor H and to have refrigerant gas passage to have refrigerant gas passage to be communicated with the second compressor K again through the finisher 6 that cooler M is communicated with vaporizer 6, the second compressor K also has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor O through regenerator P again through the finisher 6 that cooler M is communicated with vaporizer 6; The refrigerant gas that compressor H produces flows through cooler M successively and vaporizer 6, heat release are supplied to the second compressor K after lowering the temperature, the refrigerant gas that second compressor K produces is supplied to decompressor O after flowing through cooler M, vaporizer 6 and regenerator P heat release cooling successively, forms combined cycle energy supplying system.

The energy supplying system of combined cycle shown in Figure 21 is achieved in that

In the energy supplying system of combined cycle shown in Fig. 1, increase high temperature regenerator, being had by gas compressor A compressed air channel to be communicated with firing chamber B to be adjusted to gas compressor A has compressed air channel to be communicated with firing chamber B through high temperature regenerator Q, and being had by gas turbine C blast tube to be communicated with exhaust heat boiler E to be adjusted to gas turbine C has blast tube to be communicated with exhaust heat boiler E through high temperature regenerator Q; The pressurized air that gas compressor A produces enters firing chamber B after high temperature regenerator Q absorbs heat intensification, and the gas flow that gas turbine C discharges provides through the backward exhaust heat boiler E of high temperature regenerator Q heat release cooling, forms combined cycle energy supplying system.

The energy supplying system of combined cycle shown in Figure 22 is achieved in that

(1) in structure, in the energy supplying system of combined cycle shown in Fig. 1, increase by the second heat exchanger, had by second generator 4 blast tube and ft connection to be adjusted to the second generator 4 and have blast tube through the second heat exchanger 8 and ft connection, the second heat exchanger 8 also has heated medium pipeline and ft connection, increase by the 3rd generator, second throttle, 3rd solution pump and the 3rd solution heat exchanger, second adsorber 2 is set up dilute solution pipeline and is communicated with the 3rd generator 13 with the 3rd solution heat exchanger 16 through the 3rd solution pump 15, 3rd generator 13 also has concentrated solution pipeline to be communicated with the second generator 4 through the 3rd solution heat exchanger 16, had by generator 3 refrigerant steam channel to be communicated with condenser 5 to be adjusted to generator 3 have refrigerant steam channel be communicated with the 3rd generator 13 after the 3rd generator 13 have cryogen liquid pipeline to be communicated with condenser 5 through second throttle 14 again, 3rd generator 13 also has refrigerant steam channel to be communicated with condenser 5.

(2) in flow process, the combustion gas that exhaust heat boiler E discharges flows through generator 3, second generator 4 and the second heat exchanger 8 successively, externally discharges after heat release cooling, the refrigerant vapour that generator 3 produces is supplied to the 3rd generator 13 and does to drive thermal medium, the part dilute solution of the second adsorber 2 enters the 3rd generator 13 through the 3rd solution pump 15 and the 3rd solution heat exchanger 16, refrigerant vapour flows through the 3rd generator 13, heating enters the solution release refrigerant vapour in it and provides to condenser 5, the concentrated solution of the 3rd generator 13 enters the second generator 4 through the 3rd solution heat exchanger 16, condenser 5 is entered through second throttle 14 throttling after the refrigerant vapour heat release flowing through the 3rd generator 13 becomes cryogen liquid, form combined cycle energy supplying system.

The energy supplying system of combined cycle shown in Figure 23 is achieved in that

(1) in structure, in the energy supplying system of combined cycle shown in Fig. 1, increase by the second heat exchanger, had by second generator 4 blast tube and ft connection to be adjusted to the second generator 4 and have blast tube through the second heat exchanger 8 and vaporizer 6 and ft connection, the second heat exchanger 8 also has heated medium pipeline and ft connection, increase by the 3rd generator, second throttle and the 3rd solution heat exchanger, had by second adsorber 2 dilute solution pipeline to be communicated with generator 3 through the second solution pump 9 and the second solution heat exchanger 11 to be adjusted to the second adsorber 2 and to have dilute solution pipeline through the second solution pump 9, second solution heat exchanger 11 is communicated with generator 3 with the 3rd solution heat exchanger 16, had by generator 3 concentrated solution pipeline to be communicated with the second generator 4 through the second solution heat exchanger 11 to be adjusted to generator 3 and to have concentrated solution pipeline to be communicated with the 3rd generator 13 through the 3rd solution heat exchanger 16, 3rd generator 13 has concentrated solution pipeline to be communicated with the second generator 4 through the second solution heat exchanger 11 again, had by generator 3 refrigerant steam channel to be communicated with condenser 5 to be adjusted to generator 3 have refrigerant steam channel be communicated with the 3rd generator 13 after the 3rd generator 13 have cryogen liquid pipeline to be communicated with condenser 5 through second throttle 14 again, 3rd generator 13 also has refrigerant steam channel to be communicated with condenser 5.

(2) in flow process, the combustion gas that exhaust heat boiler E discharges flows through generator 3, second generator 4, second heat exchanger 8 and vaporizer 6 successively, progressively externally discharges after heat release cooling, generator 3 produces refrigerant vapour and is supplied to the 3rd generator 13 do driving thermal medium, the dilute solution of the second adsorber 2 is through the second solution pump 9, second solution heat exchanger 11 and the 3rd solution heat exchanger 16 enter generator 3, the concentrated solution of generator 3 enters the 3rd generator 13 through the 3rd solution heat exchanger 16, refrigerant vapour flows through the 3rd generator 13, heating enters the solution release refrigerant vapour in it and provides to condenser 5, the concentrated solution of the 3rd generator 13 enters the second generator 4 through the second solution heat exchanger 11, condenser 5 is entered through second throttle 14 throttling after the refrigerant vapour heat release flowing through the 3rd generator 13 becomes cryogen liquid, form combined cycle energy supplying system.

The energy supplying system of combined cycle shown in Figure 24 is achieved in that

(1) in structure, in the energy supplying system of combined cycle shown in Fig. 1, increase by the second heat exchanger, had by second generator 4 blast tube and ft connection to be adjusted to the second generator 4 and have blast tube through the second heat exchanger 8, vaporizer 6 and low temperature heat exchanger J and ft connection, the second heat exchanger 8 also has heated medium pipeline and ft connection; increase by the 3rd generator, second throttle, 3rd solution pump and the 3rd solution heat exchanger, had by second adsorber 2 dilute solution pipeline to be communicated with generator 3 through the second solution pump 9 and the second solution heat exchanger 11 to be adjusted to the second adsorber 2 and to have dilute solution pipeline to be communicated with the 3rd generator 13 with the second solution heat exchanger 11 through the second solution pump 9,3rd generator 13 has concentrated solution pipeline to be communicated with generator 3 with the 3rd solution heat exchanger 16 through the 3rd solution pump 15 again, had by generator 3 concentrated solution pipeline to be communicated with the second generator 4 through the second solution heat exchanger 11 to be adjusted to generator 3 and to have concentrated solution pipeline to be communicated with the second generator 4 with the second solution heat exchanger 11 through the 3rd solution heat exchanger 16, had by generator 3 refrigerant steam channel to be communicated with condenser 5 to be adjusted to generator 3 have refrigerant steam channel be communicated with the 3rd generator 13 after the 3rd generator 13 have cryogen liquid pipeline to be communicated with condenser 5 through second throttle 14 again, 3rd generator 13 also has refrigerant steam channel to be communicated with condenser 5.

(2) in flow process, the combustion gas that exhaust heat boiler E discharges flows through generator 3, second generator 4, second heat exchanger 8, vaporizer 6 and low temperature heat exchanger J successively, progressively externally discharges after heat release cooling, generator 3 produces refrigerant vapour and is supplied to the 3rd generator 13 do driving thermal medium, the dilute solution of the second adsorber 2 enters the 3rd generator 13 through solution pump 9 and the second solution heat exchanger 11, refrigerant vapour flows through the 3rd generator 13, heating enters the solution release refrigerant vapour in it and provides to condenser 5, the concentrated solution of the 3rd generator 13 enters generator 3 through the 3rd solution pump 15 and the 3rd solution heat exchanger 16, the concentrated solution of generator 3 enters the second generator 4 through the 3rd solution heat exchanger 16 and the second solution heat exchanger 11, condenser 5 is entered through second throttle 14 throttling after the refrigerant vapour heat release flowing through the 3rd generator 13 becomes cryogen liquid, form combined cycle energy supplying system.

The energy supplying system of combined cycle shown in Figure 25 is achieved in that

In the energy supplying system of combined cycle shown in Figure 23, there is by generator 3 blast tube to be adjusted to generator 3 through the second generator 4, second heat exchanger 8 and vaporizer 6 and ft connection and have blast tube through the 3rd generator 13, second generator 4, second heat exchanger 8 and vaporizer 6 and ft connection; The combustion gas that exhaust heat boiler E discharges flows through generator 3, the 3rd generator 13, second generator 4, second heat exchanger 8 and vaporizer 6 heat release cooling successively, forms combined cycle energy supplying system.

The energy supplying system of combined cycle shown in Figure 26 is achieved in that

(1) in structure, in the energy supplying system of combined cycle shown in Figure 22, increase by the 4th generator, 3rd throttle valve, 4th solution pump and the 4th solution heat exchanger, second adsorber 2 is set up dilute solution pipeline and is communicated with the 4th generator 17 with the 4th solution heat exchanger 20 through the 4th solution pump 19, 4th generator 17 also has concentrated solution pipeline to be communicated with the second generator 4 through the 4th solution heat exchanger 20, had by 3rd generator 13 refrigerant steam channel to be communicated with condenser 5 to be adjusted to the 3rd generator 13 have refrigerant steam channel be communicated with the 4th generator 17 after the 4th generator 17 have cryogen liquid pipeline to be communicated with condenser 5 through the 3rd throttle valve 18 again, 4th generator 17 also has refrigerant steam channel to be communicated with condenser 5.

