CN105041396A - Combined cycle energy supply system - Google Patents

Combined cycle energy supply system Download PDF

Info

Publication number
CN105041396A
CN105041396A CN201510330916.8A CN201510330916A CN105041396A CN 105041396 A CN105041396 A CN 105041396A CN 201510330916 A CN201510330916 A CN 201510330916A CN 105041396 A CN105041396 A CN 105041396A
Authority
CN
China
Prior art keywords
generator
communicated
heat exchanger
solution
adsorber
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN201510330916.8A
Other languages
Chinese (zh)
Other versions
CN105041396B (en
Inventor
李华玉
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CN201510330916.8A priority Critical patent/CN105041396B/en
Publication of CN105041396A publication Critical patent/CN105041396A/en
Application granted granted Critical
Publication of CN105041396B publication Critical patent/CN105041396B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

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

Abstract

The invention provides a combined cycle energy supply system and belongs to the technical field of heat energy utilization and heat pumps. A steam power device positive cycle system is formed by a turbine, a boiler, a heat exchanger and a circulating pump. A compression type reverse cycle system is formed by a compressor, a cooler, an expander, a low-temperature heat exchanger and a heat regenerator. An absorption type reverse cycle system is composed of 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 steam power device 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 and supplies heat through the cooler. The absorption type reverse cycle acquires low-temperature heat loads and supplies heat through the absorber, the second absorber and the condenser. Thus, the combined cycle heat 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 steam power plant, 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, all gratifying working medium of the thermal performance of applicable absorption heat pump unit and Safety performance 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 steam power plant, 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 steam power plant 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, and efficiently heat and highly effective refrigeration under realizing low grade fuel situation.
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 turbo machine, boiler, heat exchanger, recycle pump, compressor, cryogenic throttle valve, low temperature heat exchanger, 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, turbo machine has low pressure steam passage to be communicated with heat exchanger, heat exchanger also has condensed fluid pipeline to be communicated with boiler through recycle pump, boiler also has high pressure steam passage to be communicated with turbo machine, boiler has fuel and air passageways and ft connection, 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, 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, turbo machine, boiler, heat exchanger and recycle pump form steam power plant 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, steam power plant forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, steam power plant 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 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 turbo machine, boiler, heat exchanger, recycle pump, compressor, the second condenser, cryogenic throttle valve, low temperature heat exchanger, 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, turbo machine has low pressure steam passage to be communicated with heat exchanger, heat exchanger also has condensed fluid pipeline to be communicated with boiler through recycle pump, boiler also has high pressure steam passage to be communicated with turbo machine, boiler has fuel and air passageways and ft connection, 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, 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 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, turbo machine, boiler, heat exchanger and recycle pump form steam power plant 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, steam power plant forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, steam power plant 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 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 turbo machine, boiler, heat exchanger, recycle pump, compressor, cooler, cryogenic throttle valve, low temperature heat exchanger, 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, turbo machine has low pressure steam passage to be communicated with heat exchanger, heat exchanger also has condensed fluid pipeline to be communicated with boiler through recycle pump, boiler also has high pressure steam passage to be communicated with turbo machine, boiler has fuel and air passageways and ft connection, 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, 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, turbo machine, boiler, heat exchanger and recycle pump form steam power plant 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, steam power plant forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, steam power plant 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 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 turbo machine, boiler, heat exchanger, recycle pump, compressor, the second compressor, the second condenser, cryogenic throttle valve, the second cryogenic throttle valve, low temperature heat exchanger, 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, turbo machine has low pressure steam passage to be communicated with heat exchanger, heat exchanger also has condensed fluid pipeline to be communicated with boiler through recycle pump, boiler also has high pressure steam passage to be communicated with turbo machine, boiler has fuel and air passageways and ft connection, 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, 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, turbo machine, boiler, heat exchanger and recycle pump form steam power plant forward circulation system, 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, 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, steam power plant forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, steam power plant 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 turbo machine, boiler, heat exchanger, recycle pump, compressor, the second condenser, cryogenic throttle valve, the second cryogenic throttle valve, low temperature heat exchanger, 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, turbo machine has low pressure steam passage to be communicated with heat exchanger, heat exchanger also has condensed fluid pipeline to be communicated with boiler through recycle pump, boiler also has high pressure steam passage to be communicated with turbo machine, boiler has fuel and air passageways and ft connection, 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, 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, turbo machine, boiler, heat exchanger and recycle pump form steam power plant 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, steam power plant forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, steam power plant 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 turbo machine, boiler, heat exchanger, recycle pump, compressor, decompressor, vaporizer, 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, turbo machine has low pressure steam passage to be communicated with heat exchanger, heat exchanger also has condensed fluid pipeline to be communicated with boiler through recycle pump, boiler also has high pressure steam passage to be communicated with turbo machine, boiler has fuel and air passageways and ft connection, 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, 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, turbo machine, boiler, heat exchanger and recycle pump form steam power plant 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, steam power plant forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, steam power plant 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 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 turbo machine, boiler, heat exchanger, recycle pump, 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, turbo machine has low pressure steam passage to be communicated with heat exchanger, heat exchanger also has condensed fluid pipeline to be communicated with boiler through recycle pump, boiler also has high pressure steam passage to be communicated with turbo machine, boiler has fuel and air passageways and ft connection, 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, 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, turbo machine, boiler, heat exchanger and recycle pump form steam power plant 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, steam power plant forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, steam power plant 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 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 turbo machine, boiler, heat exchanger, recycle pump, 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, turbo machine has low pressure steam passage to be communicated with heat exchanger, heat exchanger also has condensed fluid pipeline to be communicated with boiler through recycle pump, boiler also has high pressure steam passage to be communicated with turbo machine, boiler has fuel and air passageways and ft connection, 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, 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, turbo machine, boiler, heat exchanger and recycle pump form steam power plant 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 the absorption reverse circulation system of row, steam power plant forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, steam power plant 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 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 turbo machine, boiler, heat exchanger, recycle pump, 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, turbo machine has low pressure steam passage to be communicated with heat exchanger, heat exchanger also has condensed fluid pipeline to be communicated with boiler through recycle pump, boiler also has high pressure steam passage to be communicated with turbo machine, boiler has fuel and air passageways and ft connection, 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, 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, turbo machine, boiler, heat exchanger and recycle pump form steam power plant 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, steam power plant forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, steam power plant 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 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 turbo machine, boiler, heat exchanger, recycle pump, 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, turbo machine has low pressure steam passage to be communicated with heat exchanger, heat exchanger also has condensed fluid pipeline to be communicated with boiler through recycle pump, boiler also has high pressure steam passage to be communicated with turbo machine, boiler has fuel and air passageways and ft connection, 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, 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, turbo machine, boiler, heat exchanger and recycle pump form steam power plant 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, steam power plant forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, steam power plant 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 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 turbo machine, boiler, heat exchanger, recycle pump, 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, turbo machine has low pressure steam passage to be communicated with heat exchanger, heat exchanger also has condensed fluid pipeline to be communicated with boiler through recycle pump, boiler also has high pressure steam passage to be communicated with turbo machine, boiler has fuel and air passageways and ft connection, 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, 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, turbo machine, boiler, heat exchanger and recycle pump form steam power plant 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, steam power plant forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, steam power plant 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 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 claim 1-20, 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.
22. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-20, 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.
23. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-20, 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.
24. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-20, 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.
25. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-20, 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.
26. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-20, 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.
27. combined cycle energy supplying systems, in arbitrary combined cycle energy supplying system according to claim 21, 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.
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 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.
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, 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.
30. combined cycle energy supplying systems, in arbitrary combined cycle energy supplying system according to claim 21, 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.
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 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.
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, 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.
33. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 27-32, 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.
34. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-33, 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.
35. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-20, 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.
36. combined cycle energy supplying systems, in arbitrary combined cycle energy supplying system according to claim 35, 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.
37. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-20, increase exhaust heat boiler and the second recycle pump, 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 boiler have blast tube be communicated with exhaust heat boiler after exhaust heat boiler have blast tube and ft connection again, exhaust heat boiler, between generator and the second generator, rely on the second recycle pump and circulating thermal medium pipeline to form closed loop, form combined cycle energy supplying system.
38. combined cycle energy supplying systems, in arbitrary combined cycle energy supplying system according to claim 37, increase by the second heat exchanger, second heat exchanger has heated medium pipeline and ft connection, and take following wherein arbitrary technical measures to form combined cycle energy supplying system: 1. by exhaust heat boiler, 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 exhaust heat boiler, 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 exhaust heat boiler, 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 exhaust heat boiler, 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 exhaust heat boiler, 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 exhaust heat boiler, 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.
39. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-20, increase exhaust heat boiler, second recycle pump, 3rd generator, 3rd solution pump, 3rd solution heat exchanger and the 3rd adsorber, 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 boiler have blast tube be communicated with exhaust heat boiler after exhaust heat boiler have blast tube and ft connection again, exhaust heat boiler, 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.
40. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-39, increase working machine, steam power plant 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.
41. combined cycle energy supplying systems, are in the arbitrary combined cycle energy supplying system described in claim 1-40, fuel and air passageways are changed to high temperature heat source medium channel, blast tube is changed to low-temperature heat source medium channel, form 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-turbo machine, B-boiler, C-heat exchanger, D-recycle pump, E-compressor, F-cryogenic throttle valve, G-low temperature heat exchanger, H-second compressor, I-second condenser, J-cooler, K-second cryogenic throttle valve, L-decompressor, M-regenerator, N-exhaust heat boiler, O-second recycle pump, P-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-second 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 throttle 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) working medium---claim refrigerant vapour by the gaseous working medium in compressed steam circulation and Absorption heat-transformer, liquid refrigerant claims cryogen liquid; Working medium in being circulated by pressurized gas claims refrigerant gas, claims condensed fluid, as condensed fluid or other liquid medium by the liquid refrigerant in Steam Power Circulation.
(4) 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.
(5) 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.
(6) working machine---the working machine in the present invention comprises the equipment using mechanical energy, as compressor etc.; Also the equipment of the energy being other form is comprised changes mechanical energy, as generator etc.
(7) boiler---change fuel chemical energy into heat energy by burning and heating equipment is carried out to working medium; Here also comprise exhaust heat boiler, now high temperature heat source MEDIA FLOW heats working medium through boiler, and the heat source medium reduced after temperature is supplied to reverse circulation system and does to drive thermal medium.
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 turbo machine, boiler, heat exchanger, recycle pump, compressor, cryogenic throttle valve, low temperature heat exchanger, adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and working machine, turbo machine A has low pressure steam passage to be communicated with heat exchanger C, heat exchanger C also has condensed fluid pipeline to be communicated with boiler B through recycle pump D, boiler B also has high pressure steam passage to be communicated with turbo machine A, boiler B has fuel and air passageways and ft connection, boiler B 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, the finisher 6 that compressor E has refrigerant steam channel to be communicated with vaporizer 6 has cryogen liquid pipeline to be communicated with low temperature heat exchanger G through cryogenic throttle valve F again, low temperature heat exchanger G also has refrigerant steam channel to be communicated with compressor E, and low temperature heat exchanger G 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, turbo machine, boiler, heat exchanger, recycle pump and working machine form steam power plant 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, turbo machine, boiler, heat exchanger and recycle pump carry out steam power plant forward circulation---and high pressure steam enters turbo machine A step-down work done, low pressure steam after work done enters heat exchanger C and exothermic condensation, condensed fluid provides through the backward boiler B of recycle pump D pressurization, fuel and air enter boiler B and burn, condensed fluid absorbs heat into high pressure steam and provides to turbo machine A in boiler B, and the combustion gas after cooling is supplied to generator 3 and the second generator 4 is done to drive thermal medium, compressor, vaporizer, cryogenic throttle valve and low temperature heat exchanger carry out compression type reverse circulation---and refrigerant vapour enters compressor E, boosting flows through vaporizer 6 after heating up and heat release becomes cryogen liquid, and cryogen liquid enters low temperature heat exchanger G through cryogenic throttle valve F throttling, absorbs heat into refrigerant vapour and provide to compressor E, 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, steam power plant forward circulation provides power respectively to working machine and compression type reverse circulation, steam power plant forward circulation provides driving heat load to absorption reverse circulation, compression type reverse circulation obtains Low Temperature Thermal load and by vaporizer to absorption reverse circulation heat supply, absorption reverse circulation is by adsorber, the second adsorber and the external heat supply of condenser.