(2) in flow process, the refrigerant vapour that 3rd generator 13 produces is supplied to the 4th generator 17 and does to drive thermal medium, the part dilute solution of the second adsorber 2 enters the 4th generator 17 through the 4th solution pump 19 and the 4th solution heat exchanger 20, refrigerant vapour flows through the 4th generator 17, heating enters the solution release refrigerant vapour in it and provides to condenser 5, the concentrated solution of the 4th generator 17 enters the second generator 4 through the 4th solution heat exchanger 20, condenser 5 is entered through the 3rd throttle valve 18 throttling after the refrigerant vapour heat release flowing through the 4th generator 17 becomes cryogen liquid, form combined cycle energy supplying system.

The energy supplying system of combined cycle shown in Figure 27 is achieved in that

(1) in structure, in the energy supplying system of combined cycle shown in Figure 23, there is by the 3rd generator 13 cryogen liquid pipeline to be communicated with condenser 5 through second throttle 14 and be adjusted to the 3rd generator 13 and have cryogen liquid pipeline to be communicated with condenser 5 with second throttle 14 through the 4th generator 17; increase by the 4th generator, 3rd throttle valve and the 4th solution heat exchanger, second adsorber 2 there is dilute solution pipeline through the second solution pump 9, second solution heat exchanger 11 and the 3rd solution heat exchanger 16 are communicated with generator 3 and are adjusted to the second adsorber 2 and have dilute solution pipeline through the second solution pump 9, second solution heat exchanger 11,4th solution heat exchanger 20 is communicated with generator 3 with the 3rd solution heat exchanger 16, had by 3rd generator 13 concentrated solution pipeline to be communicated with the second generator 4 through the second solution heat exchanger 11 to be adjusted to the 3rd generator 13 and to have concentrated solution pipeline to be communicated with the 4th generator 17 through the 4th solution heat exchanger 20,4th generator 17 has concentrated solution pipeline to be communicated with the second generator 4 through the second solution heat exchanger 11 again, had by 3rd generator 13 refrigerant steam channel to be communicated with condenser 5 to be adjusted to the 3rd generator 13 have refrigerant steam channel be communicated with the 4th generator 17 after the 4th generator 17 have cryogen liquid pipeline to be communicated with condenser 5 through the 3rd throttle valve 18 again, 4th generator 17 also has refrigerant steam channel to be communicated with condenser 5.

(2) in flow process, the cryogen liquid that 3rd generator 13 produces and refrigerant vapour are supplied to the 4th generator 17 and do to drive thermal medium, the dilute solution of the second adsorber 2 is through the second solution pump 9, second solution heat exchanger 11, 4th solution heat exchanger 20 and the 3rd solution heat exchanger 16 enter generator 3, the concentrated solution of generator 3 enters the 3rd generator 13 through the 3rd solution heat exchanger 16, the concentrated solution of the 3rd generator 13 enters the 4th generator 17 through the 4th solution heat exchanger 20, refrigerant vapour and cryogen liquid flow through the 4th generator 17, heating enters the solution release refrigerant vapour in it and provides to condenser 5, the concentrated solution of the 4th generator 17 enters the second generator 4 through the second solution heat exchanger 11, condenser 5 is entered through the 3rd throttle valve 18 throttling after the refrigerant vapour heat release flowing through the 4th generator 17 becomes cryogen liquid, flow through the cryogen liquid heat release cooling of the 4th generator 17 after enter condenser 5 through second throttle 14 throttling, form combined cycle energy supplying system.

The energy supplying system of combined cycle shown in Figure 28 is achieved in that

(1) in structure, in the energy supplying system of combined cycle shown in Figure 24, increase by the 4th generator, 3rd throttle valve, 4th solution pump and the 4th solution heat exchanger, had by second adsorber 2 dilute solution pipeline to be communicated with the 3rd generator 13 through the second solution pump 9 and the second solution heat exchanger 11 to be adjusted to the second adsorber 2 and to have dilute solution pipeline to be communicated with the 4th generator 17 with the second solution heat exchanger 11 through the second solution pump 9,4th generator 17 has concentrated solution pipeline to be communicated with the 3rd generator 13 with the 4th solution heat exchanger 20 through the 4th solution pump 19 again, had by generator 3 concentrated solution pipeline to be communicated with the second generator 4 through the 3rd solution heat exchanger 16 and the second solution heat exchanger 11 to be adjusted to generator 3 and to have concentrated solution pipeline through the 3rd solution heat exchanger 16,4th solution heat exchanger 20 is communicated with the second generator 4 with the second solution heat exchanger 11, had by 3rd generator 13 refrigerant steam channel to be communicated with condenser 5 to be adjusted to the 3rd generator 13 have refrigerant steam channel be communicated with the 4th generator 17 after the 4th generator 17 have cryogen liquid pipeline to be communicated with condenser 5 through the 3rd throttle valve 18 again, 4th generator 17 also has refrigerant steam channel to be communicated with condenser 5.

(2) in flow process, the refrigerant vapour that 3rd generator 13 produces is supplied to the 4th generator 17 and does to drive thermal medium, the dilute solution of the second adsorber 2 enters the 4th generator 17 through the second solution pump 9 and the second solution heat exchanger 11, refrigerant vapour flows through the 4th generator 17, heating enters the solution release refrigerant vapour in it and provides to condenser 5, the concentrated solution of the 4th generator 17 enters the 3rd generator 13 through the 4th solution pump 19 and the 4th solution heat exchanger 20, the concentrated solution of the 3rd generator 13 enters generator 3 through the 3rd solution pump 15 and the 3rd solution heat exchanger 16, the concentrated solution of generator 3 is through the 3rd solution heat exchanger 16, 4th solution heat exchanger 20 and the second solution heat exchanger 11 enter the second generator 4, condenser 5 is entered through the 3rd throttle valve 18 throttling after the refrigerant vapour heat release flowing through the 4th generator 17 becomes cryogen liquid, form combined cycle energy supplying system.

The energy supplying system of combined cycle shown in Figure 29 is achieved in that

(1) in structure, in the energy supplying system of combined cycle shown in Fig. 1, increase by the 3rd generator, 3rd solution pump, 3rd solution heat exchanger and the 3rd adsorber, second generator 4 is had blast tube and ft connection be adjusted to the second generator 4 have blast tube be communicated with the 3rd generator 13 after the 3rd generator 13 have blast tube and ft connection again, being had by vaporizer 6 refrigerant steam channel to be communicated with adsorber 1 to be adjusted to vaporizer 6 has refrigerant steam channel to be communicated with the 3rd adsorber 21, 3rd adsorber 21 also has dilute solution pipeline to be communicated with the 3rd generator 13 with the 3rd solution heat exchanger 16 through the 3rd solution pump 15, 3rd generator 13 also has concentrated solution pipeline to be communicated with the 3rd adsorber 21 through the 3rd solution heat exchanger 16, 3rd generator 13 also has refrigerant steam channel to be communicated with adsorber 1, 3rd adsorber 21 also has heated medium pipeline and ft connection.

(2) in flow process, the combustion gas that exhaust heat boiler E discharges flows through generator 3, second generator 4 and the also progressively heat release of the 3rd generator 13 successively, the refrigerant vapour that vaporizer 6 produces enters the 3rd adsorber 21, the dilute solution of the 3rd adsorber 21 enters the 3rd generator 13 through the 3rd solution pump 15 and the 3rd solution heat exchanger 16, absorbing heat discharges refrigerant vapour and provide to adsorber 1, the concentrated solution of the 3rd generator 13 enters the 3rd adsorber 21 through the 3rd solution heat exchanger 16, absorb refrigerant vapour and heat release in heated medium, form combined cycle energy supplying system.

The energy supplying system of combined cycle shown in Figure 30 is achieved in that

(1) in structure, in the energy supplying system of combined cycle shown in Fig. 1, increase temperature heat exchanger and the second recycle pump, exhaust heat boiler E is had blast tube be communicated with generator 3 and the second generator 4 successively after the second generator 4 have again blast tube and ft connection be adjusted to exhaust heat boiler E have blast tube be communicated with high-temperature heat exchanger R after high-temperature heat exchanger R have blast tube and ft connection again, high-temperature heat exchanger R, between generator 3 and the second generator 4, rely on the second recycle pump S and circulating thermal medium pipeline formation closed loop.

(2) in flow process, exhaust heat boiler E discharge gas flow through high temperature heater (HTH) R and heat release in circulating thermal medium, circulating thermal medium flows through high-temperature heat exchanger R after the second recycle pump S pressurizes, heat absorption heats up or be supplied to generator 3 after heat absorption vaporization and the second generator 4 is done to drive thermal medium, circulating thermal medium flows through generator 3 and the also progressively heat release of the second generator 4, there is provided through the backward high temperature heater (HTH) R of the second recycle pump S pressurization again, form combined cycle energy supplying system.

The energy supplying system of combined cycle shown in Figure 31 is achieved in that

(1) in structure, in the energy supplying system of combined cycle shown in Fig. 1, increase high-temperature heat exchanger, second recycle pump, 3rd generator, 3rd solution pump, 3rd solution heat exchanger and the 3rd adsorber, exhaust heat boiler E is had blast tube be communicated with generator 3 and the second generator 4 successively after the second generator 4 have again blast tube and ft connection be adjusted to exhaust heat boiler E have blast tube be communicated with high-temperature heat exchanger R after high-temperature heat exchanger R have blast tube and ft connection again, high-temperature heat exchanger R, generator 3, the second recycle pump S and circulating thermal medium pipeline is relied on to form closed loop between second generator 4 and the 3rd generator 13, being had by vaporizer 6 refrigerant steam channel to be communicated with adsorber 1 to be adjusted to vaporizer 6 has refrigerant steam channel to be communicated with the 3rd adsorber 21,3rd adsorber 21 also has dilute solution pipeline to be communicated with the 3rd generator 13 with the 3rd solution heat exchanger 16 through the 3rd solution pump 15,3rd generator 13 also has concentrated solution pipeline to be communicated with the 3rd adsorber 21 through the 3rd solution heat exchanger 16,3rd generator 13 also has refrigerant steam channel to be communicated with adsorber 1, and the 3rd adsorber 21 also has heated medium pipeline and ft connection.

(2) in flow process, exhaust heat boiler E discharge gas flow through high-temperature heat exchanger R and heat release in circulating thermal medium, circulating thermal medium flows through high-temperature heat exchanger R after the second recycle pump S pressurizes, heat absorption heats up or be supplied to generator 3, second generator 4 after heat absorption vaporization and the 3rd generator 13 is done to drive thermal medium, circulating thermal medium flows through generator 3, second generator 4 and the also progressively heat release of the 3rd generator 13, there is provided through the backward high-temperature heat exchanger R of the second recycle pump S pressurization again, form combined cycle energy supplying system.

The effect that the technology of the present invention can realize---combined cycle energy supplying system proposed by the invention, has following effect and advantage:

(1) realize heat energy efficiency utilization, realize efficient heat supply and highly effective refrigeration.

(2) can realize preferably, to the utilization of such as low ambient temperature thermal resource, realizing energy saving heating.

(3) high temperature heat of combustion gas is used by fuel gas-steam circulation means and compression type reverse circulation device, and promote Low Temperature Thermal load temperature or externally provide power simultaneously, the high temperature section temperature difference obtains Appropriate application, reduces irreversible loss.

(4) waste heat gas load is used by absorption reverse circulation device, obtains or promotes Low Temperature Thermal load further, realizing the Appropriate application of the temperature difference, reducing irreversible loss.

(5) second generators and the second adsorber combine, and realize the efficient of gas thermal energy and deep exploitation.

(6) provide multiple concrete technological scheme, numerous different actual state can be tackled, have wider Applicable scope.

(7) play Gas-steam Combined Cycle, compression type reverse circulation and absorb reverse circulation advantage separately, farthest can realize the efficiency utilization of heat energy.

Claims

1. combined cycle energy supplying system, formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, vaporizer, cryogenic throttle valve, low temperature heat exchanger, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, gas compressor (A) has air passageways and ft connection, gas compressor (A) also has compressed air channel to be communicated with firing chamber (B), firing chamber (B) also has fuel channel and ft connection, firing chamber (B) also has blast tube to be communicated with gas turbine (C), gas turbine (C) also has blast tube to be communicated with exhaust heat boiler (E), exhaust heat boiler (E) also have blast tube be communicated with successively generator (3) and the second generator (4) afterwards the second generator (4) have blast tube and ft connection again, steam turbine (D) has low pressure steam passage to be communicated with heat exchanger (G), heat exchanger (G) also has condensed fluid pipeline to be communicated with exhaust heat boiler (E) through recycle pump (F), exhaust heat boiler (E) also has high pressure steam passage to be communicated with steam turbine (D), heat exchanger (G) also has heated medium pipeline and ft connection, the finisher (6) that compressor (H) has refrigerant steam channel to be communicated with vaporizer (6) has cryogen liquid pipeline to be communicated with low temperature heat exchanger (J) through cryogenic throttle valve (I) again, low temperature heat exchanger (J) also has refrigerant steam channel to be communicated with compressor (H), and low temperature heat exchanger (J) also has cryogenic media pipeline and ft connection, vaporizer (6) also has refrigerant steam channel to be communicated with adsorber (1), adsorber (1) also has dilute solution pipeline to be communicated with the second adsorber (2) with solution heat exchanger (10) through solution pump (8), second adsorber (2) also has dilute solution pipeline to be communicated with generator (3) with the second solution heat exchanger (11) through the second solution pump (9), generator (3) also has concentrated solution pipeline to be communicated with the second generator (4) through the second solution heat exchanger (11), second generator (4) also has concentrated solution pipeline to be communicated with adsorber (1) through solution heat exchanger (10), generator (3) also has refrigerant steam channel to be communicated with condenser (5), second generator (4) also has refrigerant steam channel to be communicated with the second adsorber (2), condenser (5) also has cryogen liquid pipeline to be communicated with vaporizer (6) through throttle valve (7), adsorber (1), second adsorber (2) and condenser (5) also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger form fuel gas-steam forward circulation system, compressor, vaporizer, cryogenic throttle valve and low temperature heat exchanger form compression type reverse circulation system, and adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system, fuel gas-steam forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, fuel gas-steam forward circulation provides driving heat load to absorption reverse circulation, compression type reverse circulation obtains Low Temperature Thermal load by vaporizer to absorption reverse circulation heat supply, absorption reverse circulation, by adsorber, the second adsorber and the external heat supply of condenser, forms combined cycle energy supplying system.

2. combined cycle energy supplying system, in combined cycle energy supplying system according to claim 1, increase by the second compressor, the finisher (6) being had by compressor (H) refrigerant steam channel to be communicated with vaporizer (6) has cryogen liquid pipeline to be communicated with through cryogenic throttle valve (I) finisher (6) being adjusted to compressor (H) and having refrigerant steam channel to be communicated with vaporizer (6) with low temperature heat exchanger (J) again has refrigerant steam channel to be communicated with the second compressor (K) again, the finisher (6) that second compressor (K) also has refrigerant steam channel to be communicated with vaporizer (6) has cryogen liquid pipeline to be communicated with low temperature heat exchanger (J) through cryogenic throttle valve (I) again, form combined cycle energy supplying system.

3. combined cycle energy supplying system, formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, the second condenser, cryogenic throttle valve, low temperature heat exchanger, vaporizer, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, gas compressor (A) has air passageways and ft connection, gas compressor (A) also has compressed air channel to be communicated with firing chamber (B), firing chamber (B) also has fuel channel and ft connection, firing chamber (B) also has blast tube to be communicated with gas turbine (C), gas turbine (C) also has blast tube to be communicated with exhaust heat boiler (E), exhaust heat boiler (E) also have blast tube be communicated with successively generator (3) and the second generator (4) afterwards the second generator (4) have blast tube and ft connection again, steam turbine (D) has low pressure steam passage to be communicated with heat exchanger (G), heat exchanger (G) also has condensed fluid pipeline to be communicated with exhaust heat boiler (E) through recycle pump (F), exhaust heat boiler (E) also has high pressure steam passage to be communicated with steam turbine (D), heat exchanger (G) also has heated medium pipeline and ft connection, compressor (H) have refrigerant steam channel be communicated with the second condenser (L) after the second condenser (L) have cryogen liquid pipeline to be communicated with low temperature heat exchanger (J) through cryogenic throttle valve (I) again, low temperature heat exchanger (J) also has refrigerant steam channel to be communicated with compressor (H), low temperature heat exchanger (J) also has cryogenic media pipeline and ft connection, and the second condenser (L) also has heated medium pipeline and ft connection, vaporizer (6) also has refrigerant steam channel to be communicated with adsorber (1), adsorber (1) also has dilute solution pipeline to be communicated with the second adsorber (2) with solution heat exchanger (10) through solution pump (8), second adsorber (2) also has dilute solution pipeline to be communicated with generator (3) with the second solution heat exchanger (11) through the second solution pump (9), generator (3) also has concentrated solution pipeline to be communicated with the second generator (4) through the second solution heat exchanger (11), second generator (4) also has concentrated solution pipeline to be communicated with adsorber (1) through solution heat exchanger (10), generator (3) also has refrigerant steam channel to be communicated with condenser (5), second generator (4) also has refrigerant steam channel to be communicated with the second adsorber (2), condenser (5) also has cryogen liquid pipeline to be communicated with vaporizer (6) through throttle valve (7), vaporizer (6) also has cryogenic media pipeline and ft connection, adsorber (1), second adsorber (2) and condenser (5) also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger form fuel gas-steam forward circulation system, compressor, the second condenser, cryogenic throttle valve and low temperature heat exchanger form compression type reverse circulation system, and adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system, fuel gas-steam forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, fuel gas-steam forward circulation provides driving heat load to absorption reverse circulation, compression type reverse circulation obtains Low Temperature Thermal load and passes through the external heat supply of the second condenser, absorption reverse circulation obtains Low Temperature Thermal load and by adsorber, the second adsorber and the external heat supply of condenser, forms combined cycle energy supplying system.

4. combined cycle energy supplying system, in combined cycle energy supplying system according to claim 3, increase by the second compressor, compressor (H) is had refrigerant steam channel be communicated with the second condenser (L) after the second condenser (L) have again cryogen liquid pipeline through cryogenic throttle valve (I) to be communicated with low temperature heat exchanger (J) be adjusted to compressor (H) have refrigerant steam channel to be communicated with the second condenser (L) after the second condenser (L) have refrigerant steam channel to be communicated with the second compressor (K) again, second compressor (K) also have refrigerant steam channel be communicated with the second condenser (L) after the second condenser (L) have cryogen liquid pipeline to be communicated with low temperature heat exchanger (J) through cryogenic throttle valve (I) again, form combined cycle energy supplying system.

5. combined cycle energy supplying system, formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, cooler, vaporizer, cryogenic throttle valve, low temperature heat exchanger, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, gas compressor (A) has air passageways and ft connection, gas compressor (A) also has compressed air channel to be communicated with firing chamber (B), firing chamber (B) also has fuel channel and ft connection, firing chamber (B) also has blast tube to be communicated with gas turbine (C), gas turbine (C) also has blast tube to be communicated with exhaust heat boiler (E), exhaust heat boiler (E) also have blast tube be communicated with successively generator (3) and the second generator (4) afterwards the second generator (4) have blast tube and ft connection again, steam turbine (D) has low pressure steam passage to be communicated with heat exchanger (G), heat exchanger (G) also has condensed fluid pipeline to be communicated with exhaust heat boiler (E) through recycle pump (F), exhaust heat boiler (E) also has high pressure steam passage to be communicated with steam turbine (D), heat exchanger (G) also has heated medium pipeline and ft connection, the aftercooler (M) that compressor (H) has refrigerant steam channel to be communicated with cooler (M) has refrigerant steam channel to be communicated with vaporizer (6) again, vaporizer (6) also has cryogen liquid pipeline to be communicated with low temperature heat exchanger (J) through cryogenic throttle valve (I), low temperature heat exchanger (J) also has refrigerant steam channel to be communicated with compressor (H), low temperature heat exchanger (J) also has cryogenic media pipeline and ft connection, and cooler (M) also has heated medium pipeline and ft connection, vaporizer (6) also has refrigerant steam channel to be communicated with adsorber (1), adsorber (1) also has dilute solution pipeline to be communicated with the second adsorber (2) with solution heat exchanger (10) through solution pump (8), second adsorber (2) also has dilute solution pipeline to be communicated with generator (3) with the second solution heat exchanger (11) through the second solution pump (9), generator (3) also has concentrated solution pipeline to be communicated with the second generator (4) through the second solution heat exchanger (11), second generator (4) also has concentrated solution pipeline to be communicated with adsorber (1) through solution heat exchanger (10), generator (3) also has refrigerant steam channel to be communicated with condenser (5), second generator (4) also has refrigerant steam channel to be communicated with the second adsorber (2), condenser (5) also has cryogen liquid pipeline to be communicated with vaporizer (6) through throttle valve (7), adsorber (1), second adsorber (2) and condenser (5) also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger form fuel gas-steam forward circulation system, compressor, cooler, vaporizer, cryogenic throttle valve and low temperature heat exchanger form compression type reverse circulation system, and adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system, fuel gas-steam forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, fuel gas-steam forward circulation provides driving heat load to absorption reverse circulation, compression type reverse circulation obtain Low Temperature Thermal load and respectively by the external heat supply of cooler and by vaporizer to absorption reverse circulation heat supply, absorption reverse circulation, by adsorber, the second adsorber and the external heat supply of condenser, forms combined cycle energy supplying system.