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 E refrigerant steam channel to be communicated with vaporizer 6 has cryogen liquid pipeline to be communicated with through cryogenic throttle valve F the finisher 6 being adjusted to compressor E and having refrigerant steam channel to be communicated with vaporizer 6 with low temperature heat exchanger G again has refrigerant steam channel to be communicated with the second compressor H again, and the finisher 6 that the second compressor H also has refrigerant steam channel to be communicated with vaporizer 6 has cryogen liquid pipeline to be communicated with low temperature heat exchanger G through cryogenic throttle valve F again; The refrigerant vapour that compressor E produces enters the second compressor H after flowing through vaporizer 6 heat release cooling, and the refrigerant vapour that the second compressor H 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, its main turbo machine, boiler, heat exchanger, recycle pump, compressor, the second condenser, cryogenic throttle valve, low temperature heat exchanger, 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 formed, turbo machine A has low pressure steam passage to be communicated with heat exchanger C, heat exchanger C also has condensed fluid pipeline to be communicated with boiler B through recycle pump D, boiler B also has high pressure steam passage to be communicated with turbo machine A, boiler B has fuel and air passageways and ft connection, boiler B 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, compressor E have refrigerant steam channel be communicated with the second condenser I after the second condenser I have cryogen liquid pipeline to be communicated with low temperature heat exchanger G through cryogenic throttle valve F again, low temperature heat exchanger G also has refrigerant steam channel to be communicated with compressor E, low temperature heat exchanger G also has cryogenic media pipeline and ft connection, and the second condenser I 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, turbo machine, boiler, heat exchanger and recycle pump form steam power plant 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 E, boosting flows through the second condenser I after heating up and heat release becomes cryogen liquid, and cryogen liquid enters low temperature heat exchanger G through cryogenic throttle valve F throttling, absorbs heat into refrigerant vapour and provide to compressor E; 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 E is had refrigerant steam channel be communicated with the second condenser I after the second condenser I have again cryogen liquid pipeline through cryogenic throttle valve F to be communicated with low temperature heat exchanger G be adjusted to compressor E have refrigerant steam channel to be communicated with the second condenser I after the second condenser I have refrigerant steam channel to be communicated with the second compressor H again, the second compressor H also have refrigerant steam channel be communicated with the second condenser I after the second condenser I have cryogen liquid pipeline to be communicated with low temperature heat exchanger G through cryogenic throttle valve F again; The refrigerant vapour that compressor E produces enters the second compressor H after flowing through the second condenser I heat release cooling, and the refrigerant vapour that the second compressor H produces provides to the second condenser I 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 turbo machine, boiler, heat exchanger, recycle pump, compressor, cooler, cryogenic throttle valve, low temperature heat exchanger, adsorber, the second adsorber, generator, the second generator, condenser, vaporizer, throttle valve, solution pump, the second solution pump, solution heat exchanger, the second solution heat exchanger and working machine, turbo machine A has low pressure steam passage to be communicated with heat exchanger C, heat exchanger C also has condensed fluid pipeline to be communicated with boiler B through recycle pump D, boiler B also has high pressure steam passage to be communicated with turbo machine A, boiler B has fuel and air passageways and ft connection, boiler B 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, the aftercooler J that compressor E has refrigerant steam channel to be communicated with cooler J 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 G through cryogenic throttle valve F, low temperature heat exchanger G also has refrigerant steam channel to be communicated with compressor E, low temperature heat exchanger G also has cryogenic media pipeline and ft connection, and cooler J 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, turbo machine, boiler, heat exchanger, recycle pump and working machine form steam power plant 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, difference is: compressor, cooler, vaporizer, cryogenic throttle valve and low temperature heat exchanger carry out compression type reverse circulation---refrigerant vapour enters compressor E, boosting flows through cooler J 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 G through cryogenic throttle valve F throttling, absorbs heat into refrigerant vapour and provide to compressor E.
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 J being had by compressor E refrigerant steam channel to be communicated with cooler J has refrigerant steam channel to be communicated with vaporizer 6 to be adjusted to compressor E the aftercooler J having refrigerant steam channel to be communicated with cooler J to have refrigerant steam channel to be communicated with the second compressor H more again, and the aftercooler J that the second compressor H also has refrigerant steam channel to be communicated with cooler J has refrigerant steam channel to be communicated with vaporizer 6 again; The refrigerant vapour that compressor E produces is supplied to the second compressor H after flowing through cooler J heat release cooling, and the refrigerant vapour that the second compressor H produces is supplied to vaporizer 6 after flowing through cooler J 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 turbo machine, boiler, heat exchanger, recycle pump, compressor, the second compressor, the second condenser, cryogenic throttle valve, the second cryogenic throttle valve, low temperature heat exchanger, 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, turbo machine A has low pressure steam passage to be communicated with heat exchanger C, heat exchanger C also has condensed fluid pipeline to be communicated with boiler B through recycle pump D, boiler B also has high pressure steam passage to be communicated with turbo machine A, boiler B has fuel and air passageways and ft connection, boiler B 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, compressor E 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 G after cryogenic throttle valve F is communicated with low temperature heat exchanger G to have refrigerant steam channel to be communicated with compressor E again, compressor E also has low pressure refrigerant steam channel to be communicated with the second compressor H, second compressor H also has high pressure refrigerant steam channel to be communicated with the second condenser I, second condenser I also has high pressure cryogen liquid pipeline low temperature heat exchanger G after vaporizer 6 and the second cryogenic throttle valve K are communicated with low temperature heat exchanger G to have refrigerant steam channel to be communicated with compressor E again, low temperature heat exchanger G also has cryogenic media pipeline and ft connection, second condenser I 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, turbo machine, boiler, heat exchanger and recycle pump form steam power plant forward circulation system, 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, 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, turbo machine, boiler, heat exchanger and recycle pump carry out steam power plant forward circulation---and high pressure steam enters turbo machine A step-down work done, low pressure steam after work done enters heat exchanger C and exothermic condensation, condensed fluid provides through the backward boiler B of recycle pump D pressurization, fuel and air enter boiler B and burn, condensed fluid absorbs heat into high pressure steam and provides to turbo machine A in boiler B, and the combustion gas after cooling is supplied to generator 3 and the second generator 4 is done to drive thermal medium, 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 E, the rear portion of compressed one-tenth low pressure refrigerant vapour is supplied to the second compressor H, another part flows through vaporizer 6 and heat release enters low temperature heat exchanger G through cryogenic throttle valve F throttling after becoming low pressure cryogen liquid again, absorb heat into refrigerant vapour and provide to compressor E, the high pressure refrigerant vapour that second compressor H produces flows through the second condenser I 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 G through the second cryogenic throttle valve K throttling again, absorb heat into refrigerant vapour and provide to compressor E, 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, steam power plant 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 turbo machine, boiler, heat exchanger, recycle pump, compressor, the second condenser, cryogenic throttle valve, the second cryogenic throttle valve, low temperature heat exchanger, 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, turbo machine A has low pressure steam passage to be communicated with heat exchanger C, heat exchanger C also has condensed fluid pipeline to be communicated with boiler B through recycle pump D, boiler B also has high pressure steam passage to be communicated with turbo machine A, boiler B has fuel and air passageways and ft connection, boiler B 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, compressor E 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 G after cryogenic throttle valve F is communicated with low temperature heat exchanger G to have refrigerant steam channel to be communicated with compressor E again, compressor E also has high pressure refrigerant steam channel to be communicated with the second condenser I, second condenser I also has high pressure cryogen liquid pipeline low temperature heat exchanger G after vaporizer 6 and the second cryogenic throttle valve K are communicated with low temperature heat exchanger G to have refrigerant steam channel to be communicated with compressor E again, low temperature heat exchanger G also has cryogenic media pipeline and ft connection, second condenser I 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, turbo machine, boiler, heat exchanger and recycle pump form steam power plant 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, turbo machine, boiler, heat exchanger and recycle pump carry out steam power plant forward circulation---and high pressure steam enters turbo machine A step-down work done, low pressure steam after work done enters heat exchanger C and exothermic condensation, condensed fluid provides through the backward boiler B of recycle pump D pressurization, fuel and air enter boiler B and burn, condensed fluid absorbs heat into high pressure steam and provides to turbo machine A in boiler B, and the combustion gas after cooling is supplied to generator 3 and the second generator 4 is done to drive thermal medium, 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 E, the rear portion of compressed one-tenth low pressure refrigerant vapour continues to be compressed into high pressure refrigerant vapour, another part flows through vaporizer 6 and heat release enters low temperature heat exchanger G through cryogenic throttle valve F throttling after becoming low pressure cryogen liquid again, absorb heat into refrigerant vapour and provide to compressor E, the high pressure refrigerant vapour that compressor E produces flows through the second condenser I 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 G through the second cryogenic throttle valve K throttling again, absorb heat into refrigerant vapour and provide to compressor E, 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, steam power plant 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 turbo machine, boiler, heat exchanger, recycle pump, compressor, decompressor, vaporizer, 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, turbo machine A has low pressure steam passage to be communicated with heat exchanger C, heat exchanger C also has condensed fluid pipeline to be communicated with boiler B through recycle pump D, boiler B also has high pressure steam passage to be communicated with turbo machine A, boiler B has fuel and air passageways and ft connection, boiler B 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, the finisher 6 that compressor E has refrigerant gas passage to be communicated with vaporizer 6 has refrigerant gas passage to be communicated with decompressor L again, decompressor L also has refrigerant gas passage to be communicated with compressor E through low temperature heat exchanger G, and low temperature heat exchanger G 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, turbo machine, boiler, heat exchanger, recycle pump and working machine form steam power plant 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, turbo machine, boiler, heat exchanger and recycle pump carry out steam power plant forward circulation---and high pressure steam enters turbo machine A step-down work done, low pressure steam after work done enters heat exchanger C and exothermic condensation, condensed fluid provides through the backward boiler B of recycle pump D pressurization, fuel and air enter boiler B and burn, condensed fluid absorbs heat into high pressure steam and provides to turbo machine A in boiler B, and the combustion gas after cooling is supplied to generator 3 and the second generator 4 is done to drive thermal medium, compressor, vaporizer, decompressor and low temperature heat exchanger carry out compression type reverse circulation---and refrigerant gas enters compressor E, boosting flows through vaporizer 6 after heating up and heat release cooling, and refrigerant gas flows through low temperature heat exchanger G after flowing through decompressor L step-down work done, heat absorption heats up and provides to compressor E, 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, steam power plant forward circulation provides power respectively to working machine and compression type reverse circulation, steam power plant 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 E refrigerant gas passage to be communicated with vaporizer 6 has refrigerant gas passage to be communicated with decompressor L to be adjusted to compressor E 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 H more again, the finisher 6 that second compressor H also has refrigerant gas passage to be communicated with vaporizer 6 has refrigerant gas passage to be communicated with decompressor L again, 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 turbo machine, boiler, heat exchanger, recycle pump, 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, turbo machine A has low pressure steam passage to be communicated with heat exchanger C, heat exchanger C also has condensed fluid pipeline to be communicated with boiler B through recycle pump D, boiler B also has high pressure steam passage to be communicated with turbo machine A, boiler B has fuel and air passageways and ft connection, boiler B 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, the finisher 6 that compressor E has refrigerant gas passage to be communicated with vaporizer 6 has refrigerant gas passage to be communicated with decompressor L through regenerator M again, decompressor L also has refrigerant gas passage to be communicated with compressor E with regenerator M through low temperature heat exchanger G, and low temperature heat exchanger G 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, turbo machine, boiler, heat exchanger, recycle pump and working machine form steam power plant 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.
(2) in flow process, compared with the energy supplying system of combined cycle shown in Fig. 9, difference is: the refrigerant gas that compressor E produces is supplied to regenerator M after flowing through vaporizer 6 heat release cooling, and refrigerant gas is supplied to decompressor L after flowing through regenerator M heat release cooling; After decompressor L work done, refrigerant gas flows through low temperature heat exchanger G and regenerator M, progressively heat absorption successively and is supplied to compressor E 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 E refrigerant gas passage to be communicated with vaporizer 6 has refrigerant gas passage to be communicated with through regenerator M the finisher 6 being adjusted to compressor E and having refrigerant gas passage to be communicated with logical vaporizer 6 with decompressor L again has refrigerant gas passage to be communicated with the second compressor H again, the finisher 6 that second compressor H also has refrigerant gas passage to be communicated with vaporizer 6 has refrigerant gas passage to be communicated with decompressor L through regenerator M again, 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 turbo machine, boiler, heat exchanger, recycle pump, 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, turbo machine A has low pressure steam passage to be communicated with heat exchanger C, heat exchanger C also has condensed fluid pipeline to be communicated with boiler B through recycle pump D, boiler B also has high pressure steam passage to be communicated with turbo machine A, boiler B has fuel and air passageways and ft connection, boiler B 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, compressor E has refrigerant gas passage to be communicated with decompressor L through cooler J, decompressor L also has refrigerant gas passage to be communicated with compressor E through low temperature heat exchanger G, low temperature heat exchanger G also has cryogenic media pipeline and ft connection, and cooler J 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, turbo machine, boiler, heat exchanger and recycle pump form steam power plant 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 the absorption reverse circulation system of row.