6. combined cycle energy supplying system, in combined cycle energy supplying system according to claim 5, increase by the second compressor, the aftercooler (M) being had by compressor (H) refrigerant steam channel to be communicated with cooler (M) has refrigerant steam channel to be communicated with vaporizer (6) to be adjusted to compressor (H) aftercooler (M) having refrigerant steam channel to be communicated with cooler (M) to have refrigerant steam channel to be communicated with the second compressor (K) more again, the aftercooler (M) that second compressor (K) also has refrigerant steam channel to be communicated with cooler (M) has refrigerant steam channel to be communicated with vaporizer (6) again, form combined cycle energy supplying system.

7. combined cycle energy supplying system, formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, the second compressor, the second condenser, vaporizer, cryogenic throttle valve, the second cryogenic throttle valve, low temperature heat exchanger, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, gas compressor (A) has air passageways and ft connection, gas compressor (A) also has compressed air channel to be communicated with firing chamber (B), firing chamber (B) also has fuel channel and ft connection, firing chamber (B) also has blast tube to be communicated with gas turbine (C), gas turbine (C) also has blast tube to be communicated with exhaust heat boiler (E), exhaust heat boiler (E) also have blast tube be communicated with successively generator (3) and the second generator (4) afterwards the second generator (4) have blast tube and ft connection again, steam turbine (D) has low pressure steam passage to be communicated with heat exchanger (G), heat exchanger (G) also has condensed fluid pipeline to be communicated with exhaust heat boiler (E) through recycle pump (F), exhaust heat boiler (E) also has high pressure steam passage to be communicated with steam turbine (D), heat exchanger (G) also has heated medium pipeline and ft connection, compressor (H) has low pressure refrigerant steam channel to be communicated with vaporizer (6), vaporizer (6) also has low pressure cryogen liquid pipeline low temperature heat exchanger (J) after cryogenic throttle valve (I) is communicated with low temperature heat exchanger (J) to have refrigerant steam channel to be communicated with compressor (H) again, compressor (H) also has low pressure refrigerant steam channel to be communicated with the second compressor (K), second compressor (K) also has high pressure refrigerant steam channel to be communicated with the second condenser (L), second condenser (L) also has high pressure cryogen liquid pipeline low temperature heat exchanger (J) after vaporizer (6) and the second cryogenic throttle valve (N) are communicated with low temperature heat exchanger (J) to have refrigerant steam channel to be communicated with compressor (H) again, low temperature heat exchanger (J) also has cryogenic media pipeline and ft connection, second condenser (L) also has heated medium pipeline and ft connection, vaporizer (6) also has refrigerant steam channel to be communicated with adsorber (1), adsorber (1) also has dilute solution pipeline to be communicated with the second adsorber (2) with solution heat exchanger (10) through solution pump (8), second adsorber (2) also has dilute solution pipeline to be communicated with generator (3) with the second solution heat exchanger (11) through the second solution pump (9), generator (3) also has concentrated solution pipeline to be communicated with the second generator (4) through the second solution heat exchanger (11), second generator (4) also has concentrated solution pipeline to be communicated with adsorber (1) through solution heat exchanger (10), generator (3) also has refrigerant steam channel to be communicated with condenser (5), second generator (4) also has refrigerant steam channel to be communicated with the second adsorber (2), condenser (5) also has cryogen liquid pipeline to be communicated with vaporizer (6) through throttle valve (7), adsorber (1), second adsorber (2) and condenser (5) also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger form fuel gas-steam forward circulation system, and compressor, the second compressor, the second condenser, vaporizer, cryogenic throttle valve, the second cryogenic throttle valve and low temperature heat exchanger form compression type reverse circulation system, adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system, fuel gas-steam forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, fuel gas-steam forward circulation provides driving heat load to absorption reverse circulation, compression type reverse circulation obtain Low Temperature Thermal load and respectively by the external heat supply of the second condenser and by vaporizer to absorption reverse circulation heat supply, absorption reverse circulation, by adsorber, the second adsorber and the external heat supply of condenser, forms combined cycle energy supplying system.

8. combined cycle energy supplying system, formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, the second condenser, vaporizer, cryogenic throttle valve, the second cryogenic throttle valve, low temperature heat exchanger, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, gas compressor (A) has air passageways and ft connection, gas compressor (A) also has compressed air channel to be communicated with firing chamber (B), firing chamber (B) also has fuel channel and ft connection, firing chamber (B) also has blast tube to be communicated with gas turbine (C), gas turbine (C) also has blast tube to be communicated with exhaust heat boiler (E), exhaust heat boiler (E) also have blast tube be communicated with successively generator (3) and the second generator (4) afterwards the second generator (4) have blast tube and ft connection again, steam turbine (D) has low pressure steam passage to be communicated with heat exchanger (G), heat exchanger (G) also has condensed fluid pipeline to be communicated with exhaust heat boiler (E) through recycle pump (F), exhaust heat boiler (E) also has high pressure steam passage to be communicated with steam turbine (D), heat exchanger (G) also has heated medium pipeline and ft connection, compressor (H) has low pressure refrigerant steam channel to be communicated with vaporizer (6), vaporizer (6) also has low pressure cryogen liquid pipeline low temperature heat exchanger (J) after cryogenic throttle valve (I) is communicated with low temperature heat exchanger (J) to have refrigerant steam channel to be communicated with compressor (H) again, compressor (H) also has high pressure refrigerant steam channel to be communicated with the second condenser (L), second condenser (L) also has high pressure cryogen liquid pipeline low temperature heat exchanger (J) after vaporizer (6) and the second cryogenic throttle valve (N) are communicated with low temperature heat exchanger (J) to have refrigerant steam channel to be communicated with compressor (H) again, low temperature heat exchanger (J) also has cryogenic media pipeline and ft connection, second condenser (L) also has heated medium pipeline and ft connection, vaporizer (6) also has refrigerant steam channel to be communicated with adsorber (1), adsorber (1) also has dilute solution pipeline to be communicated with the second adsorber (2) with solution heat exchanger (10) through solution pump (8), second adsorber (2) also has dilute solution pipeline to be communicated with generator (3) with the second solution heat exchanger (11) through the second solution pump (9), generator (3) also has concentrated solution pipeline to be communicated with the second generator (4) through the second solution heat exchanger (11), second generator (4) also has concentrated solution pipeline to be communicated with adsorber (1) through solution heat exchanger (10), generator (3) also has refrigerant steam channel to be communicated with condenser (5), second generator (4) also has refrigerant steam channel to be communicated with the second adsorber (2), condenser (5) also has cryogen liquid pipeline to be communicated with vaporizer (6) through throttle valve (7), adsorber (1), second adsorber (2) and condenser (5) also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger form fuel gas-steam forward circulation system, compressor, the second condenser, vaporizer, cryogenic throttle valve, the second cryogenic throttle valve and low temperature heat exchanger form compression type reverse circulation system, and adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system, fuel gas-steam forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, fuel gas-steam forward circulation provides driving heat load to absorption reverse circulation, compression type reverse circulation obtain Low Temperature Thermal load and respectively by the external heat supply of the second condenser and by vaporizer to absorption reverse circulation heat supply, absorption reverse circulation, by adsorber, the second adsorber and the external heat supply of condenser, forms combined cycle energy supplying system.

9. combined cycle energy supplying system, formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, vaporizer, decompressor, low temperature heat exchanger, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, gas compressor (A) has air passageways and ft connection, gas compressor (A) also has compressed air channel to be communicated with firing chamber (B), firing chamber (B) also has fuel channel and ft connection, firing chamber (B) also has blast tube to be communicated with gas turbine (C), gas turbine (C) also has blast tube to be communicated with exhaust heat boiler (E), exhaust heat boiler (E) also have blast tube be communicated with successively generator (3) and the second generator (4) afterwards the second generator (4) have blast tube and ft connection again, steam turbine (D) has low pressure steam passage to be communicated with heat exchanger (G), heat exchanger (G) also has condensed fluid pipeline to be communicated with exhaust heat boiler (E) through recycle pump (F), exhaust heat boiler (E) also has high pressure steam passage to be communicated with steam turbine (D), heat exchanger (G) also has heated medium pipeline and ft connection, the finisher (6) that compressor (H) has refrigerant gas passage to be communicated with vaporizer (6) has refrigerant gas passage to be communicated with decompressor (O) again, decompressor (O) also has refrigerant gas passage to be communicated with compressor (H) through low temperature heat exchanger (J), and low temperature heat exchanger (J) also has cryogenic media pipeline and ft connection, vaporizer (6) also has refrigerant steam channel to be communicated with adsorber (1), adsorber (1) also has dilute solution pipeline to be communicated with the second adsorber (2) with solution heat exchanger (10) through solution pump (8), second adsorber (2) also has dilute solution pipeline to be communicated with generator (3) with the second solution heat exchanger (11) through the second solution pump (9), generator (3) also has concentrated solution pipeline to be communicated with the second generator (4) through the second solution heat exchanger (11), second generator (4) also has concentrated solution pipeline to be communicated with adsorber (1) through solution heat exchanger (10), generator (3) also has refrigerant steam channel to be communicated with condenser (5), second generator (4) also has refrigerant steam channel to be communicated with the second adsorber (2), condenser (5) also has cryogen liquid pipeline to be communicated with vaporizer (6) through throttle valve (7), adsorber (1), second adsorber (2) and condenser (5) also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger form fuel gas-steam forward circulation system, compressor, vaporizer, decompressor and low temperature heat exchanger form compression type reverse circulation system, and adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system, fuel gas-steam forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, fuel gas-steam forward circulation provides driving heat load to absorption reverse circulation, compression type reverse circulation obtains Low Temperature Thermal load by vaporizer to absorption reverse circulation heat supply, absorption reverse circulation, by adsorber, the second adsorber and the external heat supply of condenser, forms combined cycle energy supplying system.