(2) in flow process, turbo machine, boiler, heat exchanger and recycle pump carry out steam power plant forward circulation---and high pressure steam enters turbo machine A step-down work done, low pressure steam after work done enters heat exchanger C and exothermic condensation, condensed fluid provides through the backward boiler B of recycle pump D pressurization, fuel and air enter boiler B and burn, condensed fluid absorbs heat into high pressure steam and provides to turbo machine A in boiler B, and the combustion gas after cooling is supplied to generator 3 and the second generator 4 is done to drive thermal medium, compressor, cooler, decompressor and low temperature heat exchanger carry out compression type reverse circulation---and refrigerant gas enters compressor E, boosting flows through cooler J after heating up and heat release cooling, and refrigerant gas flows through low temperature heat exchanger G after decompressor L step-down work done, heat absorption heats up and provides to compressor E, 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, steam power plant 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 E refrigerant gas passage to be communicated with decompressor L through cooler J to be adjusted to compressor E and to have refrigerant gas passage to be communicated with the second compressor H through cooler J, the second compressor H also has refrigerant gas passage to be communicated with decompressor L through cooler J; The refrigerant gas that compressor E produces is supplied to the second compressor H after flowing through cooler J heat release cooling, and the refrigerant gas that the second compressor H produces is supplied to decompressor L after flowing through cooler J heat release cooling, 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 turbo machine, boiler, heat exchanger, recycle pump, 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, turbo machine A has low pressure steam passage to be communicated with heat exchanger C, heat exchanger C also has condensed fluid pipeline to be communicated with boiler B through recycle pump D, boiler B also has high pressure steam passage to be communicated with turbo machine A, boiler B has fuel and air passageways and ft connection, boiler B 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, compressor E has refrigerant gas passage to be communicated with decompressor L with regenerator M through cooler J, decompressor L also has refrigerant gas passage to be communicated with compressor E with regenerator M through low temperature heat exchanger G, low temperature heat exchanger G also has cryogenic media pipeline and ft connection, and cooler J 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, turbo machine, boiler, heat exchanger and recycle pump form steam power plant 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 E produces is supplied to decompressor L after flowing through cooler J and regenerator M, heat release cooling successively, refrigerant gas flows through decompressor L step-down work done, and refrigerant gas flows through low temperature heat exchanger G and regenerator M more successively, the backward compressor E 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 E refrigerant gas passage to be communicated with decompressor L through cooler J and regenerator M to be adjusted to compressor E and to have refrigerant gas passage to be communicated with the second compressor H through cooler J, the second compressor H has refrigerant gas passage to be communicated with decompressor L with regenerator M through cooler J again; The refrigerant gas that compressor E produces is supplied to the second compressor H after flowing through cooler J heat release cooling, the refrigerant gas that second compressor H produces is supplied to decompressor L after flowing through cooler J and regenerator M, 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 turbo machine, boiler, heat exchanger, recycle pump, 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, turbo machine A has low pressure steam passage to be communicated with heat exchanger C, heat exchanger C also has condensed fluid pipeline to be communicated with boiler B through recycle pump D, boiler B also has high pressure steam passage to be communicated with turbo machine A, boiler B has fuel and air passageways and ft connection, boiler B 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, compressor E has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor L again through the finisher 6 that cooler J is communicated with vaporizer 6, decompressor L also has refrigerant gas passage to be communicated with compressor E through low temperature heat exchanger G, low temperature heat exchanger G also has cryogenic media pipeline and ft connection, and cooler J 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, turbo machine, boiler, heat exchanger and recycle pump form steam power plant 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, difference is: compressor E produce refrigerant gas flow through successively cooler J and vaporizer 6, progressively heat release cooling after be supplied to decompressor L, 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 E refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor L to be again adjusted to compressor E through the finisher 6 that cooler J is communicated with vaporizer 6 and have refrigerant gas passage to have refrigerant gas passage to be communicated with the second compressor H again through the finisher 6 that cooler J is communicated with vaporizer 6, the second compressor H also has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor L again through the finisher 6 that cooler J is communicated with vaporizer 6; The refrigerant gas that compressor E produces flows through cooler J successively and vaporizer 6, heat release are supplied to the second compressor H after lowering the temperature, the refrigerant gas that second compressor H produces flows through cooler J successively and vaporizer 6, heat release are supplied to decompressor L 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 turbo machine, boiler, heat exchanger, recycle pump, 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, turbo machine A has low pressure steam passage to be communicated with heat exchanger C, heat exchanger C also has condensed fluid pipeline to be communicated with boiler B through recycle pump D, boiler B also has high pressure steam passage to be communicated with turbo machine A, boiler B has fuel and air passageways and ft connection, boiler B 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, compressor E has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor L through regenerator M again through the finisher 6 that cooler J is communicated with vaporizer 6, decompressor L also has refrigerant gas passage to be communicated with compressor E with regenerator M through low temperature heat exchanger G, low temperature heat exchanger G also has cryogenic media pipeline and ft connection, and cooler J 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, turbo machine, boiler, heat exchanger and recycle pump form steam power plant 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 E produces is supplied to decompressor L after flowing through cooler J, vaporizer 6 and regenerator M heat release cooling successively, and the refrigerant gas that decompressor L discharges flows through successively after low temperature heat exchanger G and regenerator M heat absorption heats up and is supplied to compressor E.
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 E refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor L through regenerator M again through the finisher 6 that cooler J is communicated with vaporizer 6 to be adjusted to compressor E and to have refrigerant gas passage to have refrigerant gas passage to be communicated with the second compressor H again through the finisher 6 that cooler J is communicated with vaporizer 6, the second compressor H also has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor L through regenerator M again through the finisher 6 that cooler J is communicated with vaporizer 6; The refrigerant gas that compressor E produces flows through cooler J successively and vaporizer 6, heat release are supplied to the second compressor H after lowering the temperature, the refrigerant gas that second compressor H produces is supplied to decompressor L after flowing through cooler J, vaporizer 6 and regenerator M 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
(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 12 and ft connection, the second heat exchanger 12 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 boiler B discharges flows through generator 3, second generator 4 and the second heat exchanger 12 successively, progressively 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 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 12 and vaporizer 6 and ft connection, the second heat exchanger 12 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 gas turbine C discharges flows through generator 3, second generator 4, second heat exchanger 12 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 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 12, vaporizer 6 and low temperature heat exchanger G and ft connection, the second heat exchanger 12 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 gas turbine C discharges flows through generator 3, second generator 4, second heat exchanger 12, vaporizer 6 and low temperature heat exchanger F 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 24 is achieved in that
In the energy supplying system of combined cycle shown in Figure 22, 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 again through the second heat exchanger 12 and vaporizer 6 and ft connection; The combustion gas that boiler B discharges flows through generator 3, the 3rd generator 13, second generator 4, second heat exchanger 12 and vaporizer 6 successively, progressively externally discharges after heat release cooling, forms combined cycle energy supplying system.
The energy supplying system of combined cycle shown in Figure 25 is achieved in that
(1) in structure, in the energy supplying system of combined cycle shown in Figure 21, 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 26 is achieved in that
(1) in structure, in the energy supplying system of combined cycle shown in Figure 22, 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 27 is achieved in that
(1) in structure, in the energy supplying system of combined cycle shown in Figure 23, 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 28 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 boiler B 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 29 is achieved in that
(1) in structure, in the energy supplying system of combined cycle shown in Fig. 1, increase exhaust heat boiler and the second recycle pump, boiler B 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 boiler B have blast tube be communicated with exhaust heat boiler N after exhaust heat boiler N have blast tube and ft connection again, exhaust heat boiler N, between generator 3 and the second generator 4, rely on the second recycle pump O and circulating thermal medium pipeline formation closed loop.
(2) in flow process, the gas flow that boiler B discharges is lowered the temperature through exhaust heat boiler N heat release, circulating thermal medium flows through exhaust heat boiler N after the second recycle pump O 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 exhaust heat boiler N of the second recycle pump O pressurization again, 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 exhaust heat boiler, second recycle pump, 3rd generator, 3rd solution pump, 3rd solution heat exchanger and the 3rd adsorber, boiler B 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 boiler B have blast tube be communicated with exhaust heat boiler N after exhaust heat boiler N have blast tube and ft connection again, exhaust heat boiler N, generator 3, the second recycle pump O 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, the gas flow that boiler B discharges is lowered the temperature through exhaust heat boiler N heat release, circulating thermal medium flows through exhaust heat boiler N after the second recycle pump O 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, then provides through the backward exhaust heat boiler N of the second recycle pump O pressurization; 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 31 is achieved in that
In the energy supplying system of combined cycle shown in Fig. 1, fuel and air passageways are changed to high temperature heat source medium channel, blast tube is changed to low-temperature heat source medium channel; High temperature heat source dielectric heating condensed fluid becomes high pressure steam and provides to turbo machine A, and the low-temperature heat source MEDIA FLOW that boiler B discharges, through generator 3 and the also progressively heat release cooling of the second generator 4, forms 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) adapt to different fuel or heat source medium, 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 steam power plant 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 steam power plant circulation, compression type reverse circulation and absorb reverse circulation advantage separately, the efficiency utilization of heat energy can be realized largely.

Claims (41)

1. combined cycle energy supplying system, formed primarily of turbo machine, boiler, heat exchanger, recycle pump, compressor, cryogenic throttle valve, low temperature heat exchanger, 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; Turbo machine (A) has low pressure steam passage to be communicated with heat exchanger (C), heat exchanger (C) also has condensed fluid pipeline to be communicated with boiler (B) through recycle pump (D), boiler (B) also has high pressure steam passage to be communicated with turbo machine (A), boiler (B) has fuel and air passageways and ft connection, boiler (B) 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; The finisher (6) that compressor (E) has refrigerant steam channel to be communicated with vaporizer (6) has cryogen liquid pipeline to be communicated with low temperature heat exchanger (G) through cryogenic throttle valve (F) again, low temperature heat exchanger (G) also has refrigerant steam channel to be communicated with compressor (E), and low temperature heat exchanger (G) 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, turbo machine, boiler, heat exchanger and recycle pump form steam power plant 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, steam power plant forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, steam power plant 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 (E) refrigerant steam channel to be communicated with vaporizer (6) has cryogen liquid pipeline to be communicated with through cryogenic throttle valve (F) finisher (6) being adjusted to compressor (E) and having refrigerant steam channel to be communicated with vaporizer (6) with low temperature heat exchanger (G) again has refrigerant steam channel to be communicated with the second compressor (H) again, the finisher (6) that second compressor (H) also has refrigerant steam channel to be communicated with vaporizer (6) has cryogen liquid pipeline to be communicated with low temperature heat exchanger (G) through cryogenic throttle valve (F) again, form combined cycle energy supplying system.
3. combined cycle energy supplying system, formed primarily of turbo machine, boiler, heat exchanger, recycle pump, compressor, the second condenser, cryogenic throttle valve, low temperature heat exchanger, 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; Turbo machine (A) has low pressure steam passage to be communicated with heat exchanger (C), heat exchanger (C) also has condensed fluid pipeline to be communicated with boiler (B) through recycle pump (D), boiler (B) also has high pressure steam passage to be communicated with turbo machine (A), boiler (B) has fuel and air passageways and ft connection, boiler (B) 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; Compressor (E) have refrigerant steam channel be communicated with the second condenser (I) after the second condenser (I) have cryogen liquid pipeline to be communicated with low temperature heat exchanger (G) through cryogenic throttle valve (F) again, low temperature heat exchanger (G) also has refrigerant steam channel to be communicated with compressor (E), low temperature heat exchanger (G) also has cryogenic media pipeline and ft connection, and the second condenser (I) 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, turbo machine, boiler, heat exchanger and recycle pump form steam power plant 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, steam power plant forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, steam power plant 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 (E) is had refrigerant steam channel be communicated with the second condenser (I) after the second condenser (I) have again cryogen liquid pipeline through cryogenic throttle valve (F) to be communicated with low temperature heat exchanger (G) be adjusted to compressor (E) have refrigerant steam channel to be communicated with the second condenser (I) after the second condenser (I) have refrigerant steam channel to be communicated with the second compressor (H) again, second compressor (H) also have refrigerant steam channel be communicated with the second condenser (I) after the second condenser (I) have cryogen liquid pipeline to be communicated with low temperature heat exchanger (G) through cryogenic throttle valve (F) again, form combined cycle energy supplying system.