10. combined cycle energy supplying system, in combined cycle energy supplying system according to claim 9, increase by the second compressor, the finisher (6) being had by compressor (H) refrigerant gas passage to be communicated with vaporizer (6) has refrigerant gas passage to be communicated with decompressor (O) to be adjusted to compressor (H) finisher (6) having refrigerant gas passage to be communicated with vaporizer (6) to have refrigerant gas passage to be communicated with the second compressor (K) more again, the finisher (6) that second compressor (K) also has refrigerant gas passage to be communicated with vaporizer (6) has refrigerant gas passage to be communicated with decompressor (O) again, form combined cycle energy supplying system.

11. combined cycle energy supplying systems, formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, vaporizer, decompressor, low temperature heat exchanger, regenerator, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, gas compressor (A) has air passageways and ft connection, gas compressor (A) also has compressed air channel to be communicated with firing chamber (B), firing chamber (B) also has fuel channel and ft connection, firing chamber (B) also has blast tube to be communicated with gas turbine (C), gas turbine (C) also has blast tube to be communicated with exhaust heat boiler (E), exhaust heat boiler (E) also have blast tube be communicated with successively generator (3) and the second generator (4) afterwards the second generator (4) have blast tube and ft connection again, steam turbine (D) has low pressure steam passage to be communicated with heat exchanger (G), heat exchanger (G) also has condensed fluid pipeline to be communicated with exhaust heat boiler (E) through recycle pump (F), exhaust heat boiler (E) also has high pressure steam passage to be communicated with steam turbine (D), heat exchanger (G) also has heated medium pipeline and ft connection, the finisher (6) that compressor (H) has refrigerant gas passage to be communicated with vaporizer (6) has refrigerant gas passage to be communicated with decompressor (O) through regenerator (P) again, decompressor (O) also has refrigerant gas passage to be communicated with compressor (H) with regenerator (P) through low temperature heat exchanger (J), and low temperature heat exchanger (J) also has cryogenic media pipeline and ft connection, vaporizer (6) also has refrigerant steam channel to be communicated with adsorber (1), adsorber (1) also has dilute solution pipeline to be communicated with the second adsorber (2) with solution heat exchanger (10) through solution pump (8), second adsorber (2) also has dilute solution pipeline to be communicated with generator (3) with the second solution heat exchanger (11) through the second solution pump (9), generator (3) also has concentrated solution pipeline to be communicated with the second generator (4) through the second solution heat exchanger (11), second generator (4) also has concentrated solution pipeline to be communicated with adsorber (1) through solution heat exchanger (10), generator (3) also has refrigerant steam channel to be communicated with condenser (5), second generator (4) also has refrigerant steam channel to be communicated with the second adsorber (2), condenser (5) also has cryogen liquid pipeline to be communicated with vaporizer (6) through throttle valve (7), adsorber (1), second adsorber (2) and condenser (5) also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger form fuel gas-steam forward circulation system, compressor, vaporizer, decompressor, low temperature heat exchanger and regenerator form compression type reverse circulation system, and adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system, fuel gas-steam forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, fuel gas-steam forward circulation provides driving heat load to absorption reverse circulation, compression type reverse circulation obtains Low Temperature Thermal load by vaporizer to absorption reverse circulation heat supply, absorption reverse circulation, by adsorber, the second adsorber and the external heat supply of condenser, forms combined cycle energy supplying system.

12. combined cycle energy supplying systems, in combined cycle energy supplying system according to claim 11, increase by the second compressor, the finisher (6) being had by compressor (H) refrigerant gas passage to be communicated with vaporizer (6) has refrigerant gas passage to be communicated with through regenerator (P) finisher (6) being adjusted to compressor (H) and having refrigerant gas passage to be communicated with logical vaporizer (6) with decompressor (O) again has refrigerant gas passage to be communicated with the second compressor (K) again, the finisher (6) that second compressor (K) also has refrigerant gas passage to be communicated with vaporizer (6) has refrigerant gas passage to be communicated with decompressor (O) through regenerator (P) again, form combined cycle energy supplying system.

13. combined cycle energy supplying systems, formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, decompressor, cooler, low temperature heat exchanger, vaporizer, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, gas compressor (A) has air passageways and ft connection, gas compressor (A) also has compressed air channel to be communicated with firing chamber (B), firing chamber (B) also has fuel channel and ft connection, firing chamber (B) also has blast tube to be communicated with gas turbine (C), gas turbine (C) also has blast tube to be communicated with exhaust heat boiler (E), exhaust heat boiler (E) also have blast tube be communicated with successively generator (3) and the second generator (4) afterwards the second generator (4) have blast tube and ft connection again, steam turbine (D) has low pressure steam passage to be communicated with heat exchanger (G), heat exchanger (G) also has condensed fluid pipeline to be communicated with exhaust heat boiler (E) through recycle pump (F), exhaust heat boiler (E) also has high pressure steam passage to be communicated with steam turbine (D), heat exchanger (G) also has heated medium pipeline and ft connection, compressor (H) has refrigerant gas passage to be communicated with decompressor (O) through cooler (M), decompressor (O) also has refrigerant gas passage to be communicated with compressor (H) through low temperature heat exchanger (J), low temperature heat exchanger (J) also has cryogenic media pipeline and ft connection, and cooler (M) also has heated medium pipeline and ft connection, vaporizer (6) has refrigerant steam channel to be communicated with adsorber (1), adsorber (1) also has dilute solution pipeline to be communicated with the second adsorber (2) with solution heat exchanger (10) through solution pump (8), second adsorber (2) also has dilute solution pipeline to be communicated with generator (3) with the second solution heat exchanger (11) through the second solution pump (9), generator (3) also has concentrated solution pipeline to be communicated with the second generator (4) through the second solution heat exchanger (11), second generator (4) also has concentrated solution pipeline to be communicated with adsorber (1) through solution heat exchanger (10), generator (3) also has refrigerant steam channel to be communicated with condenser (5), second generator (4) also has refrigerant steam channel to be communicated with the second adsorber (2), condenser (5) also has cryogen liquid pipeline to be communicated with vaporizer (6) through throttle valve (7), vaporizer (6) also has cryogenic media pipeline and ft connection, adsorber (1), second adsorber (2) and condenser (5) also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger form fuel gas-steam forward circulation system, compressor, cooler, decompressor and low temperature heat exchanger form compression type reverse circulation system, and adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system, fuel gas-steam forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, fuel gas-steam forward circulation provides driving heat load to absorption reverse circulation, compression type reverse circulation obtains Low Temperature Thermal load and passes through the external heat supply of cooler, absorption reverse circulation obtains Low Temperature Thermal load and by adsorber, the second adsorber and the external heat supply of condenser, forms combined cycle energy supplying system.

14. combined cycle energy supplying systems, in combined cycle energy supplying system according to claim 13, increase by the second compressor, had by compressor (H) refrigerant gas passage to be communicated with decompressor (O) through cooler (M) to be adjusted to compressor (H) and to have refrigerant gas passage to be communicated with the second compressor (K) through cooler (M), second compressor (K) also has refrigerant gas passage to be communicated with decompressor (O) through cooler (M), forms combined cycle energy supplying system.

15. combined cycle energy supplying systems, formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, cooler, decompressor, low temperature heat exchanger, regenerator, vaporizer, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, gas compressor (A) has air passageways and ft connection, gas compressor (A) also has compressed air channel to be communicated with firing chamber (B), firing chamber (B) also has fuel channel and ft connection, firing chamber (B) also has blast tube to be communicated with gas turbine (C), gas turbine (C) also has blast tube to be communicated with exhaust heat boiler (E), exhaust heat boiler (E) also have blast tube be communicated with successively generator (3) and the second generator (4) afterwards the second generator (4) have blast tube and ft connection again, steam turbine (D) has low pressure steam passage to be communicated with heat exchanger (G), heat exchanger (G) also has condensed fluid pipeline to be communicated with exhaust heat boiler (E) through recycle pump (F), exhaust heat boiler (E) also has high pressure steam passage to be communicated with steam turbine (D), heat exchanger (G) also has heated medium pipeline and ft connection, compressor (H) has refrigerant gas passage to be communicated with decompressor (O) with regenerator (P) through cooler (M), decompressor (O) also has refrigerant gas passage to be communicated with compressor (H) with regenerator (P) through low temperature heat exchanger (J), low temperature heat exchanger (J) also has cryogenic media pipeline and ft connection, and cooler (M) also has heated medium pipeline and ft connection, vaporizer (6) has refrigerant steam channel to be communicated with adsorber (1), adsorber (1) also has dilute solution pipeline to be communicated with the second adsorber (2) with solution heat exchanger (10) through solution pump (8), second adsorber (2) also has dilute solution pipeline to be communicated with generator (3) with the second solution heat exchanger (11) through the second solution pump (9), generator (3) also has concentrated solution pipeline to be communicated with the second generator (4) through the second solution heat exchanger (11), second generator (4) also has concentrated solution pipeline to be communicated with adsorber (1) through solution heat exchanger (10), generator (3) also has refrigerant steam channel to be communicated with condenser (5), second generator (4) also has refrigerant steam channel to be communicated with the second adsorber (2), condenser (5) also has cryogen liquid pipeline to be communicated with vaporizer (6) through throttle valve (7), vaporizer (6) also has cryogenic media pipeline and ft connection, adsorber (1), second adsorber (2) and condenser (5) also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger form fuel gas-steam forward circulation system, compressor, cooler, decompressor, low temperature heat exchanger and regenerator form compression type reverse circulation system, and adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system, fuel gas-steam forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, fuel gas-steam forward circulation provides driving heat load to absorption reverse circulation, compression type reverse circulation obtains Low Temperature Thermal load and passes through the external heat supply of cooler, absorption reverse circulation obtains Low Temperature Thermal load and by adsorber, the second adsorber and the external heat supply of condenser, forms combined cycle energy supplying system.