5. combined cycle energy supplying system, formed primarily of turbo machine, boiler, heat exchanger, recycle pump, compressor, cooler, cryogenic throttle valve, low temperature heat exchanger, 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; Turbo machine (A) has low pressure steam passage to be communicated with heat exchanger (C), heat exchanger (C) also has condensed fluid pipeline to be communicated with boiler (B) through recycle pump (D), boiler (B) also has high pressure steam passage to be communicated with turbo machine (A), boiler (B) has fuel and air passageways and ft connection, boiler (B) 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; The aftercooler (J) that compressor (E) has refrigerant steam channel to be communicated with cooler (J) 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 (G) through cryogenic throttle valve (F), low temperature heat exchanger (G) also has refrigerant steam channel to be communicated with compressor (E), low temperature heat exchanger (G) also has cryogenic media pipeline and ft connection, and cooler (J) 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, turbo machine, boiler, heat exchanger and recycle pump form steam power plant 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, steam power plant forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, steam power plant 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 (J) being had by compressor (E) refrigerant steam channel to be communicated with cooler (J) has refrigerant steam channel to be communicated with vaporizer (6) to be adjusted to compressor (E) aftercooler (J) having refrigerant steam channel to be communicated with cooler (J) to have refrigerant steam channel to be communicated with the second compressor (H) more again, the aftercooler (J) that second compressor (H) also has refrigerant steam channel to be communicated with cooler (J) 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 turbo machine, boiler, heat exchanger, recycle pump, compressor, the second compressor, the second condenser, cryogenic throttle valve, the second cryogenic throttle valve, low temperature heat exchanger, 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, turbo machine (A) has low pressure steam passage to be communicated with heat exchanger (C), heat exchanger (C) also has condensed fluid pipeline to be communicated with boiler (B) through recycle pump (D), boiler (B) also has high pressure steam passage to be communicated with turbo machine (A), boiler (B) has fuel and air passageways and ft connection, boiler (B) 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, compressor (E) 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 (G) after cryogenic throttle valve (F) is communicated with low temperature heat exchanger (G) to have refrigerant steam channel to be communicated with compressor (E) again, compressor (E) also has low pressure refrigerant steam channel to be communicated with the second compressor (H), second compressor (H) also has high pressure refrigerant steam channel to be communicated with the second condenser (I), second condenser (I) also has high pressure cryogen liquid pipeline low temperature heat exchanger (G) after vaporizer (6) and the second cryogenic throttle valve (K) are communicated with low temperature heat exchanger (G) to have refrigerant steam channel to be communicated with compressor (E) again, low temperature heat exchanger (G) also has cryogenic media pipeline and ft connection, second condenser (I) 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, turbo machine, boiler, heat exchanger and recycle pump form steam power plant forward circulation system, 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, 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, steam power plant forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, steam power plant 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 turbo machine, boiler, heat exchanger, recycle pump, compressor, the second condenser, cryogenic throttle valve, the second cryogenic throttle valve, low temperature heat exchanger, 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, turbo machine (A) has low pressure steam passage to be communicated with heat exchanger (C), heat exchanger (C) also has condensed fluid pipeline to be communicated with boiler (B) through recycle pump (D), boiler (B) also has high pressure steam passage to be communicated with turbo machine (A), boiler (B) has fuel and air passageways and ft connection, boiler (B) 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, compressor (E) 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 (G) after cryogenic throttle valve (F) is communicated with low temperature heat exchanger (G) to have refrigerant steam channel to be communicated with compressor (E) again, compressor (E) also has high pressure refrigerant steam channel to be communicated with the second condenser (I), second condenser (I) also has high pressure cryogen liquid pipeline low temperature heat exchanger (G) after vaporizer (6) and the second cryogenic throttle valve (K) are communicated with low temperature heat exchanger (G) to have refrigerant steam channel to be communicated with compressor (E) again, low temperature heat exchanger (G) also has cryogenic media pipeline and ft connection, second condenser (I) 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, turbo machine, boiler, heat exchanger and recycle pump form steam power plant 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, steam power plant forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, steam power plant 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 turbo machine, boiler, heat exchanger, recycle pump, compressor, decompressor, vaporizer, 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; Turbo machine (A) has low pressure steam passage to be communicated with heat exchanger (C), heat exchanger (C) also has condensed fluid pipeline to be communicated with boiler (B) through recycle pump (D), boiler (B) also has high pressure steam passage to be communicated with turbo machine (A), boiler (B) has fuel and air passageways and ft connection, boiler (B) 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; The finisher (6) that compressor (E) has refrigerant gas passage to be communicated with vaporizer (6) has refrigerant gas passage to be communicated with decompressor (L) again, decompressor (L) also has refrigerant gas passage to be communicated with compressor (E) through low temperature heat exchanger (G), and low temperature heat exchanger (G) 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, turbo machine, boiler, heat exchanger and recycle pump form steam power plant 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, steam power plant forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, steam power plant 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 (E) refrigerant gas passage to be communicated with vaporizer (6) has refrigerant gas passage to be communicated with decompressor (L) to be adjusted to compressor (E) finisher (6) having refrigerant gas passage to be communicated with vaporizer (6) to have refrigerant gas passage to be communicated with the second compressor (H) more again, the finisher (6) that second compressor (H) also has refrigerant gas passage to be communicated with vaporizer (6) has refrigerant gas passage to be communicated with decompressor (L) again, form combined cycle energy supplying system.
11. combined cycle energy supplying systems, formed primarily of turbo machine, boiler, heat exchanger, recycle pump, 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; Turbo machine (A) has low pressure steam passage to be communicated with heat exchanger (C), heat exchanger (C) also has condensed fluid pipeline to be communicated with boiler (B) through recycle pump (D), boiler (B) also has high pressure steam passage to be communicated with turbo machine (A), boiler (B) has fuel and air passageways and ft connection, boiler (B) 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; The finisher (6) that compressor (E) has refrigerant gas passage to be communicated with vaporizer (6) has refrigerant gas passage to be communicated with decompressor (L) through regenerator (M) again, decompressor (L) also has refrigerant gas passage to be communicated with compressor (E) with regenerator (M) through low temperature heat exchanger (G), and low temperature heat exchanger (G) 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, turbo machine, boiler, heat exchanger and recycle pump form steam power plant 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, steam power plant forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, steam power plant 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 (E) refrigerant gas passage to be communicated with vaporizer (6) has refrigerant gas passage to be communicated with through regenerator (M) finisher (6) being adjusted to compressor (E) and having refrigerant gas passage to be communicated with logical vaporizer (6) with decompressor (L) again has refrigerant gas passage to be communicated with the second compressor (H) again, the finisher (6) that second compressor (H) also has refrigerant gas passage to be communicated with vaporizer (6) has refrigerant gas passage to be communicated with decompressor (L) through regenerator (M) again, form combined cycle energy supplying system.