16. combined cycle energy supplying systems, in combined cycle energy supplying system according to claim 15, increase by the second compressor, had by compressor (H) refrigerant gas passage to be communicated with decompressor (O) through cooler (M) and regenerator (P) to be adjusted to compressor (H) and to have refrigerant gas passage to be communicated with the second compressor (K) through cooler (M), second compressor (K) has refrigerant gas passage to be communicated with decompressor (O) with regenerator (P) through cooler (M) again, forms combined cycle energy supplying system.

17. combined cycle energy supplying systems, formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, cooler, vaporizer, decompressor, low temperature heat exchanger, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, gas compressor (A) has air passageways and ft connection, gas compressor (A) also has compressed air channel to be communicated with firing chamber (B), firing chamber (B) also has fuel channel and ft connection, firing chamber (B) also has blast tube to be communicated with gas turbine (C), gas turbine (C) also has blast tube to be communicated with exhaust heat boiler (E), exhaust heat boiler (E) also have blast tube be communicated with successively generator (3) and the second generator (4) afterwards the second generator (4) have blast tube and ft connection again, steam turbine (D) has low pressure steam passage to be communicated with heat exchanger (G), heat exchanger (G) also has condensed fluid pipeline to be communicated with exhaust heat boiler (E) through recycle pump (F), exhaust heat boiler (E) also has high pressure steam passage to be communicated with steam turbine (D), heat exchanger (G) also has heated medium pipeline and ft connection, compressor (H) has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor (O) again through the finisher (6) that cooler (M) is communicated with vaporizer (6), decompressor (O) also has refrigerant gas passage to be communicated with compressor (H) through low temperature heat exchanger (J), low temperature heat exchanger (J) also has cryogenic media pipeline and ft connection, and cooler (M) also has heated medium pipeline and ft connection, vaporizer (6) also has refrigerant steam channel to be communicated with adsorber (1), adsorber (1) also has dilute solution pipeline to be communicated with the second adsorber (2) with solution heat exchanger (10) through solution pump (8), second adsorber (2) also has dilute solution pipeline to be communicated with generator (3) with the second solution heat exchanger (11) through the second solution pump (9), generator (3) also has concentrated solution pipeline to be communicated with the second generator (4) through the second solution heat exchanger (11), second generator (4) also has concentrated solution pipeline to be communicated with adsorber (1) through solution heat exchanger (10), generator (3) also has refrigerant steam channel to be communicated with condenser (5), second generator (4) also has refrigerant steam channel to be communicated with the second adsorber (2), condenser (5) also has cryogen liquid pipeline to be communicated with vaporizer (6) through throttle valve (7), adsorber (1), second adsorber (2) and condenser (5) also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger form fuel gas-steam forward circulation system, compressor, cooler, vaporizer, decompressor and low temperature heat exchanger form compression type reverse circulation system, and adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system, fuel gas-steam forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, fuel gas-steam forward circulation provides driving heat load to absorption reverse circulation, compression type reverse circulation obtain Low Temperature Thermal load and respectively by the external heat supply of cooler and by vaporizer to absorption reverse circulation heat supply, absorption reverse circulation, by adsorber, the second adsorber and the external heat supply of condenser, forms combined cycle energy supplying system.

18. combined cycle energy supplying systems, in combined cycle energy supplying system according to claim 17, increase by the second compressor, refrigerant gas passage is had by compressor (H) to have refrigerant gas passage to be communicated with decompressor (O) to be again adjusted to compressor (H) through the finisher (6) that cooler (M) is communicated with vaporizer (6) and have refrigerant gas passage to have refrigerant gas passage to be communicated with the second compressor (K) again through the finisher (6) that cooler (M) is communicated with vaporizer (6), second compressor (K) also has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor (O) again through the finisher (6) that cooler (M) is communicated with vaporizer (6), form combined cycle energy supplying system.

19. combined cycle energy supplying systems, formed primarily of gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump, heat exchanger, compressor, cooler, vaporizer, regenerator, decompressor, low temperature heat exchanger, adsorber, the second adsorber, generator, the second generator, condenser, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger, gas compressor (A) has air passageways and ft connection, gas compressor (A) also has compressed air channel to be communicated with firing chamber (B), firing chamber (B) also has fuel channel and ft connection, firing chamber (B) also has blast tube to be communicated with gas turbine (C), gas turbine (C) also has blast tube to be communicated with exhaust heat boiler (E), exhaust heat boiler (E) also have blast tube be communicated with successively generator (3) and the second generator (4) afterwards the second generator (4) have blast tube and ft connection again, steam turbine (D) has low pressure steam passage to be communicated with heat exchanger (G), heat exchanger (G) also has condensed fluid pipeline to be communicated with exhaust heat boiler (E) through recycle pump (F), exhaust heat boiler (E) also has high pressure steam passage to be communicated with steam turbine (D), heat exchanger (G) also has heated medium pipeline and ft connection, compressor (H) has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor (O) through regenerator (P) again through the finisher (6) that cooler (M) is communicated with vaporizer (6), decompressor (O) also has refrigerant gas passage to be communicated with compressor (H) with regenerator (P) through low temperature heat exchanger (J), low temperature heat exchanger (J) also has cryogenic media pipeline and ft connection, and cooler (M) also has heated medium pipeline and ft connection, vaporizer (6) also has refrigerant steam channel to be communicated with adsorber (1), adsorber (1) also has dilute solution pipeline to be communicated with the second adsorber (2) with solution heat exchanger (10) through solution pump (8), second adsorber (2) also has dilute solution pipeline to be communicated with generator (3) with the second solution heat exchanger (11) through the second solution pump (9), generator (3) also has concentrated solution pipeline to be communicated with the second generator (4) through the second solution heat exchanger (11), second generator (4) also has concentrated solution pipeline to be communicated with adsorber (1) through solution heat exchanger (10), generator (3) also has refrigerant steam channel to be communicated with condenser (5), second generator (4) also has refrigerant steam channel to be communicated with the second adsorber (2), condenser (5) also has cryogen liquid pipeline to be communicated with vaporizer (6) through throttle valve (7), adsorber (1), second adsorber (2) and condenser (5) also have heated medium pipeline and ft connection respectively, gas compressor, firing chamber, gas turbine, steam turbine, exhaust heat boiler, recycle pump and heat exchanger form fuel gas-steam forward circulation system, compressor, cooler, vaporizer, regenerator, decompressor and low temperature heat exchanger form compression type reverse circulation system, and adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger and the second solution heat exchanger form absorption reverse circulation system, fuel gas-steam forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, fuel gas-steam forward circulation provides driving heat load to absorption reverse circulation, compression type reverse circulation obtain Low Temperature Thermal load and respectively by the external heat supply of cooler and by vaporizer to absorption reverse circulation heat supply, absorption reverse circulation, by adsorber, the second adsorber and the external heat supply of condenser, forms combined cycle energy supplying system.

20. combined cycle energy supplying systems, in combined cycle energy supplying system according to claim 19, increase by the second compressor, had by compressor (H) refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor (O) through regenerator (P) again through the finisher (6) that cooler (M) is communicated with vaporizer (6) to be adjusted to compressor (H) and to have refrigerant gas passage to have refrigerant gas passage to be communicated with the second compressor (K) again through the finisher (6) that cooler (M) is communicated with vaporizer (6), second compressor (K) also has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor (O) through regenerator (P) again through the finisher (6) that cooler (M) is communicated with vaporizer (6), form combined cycle energy supplying system.

21. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-20, increase high temperature regenerator, being had by gas compressor (A) compressed air channel to be communicated with firing chamber (B) to be adjusted to gas compressor (A) has compressed air channel to be communicated with firing chamber (B) through high temperature regenerator (Q), being had by gas turbine (C) blast tube to be communicated with exhaust heat boiler (E) to be adjusted to gas turbine (C) has blast tube to be communicated with exhaust heat boiler (E) through high temperature regenerator (Q), forms combined cycle energy supplying system.

22. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-21, increase by the 3rd generator, second throttle, 3rd solution pump and the 3rd solution heat exchanger, second adsorber (2) is set up dilute solution pipeline and is communicated with the 3rd generator (13) with the 3rd solution heat exchanger (16) through the 3rd solution pump (15), 3rd generator (13) also has concentrated solution pipeline to be communicated with the second generator (4) through the 3rd solution heat exchanger (16), had by generator (3) refrigerant steam channel to be communicated with condenser (5) to be adjusted to generator (3) have refrigerant steam channel be communicated with the 3rd generator (13) after the 3rd generator (13) have cryogen liquid pipeline to be communicated with condenser (5) through second throttle (14) again, 3rd generator (13) also has refrigerant steam channel to be communicated with condenser (5), form combined cycle energy supplying system.

23. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-21, increase by the 3rd generator, second throttle and the 3rd solution heat exchanger, had by second adsorber (2) dilute solution pipeline to be communicated with generator (3) through the second solution pump (9) and the second solution heat exchanger (11) to be adjusted to the second adsorber (2) and to have dilute solution pipeline through the second solution pump (9), second solution heat exchanger (11) is communicated with generator (3) with the 3rd solution heat exchanger (16), had by generator (3) concentrated solution pipeline to be communicated with the second generator (4) through the second solution heat exchanger (11) to be adjusted to generator (3) and to have concentrated solution pipeline to be communicated with the 3rd generator (13) through the 3rd solution heat exchanger (16), 3rd generator (13) has concentrated solution pipeline to be communicated with the second generator (4) through the second solution heat exchanger (11) again, had by generator (3) refrigerant steam channel to be communicated with condenser (5) to be adjusted to generator (3) have refrigerant steam channel be communicated with the 3rd generator (13) after the 3rd generator (13) have cryogen liquid pipeline to be communicated with condenser (5) through second throttle (14) again, 3rd generator (13) also has refrigerant steam channel to be communicated with condenser (5), form combined cycle energy supplying system.

24. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-21, increase by the 3rd generator, second throttle, 3rd solution pump and the 3rd solution heat exchanger, had by second adsorber (2) dilute solution pipeline to be communicated with generator (3) through the second solution pump (9) and the second solution heat exchanger (11) to be adjusted to the second adsorber (2) and to have dilute solution pipeline to be communicated with the 3rd generator (13) with the second solution heat exchanger (11) through the second solution pump (9), 3rd generator (13) has concentrated solution pipeline to be communicated with generator (3) with the 3rd solution heat exchanger (16) through the 3rd solution pump (15) again, had by generator (3) concentrated solution pipeline to be communicated with the second generator (4) through the second solution heat exchanger (11) to be adjusted to generator (3) and to have concentrated solution pipeline to be communicated with the second generator (4) with the second solution heat exchanger (11) through the 3rd solution heat exchanger (16), had by generator (3) refrigerant steam channel to be communicated with condenser (5) to be adjusted to generator (3) have refrigerant steam channel be communicated with the 3rd generator (13) after the 3rd generator (13) have cryogen liquid pipeline to be communicated with condenser (5) through second throttle (14) again, 3rd generator (13) also has refrigerant steam channel to be communicated with condenser (5), form combined cycle energy supplying system.

25. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-21, increase by the 3rd generator, second throttle, 3rd solution pump and the 3rd solution heat exchanger, generator (3) is had blast tube be communicated with the second generator (4) after the second generator (4) have again blast tube and ft connection be adjusted to generator (3) have blast tube be communicated with the 3rd generator (13) and the second generator (4) successively after the second generator (4) have blast tube and ft connection again, second adsorber (2) is set up dilute solution pipeline and is communicated with the 3rd generator (13) with the 3rd solution heat exchanger (16) through the 3rd solution pump (15), 3rd generator (13) also has concentrated solution pipeline to be communicated with the second generator (4) through the 3rd solution heat exchanger (16), had by generator (3) refrigerant steam channel to be communicated with condenser (5) to be adjusted to generator (3) have refrigerant steam channel be communicated with the 3rd generator (13) after the 3rd generator (13) have cryogen liquid pipeline to be communicated with condenser (5) through second throttle (14) again, 3rd generator (13) also has refrigerant steam channel to be communicated with condenser (5), form combined cycle energy supplying system.

26. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-21, increase by the 3rd generator, second throttle and the 3rd solution heat exchanger, generator (3) is had blast tube be communicated with the second generator (4) after the second generator (4) have again blast tube and ft connection be adjusted to generator (3) have blast tube be communicated with the 3rd generator (13) and the second generator (4) successively after the second generator (4) have blast tube and ft connection again, had by second adsorber (2) dilute solution pipeline to be communicated with generator (3) through the second solution pump (9) and the second solution heat exchanger (11) to be adjusted to the second adsorber (2) and to have dilute solution pipeline through the second solution pump (9), second solution heat exchanger (11) is communicated with generator (3) with the 3rd solution heat exchanger (16), had by generator (3) concentrated solution pipeline to be communicated with the second generator (4) through the second solution heat exchanger (11) to be adjusted to generator (3) and to have concentrated solution pipeline to be communicated with the 3rd generator (13) through the 3rd solution heat exchanger (16), 3rd generator (13) has concentrated solution pipeline to be communicated with the second generator (4) through the second solution heat exchanger (11) again, had by generator (3) refrigerant steam channel to be communicated with condenser (5) to be adjusted to generator (3) have refrigerant steam channel be communicated with the 3rd generator (13) after the 3rd generator (13) have cryogen liquid pipeline to be communicated with condenser (5) through second throttle (14) again, 3rd generator (13) also has refrigerant steam channel to be communicated with condenser (5), form combined cycle energy supplying system.

27. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-21, increase by the 3rd generator, second throttle, 3rd solution pump and the 3rd solution heat exchanger, generator (3) is had blast tube be communicated with the second generator (4) after the second generator (4) have again blast tube and ft connection be adjusted to generator (3) have blast tube be communicated with the 3rd generator (13) and the second generator (4) successively after the second generator (4) have blast tube and ft connection again, had by second adsorber (2) dilute solution pipeline to be communicated with generator (3) through the second solution pump (9) and the second solution heat exchanger (11) to be adjusted to the second adsorber (2) and to have dilute solution pipeline to be communicated with the 3rd generator (13) with the second solution heat exchanger (11) through the second solution pump (9), 3rd generator (13) has concentrated solution pipeline to be communicated with generator (3) with the 3rd solution heat exchanger (16) through the 3rd solution pump (15) again, had by generator (3) concentrated solution pipeline to be communicated with the second generator (4) through the second solution heat exchanger (11) to be adjusted to generator (3) and to have concentrated solution pipeline to be communicated with the second generator (4) with the second solution heat exchanger (11) through the 3rd solution heat exchanger (16), had by generator (3) refrigerant steam channel to be communicated with condenser (5) to be adjusted to generator (3) have refrigerant steam channel be communicated with the 3rd generator (13) after the 3rd generator (13) have cryogen liquid pipeline to be communicated with condenser (5) through second throttle (14) again, 3rd generator (13) also has refrigerant steam channel to be communicated with condenser (5), form combined cycle energy supplying system.

28. combined cycle energy supplying systems, in arbitrary combined cycle energy supplying system according to claim 22, increase by the 4th generator, 3rd throttle valve, 4th solution pump and the 4th solution heat exchanger, second adsorber (2) is set up dilute solution pipeline and is communicated with the 4th generator (17) with the 4th solution heat exchanger (20) through the 4th solution pump (19), 4th generator (17) also has concentrated solution pipeline to be communicated with the second generator (4) through the 4th solution heat exchanger (20), had by 3rd generator (13) refrigerant steam channel to be communicated with condenser (5) to be adjusted to the 3rd generator (13) have refrigerant steam channel be communicated with the 4th generator (17) after the 4th generator (17) have cryogen liquid pipeline to be communicated with condenser (5) through the 3rd throttle valve (18) again, 4th generator (17) also has refrigerant steam channel to be communicated with condenser (5), form combined cycle energy supplying system.

29. combined cycle energy supplying systems, in arbitrary combined cycle energy supplying system according to claim 23, increase by the 4th generator, 3rd throttle valve and the 4th solution heat exchanger, second adsorber (2) there is dilute solution pipeline through the second solution pump (9), second solution heat exchanger (11) and the 3rd solution heat exchanger (16) are communicated with generator (3) and are adjusted to the second adsorber (2) and have dilute solution pipeline through the second solution pump (9), second solution heat exchanger (11), 4th solution heat exchanger (20) is communicated with generator (3) with the 3rd solution heat exchanger (16), had by 3rd generator (13) concentrated solution pipeline to be communicated with the second generator (4) through the second solution heat exchanger (11) to be adjusted to the 3rd generator (13) and to have concentrated solution pipeline to be communicated with the 4th generator (17) through the 4th solution heat exchanger (20), 4th generator (17) has concentrated solution pipeline to be communicated with the second generator (4) through the second solution heat exchanger (11) again, had by 3rd generator (13) refrigerant steam channel to be communicated with condenser (5) to be adjusted to the 3rd generator (13) have refrigerant steam channel be communicated with the 4th generator (17) after the 4th generator (17) have cryogen liquid pipeline to be communicated with condenser (5) through the 3rd throttle valve (18) again, 4th generator (17) also has refrigerant steam channel to be communicated with condenser (5), form combined cycle energy supplying system.

30. combined cycle energy supplying systems, in arbitrary combined cycle energy supplying system according to claim 24, increase by the 4th generator, 3rd throttle valve, 4th solution pump and the 4th solution heat exchanger, had by second adsorber (2) dilute solution pipeline to be communicated with the 3rd generator (13) through the second solution pump (9) and the second solution heat exchanger (11) to be adjusted to the second adsorber (2) and to have dilute solution pipeline to be communicated with the 4th generator (17) with the second solution heat exchanger (11) through the second solution pump (9), 4th generator (17) has concentrated solution pipeline to be communicated with the 3rd generator (13) with the 4th solution heat exchanger (20) through the 4th solution pump (19) again, had by generator (3) concentrated solution pipeline to be communicated with the second generator (4) through the 3rd solution heat exchanger (16) and the second solution heat exchanger (11) to be adjusted to generator (3) and to have concentrated solution pipeline through the 3rd solution heat exchanger (16), 4th solution heat exchanger (20) is communicated with the second generator (4) with the second solution heat exchanger (11), had by 3rd generator (13) refrigerant steam channel to be communicated with condenser (5) to be adjusted to the 3rd generator (13) have refrigerant steam channel be communicated with the 4th generator (17) after the 4th generator (17) have cryogen liquid pipeline to be communicated with condenser (5) through the 3rd throttle valve (18) again, 4th generator (17) also has refrigerant steam channel to be communicated with condenser (5), form combined cycle energy supplying system.

31. combined cycle energy supplying systems, in arbitrary combined cycle energy supplying system according to claim 22, increase by the 4th generator, 3rd throttle valve, 4th solution pump and the 4th solution heat exchanger, generator (3) is had blast tube be communicated with the second generator (4) after the second generator (4) have blast tube and ft connection to be adjusted to generator (3) again to have blast tube to be communicated with the 3rd generator (13) successively, 4th generator (17) and the second generator (4) afterwards the second generator (4) have blast tube and ft connection again, second adsorber (2) is set up dilute solution pipeline and is communicated with the 4th generator (17) with the 4th solution heat exchanger (20) through the 4th solution pump (19), 4th generator (17) also has concentrated solution pipeline to be communicated with the second generator (4) through the 4th solution heat exchanger (20), had by 3rd generator (13) refrigerant steam channel to be communicated with condenser (5) to be adjusted to the 3rd generator (13) have refrigerant steam channel be communicated with the 4th generator (17) after the 4th generator (17) have cryogen liquid pipeline to be communicated with condenser (5) through the 3rd throttle valve (18) again, 4th generator (17) also has refrigerant steam channel to be communicated with condenser (5), form combined cycle energy supplying system.

32. combined cycle energy supplying systems, in arbitrary combined cycle energy supplying system according to claim 23, increase by the 4th generator, 3rd throttle valve and the 4th solution heat exchanger, generator (3) is had blast tube be communicated with the second generator (4) after the second generator (4) have blast tube and ft connection to be adjusted to generator (3) again to have blast tube to be communicated with the 3rd generator (13) successively, 4th generator (17) and the second generator (4) afterwards the second generator (4) have blast tube and ft connection again, second adsorber (2) there is dilute solution pipeline through the second solution pump (9), second solution heat exchanger (11) and the 3rd solution heat exchanger (16) are communicated with generator (3) and are adjusted to the second adsorber (2) and have dilute solution pipeline through the second solution pump (9), second solution heat exchanger (11), 4th solution heat exchanger (20) is communicated with generator (3) with the 3rd solution heat exchanger (16), had by 3rd generator (13) concentrated solution pipeline to be communicated with the second generator (4) through the second solution heat exchanger (11) to be adjusted to the 3rd generator (13) and to have concentrated solution pipeline to be communicated with the 4th generator (17) through the 4th solution heat exchanger (20), 4th generator (17) has concentrated solution pipeline to be communicated with the second generator (4) through the second solution heat exchanger (11) again, had by 3rd generator (13) refrigerant steam channel to be communicated with condenser (5) to be adjusted to the 3rd generator (13) have refrigerant steam channel be communicated with the 4th generator (17) after the 4th generator (17) have cryogen liquid pipeline to be communicated with condenser (5) through the 3rd throttle valve (18) again, 4th generator (17) also has refrigerant steam channel to be communicated with condenser (5), form combined cycle energy supplying system.

33. combined cycle energy supplying systems, in arbitrary combined cycle energy supplying system according to claim 24, increase by the 4th generator, 3rd throttle valve, 4th solution pump and the 4th solution heat exchanger, generator (3) is had blast tube be communicated with the second generator (4) after the second generator (4) have blast tube and ft connection to be adjusted to generator (3) again to have blast tube to be communicated with the 3rd generator (13) successively, 4th generator (17) and the second generator (4) afterwards the second generator (4) have blast tube and ft connection again, had by second adsorber (2) dilute solution pipeline to be communicated with the 3rd generator (13) through the second solution pump (9) and the second solution heat exchanger (11) to be adjusted to the second adsorber (2) and to have dilute solution pipeline to be communicated with the 4th generator (17) with the second solution heat exchanger (11) through the second solution pump (9), 4th generator (17) has concentrated solution pipeline to be communicated with the 3rd generator (13) with the 4th solution heat exchanger (20) through the 4th solution pump (19) again, had by generator (3) concentrated solution pipeline to be communicated with the second generator (4) through the 3rd solution heat exchanger (16) and the second solution heat exchanger (11) to be adjusted to generator (3) and to have concentrated solution pipeline through the 3rd solution heat exchanger (16), 4th solution heat exchanger (20) is communicated with the second generator (4) with the second solution heat exchanger (11), had by 3rd generator (13) refrigerant steam channel to be communicated with condenser (5) to be adjusted to the 3rd generator (13) have refrigerant steam channel be communicated with the 4th generator (17) after the 4th generator (17) have cryogen liquid pipeline to be communicated with condenser (5) through the 3rd throttle valve (18) again, 4th generator (17) also has refrigerant steam channel to be communicated with condenser (5), form combined cycle energy supplying system.

34. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 28-33, there is by 3rd generator (13) cryogen liquid pipeline to be communicated with condenser (5) through second throttle (14) to be adjusted to the 3rd generator (13) and to have cryogen liquid pipeline to be communicated with condenser (5) with second throttle (14) through the 4th generator (17), form combined cycle energy supplying system.

35. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-34, increase by the second heat exchanger, second heat exchanger (12) has heated medium pipeline and ft connection, and takes following wherein arbitrary technical measures to form combined cycle energy supplying system: 1. had by the second generator (4) blast tube and ft connection to be adjusted to the second generator (4) and have blast tube through the second heat exchanger (12) and ft connection; 2. there are by the second generator (4) blast tube and ft connection to be adjusted to the second generator (4) and have blast tube through the second heat exchanger (12) and vaporizer (6) and ft connection; 3. there are by the second generator (4) blast tube and ft connection to be adjusted to the second generator (4) and have blast tube through the second heat exchanger (12), vaporizer (6) and low temperature heat exchanger (F) and ft connection.

36. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-21, increase by the 3rd generator, 3rd solution pump, 3rd solution heat exchanger and the 3rd adsorber, second generator (4) is had blast tube and ft connection be adjusted to the second generator (4) have blast tube be communicated with the 3rd generator (13) after the 3rd generator (13) have blast tube and ft connection again, being had by vaporizer (6) refrigerant steam channel to be communicated with adsorber (1) to be adjusted to vaporizer (6) has refrigerant steam channel to be communicated with the 3rd adsorber (21), 3rd adsorber (21) also has dilute solution pipeline to be communicated with the 3rd generator (13) with the 3rd solution heat exchanger (16) through the 3rd solution pump (15), 3rd generator (13) also has concentrated solution pipeline to be communicated with the 3rd adsorber (21) through the 3rd solution heat exchanger (16), 3rd generator (13) also has refrigerant steam channel to be communicated with adsorber (1), 3rd adsorber (21) also has heated medium pipeline and ft connection, form combined cycle energy supplying system.

37. combined cycle energy supplying systems, in arbitrary combined cycle energy supplying system according to claim 36, increase by the second heat exchanger, second heat exchanger (12) has heated medium pipeline and ft connection, and takes following wherein arbitrary technical measures to form combined cycle energy supplying system: 1. had by the 3rd generator (13) blast tube and ft connection to be adjusted to the 3rd generator (13) and have blast tube through the second heat exchanger (12) and ft connection; 2. there are by the 3rd generator (13) blast tube and ft connection to be adjusted to the 3rd generator (13) and have blast tube through the second heat exchanger (12) and vaporizer (6) and ft connection; 3. there are by the 3rd generator (13) blast tube and ft connection to be adjusted to the 3rd generator (13) and have blast tube through the second heat exchanger (12), vaporizer (6) and low temperature heat exchanger (F) and ft connection.

38. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-21, increase high-temperature heat exchanger and the second recycle pump, exhaust heat boiler (E) is had blast tube be communicated with generator (3) and the second generator (4) successively after the second generator (4) have again blast tube and ft connection be adjusted to exhaust heat boiler (E) have blast tube be communicated with high-temperature heat exchanger (R) after high-temperature heat exchanger (R) have blast tube and ft connection again, high-temperature heat exchanger (R), the second recycle pump (S) and circulating thermal medium pipeline is relied on to form closed loop between generator (3) and the second generator (4), form combined cycle energy supplying system.

39. combined cycle energy supplying systems, in arbitrary combined cycle energy supplying system according to claim 38, increase by the second heat exchanger, second heat exchanger (8) has heated medium pipeline and ft connection, and take following wherein technical measures to form combined cycle energy supplying system: 1. by high-temperature heat exchanger (R), rely on the second recycle pump (S) and circulating thermal medium pipeline to form closed loop between generator (3) and the second generator (4) and be adjusted to high-temperature heat exchanger (R), generator (3), the second recycle pump (S) and circulating thermal medium pipeline is relied on to form closed loop between second generator (4) and the second heat exchanger (8), 2. by high-temperature heat exchanger (R), rely on the second recycle pump (S) and circulating thermal medium pipeline to form closed loop between generator (3) and the second generator (4) to be adjusted to high-temperature heat exchanger (R), generator (3), the second generator (4), between the second heat exchanger (8) and vaporizer (6), to rely on the second recycle pump (S) and circulating thermal medium pipeline formation closed loop, 3. by high-temperature heat exchanger (R), rely on the second recycle pump (S) and circulating thermal medium pipeline to form closed loop between generator (3) and the second generator (4) to be adjusted to high-temperature heat exchanger (R), generator (3), the second generator (4), the second heat exchanger (8), between vaporizer (6) and low temperature heat exchanger (J), to rely on the second recycle pump (S) and circulating thermal medium pipeline formation closed loop.

40. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-21, increase high-temperature heat exchanger, second recycle pump, 3rd generator, 3rd solution pump, 3rd solution heat exchanger and the 3rd adsorber, exhaust heat boiler (E) is had blast tube be communicated with generator (3) and the second generator (4) successively after the second generator (4) have again blast tube and ft connection be adjusted to exhaust heat boiler (E) have blast tube be communicated with high-temperature heat exchanger (R) after high-temperature heat exchanger (R) have blast tube and ft connection again, high-temperature heat exchanger (R), generator (3), the second recycle pump (S) and circulating thermal medium pipeline is relied on to form closed loop between second generator (4) and the 3rd generator (13), being had by vaporizer (6) refrigerant steam channel to be communicated with adsorber (1) to be adjusted to vaporizer (6) has refrigerant steam channel to be communicated with the 3rd adsorber (21), 3rd adsorber (21) also has dilute solution pipeline to be communicated with the 3rd generator (13) with the 3rd solution heat exchanger (16) through the 3rd solution pump (15), 3rd generator (13) also has concentrated solution pipeline to be communicated with the 3rd adsorber (21) through the 3rd solution heat exchanger (16), 3rd generator (13) also has refrigerant steam channel to be communicated with adsorber (1), 3rd adsorber (21) also has heated medium pipeline and ft connection, form combined cycle energy supplying system.

41. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-40, increase working machine, fuel gas-steam forward circulation provides power respectively to working machine (T), provides power and provide driving heat load to absorption reverse circulation to compression type reverse circulation, forms combined cycle energy supplying system.