13. combined cycle energy supplying systems, formed primarily of turbo machine, boiler, heat exchanger, recycle pump, 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; Turbo machine (A) has low pressure steam passage to be communicated with heat exchanger (C), heat exchanger (C) also has condensed fluid pipeline to be communicated with boiler (B) through recycle pump (D), boiler (B) also has high pressure steam passage to be communicated with turbo machine (A), boiler (B) has fuel and air passageways and ft connection, boiler (B) 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; Compressor (E) has refrigerant gas passage to be communicated with decompressor (L) through cooler (J), decompressor (L) also has refrigerant gas passage to be communicated with compressor (E) through low temperature heat exchanger (G), low temperature heat exchanger (G) also has cryogenic media pipeline and ft connection, and cooler (J) 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, turbo machine, boiler, heat exchanger and recycle pump form steam power plant 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 the absorption reverse circulation system of row, steam power plant forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, steam power plant 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 (E) refrigerant gas passage to be communicated with decompressor (L) through cooler (J) to be adjusted to compressor (E) and to have refrigerant gas passage to be communicated with the second compressor (H) through cooler (J), second compressor (H) also has refrigerant gas passage to be communicated with decompressor (L) through cooler (J), forms combined cycle energy supplying system.
15. combined cycle energy supplying systems, formed primarily of turbo machine, boiler, heat exchanger, recycle pump, 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; Turbo machine (A) has low pressure steam passage to be communicated with heat exchanger (C), heat exchanger (C) also has condensed fluid pipeline to be communicated with boiler (B) through recycle pump (D), boiler (B) also has high pressure steam passage to be communicated with turbo machine (A), boiler (B) has fuel and air passageways and ft connection, boiler (B) 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; Compressor (E) has refrigerant gas passage to be communicated with decompressor (L) with regenerator (M) through cooler (J), decompressor (L) also has refrigerant gas passage to be communicated with compressor (E) with regenerator (M) through low temperature heat exchanger (G), low temperature heat exchanger (G) also has cryogenic media pipeline and ft connection, and cooler (J) 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, turbo machine, boiler, heat exchanger and recycle pump form steam power plant 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, steam power plant forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, steam power plant 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 (E) refrigerant gas passage to be communicated with decompressor (L) through cooler (J) and regenerator (M) to be adjusted to compressor (E) and to have refrigerant gas passage to be communicated with the second compressor (H) through cooler (J), second compressor (H) has refrigerant gas passage to be communicated with decompressor (L) with regenerator (M) through cooler (J) again, forms combined cycle energy supplying system.
17. combined cycle energy supplying systems, formed primarily of turbo machine, boiler, heat exchanger, recycle pump, 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; Turbo machine (A) has low pressure steam passage to be communicated with heat exchanger (C), heat exchanger (C) also has condensed fluid pipeline to be communicated with boiler (B) through recycle pump (D), boiler (B) also has high pressure steam passage to be communicated with turbo machine (A), boiler (B) has fuel and air passageways and ft connection, boiler (B) 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; Compressor (E) has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor (L) again through the finisher (6) that cooler (J) is communicated with vaporizer (6), decompressor (L) also has refrigerant gas passage to be communicated with compressor (E) through low temperature heat exchanger (G), low temperature heat exchanger (G) also has cryogenic media pipeline and ft connection, and cooler (J) 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, turbo machine, boiler, heat exchanger and recycle pump form steam power plant 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, steam power plant forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, steam power plant 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 (E) to have refrigerant gas passage to be communicated with decompressor (L) to be again adjusted to compressor (E) through the finisher (6) that cooler (J) is communicated with vaporizer (6) and have refrigerant gas passage to have refrigerant gas passage to be communicated with the second compressor (H) again through the finisher (6) that cooler (J) is communicated with vaporizer (6), second compressor (H) also has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor (L) again through the finisher (6) that cooler (J) is communicated with vaporizer (6), form combined cycle energy supplying system.
19. combined cycle energy supplying systems, formed primarily of turbo machine, boiler, heat exchanger, recycle pump, 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; Turbo machine (A) has low pressure steam passage to be communicated with heat exchanger (C), heat exchanger (C) also has condensed fluid pipeline to be communicated with boiler (B) through recycle pump (D), boiler (B) also has high pressure steam passage to be communicated with turbo machine (A), boiler (B) has fuel and air passageways and ft connection, boiler (B) 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; Compressor (E) has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor (L) through regenerator (M) again through the finisher (6) that cooler (J) is communicated with vaporizer (6), decompressor (L) also has refrigerant gas passage to be communicated with compressor (E) with regenerator (M) through low temperature heat exchanger (G), low temperature heat exchanger (G) also has cryogenic media pipeline and ft connection, and cooler (J) 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, turbo machine, boiler, heat exchanger and recycle pump form steam power plant 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, steam power plant forward circulation provides power to compression type reverse circulation or externally provides power simultaneously, steam power plant 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 (E) refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor (L) through regenerator (M) again through the finisher (6) that cooler (J) is communicated with vaporizer (6) to be adjusted to compressor (E) and to have refrigerant gas passage to have refrigerant gas passage to be communicated with the second compressor (H) again through the finisher (6) that cooler (J) is communicated with vaporizer (6), second compressor (H) also has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor (L) through regenerator (M) again through the finisher (6) that cooler (J) 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 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.
22. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-20, 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.
23. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-20, 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.
24. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-20, 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.
25. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-20, 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.
26. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-20, 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.
27. combined cycle energy supplying systems, in arbitrary combined cycle energy supplying system according to claim 21, 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.
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 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.
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, 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.
30. combined cycle energy supplying systems, in arbitrary combined cycle energy supplying system according to claim 21, 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.
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 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.
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, 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.
33. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 27-32, 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.
34. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-33, 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.
35. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-20, 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.
36. combined cycle energy supplying systems, in arbitrary combined cycle energy supplying system according to claim 35, 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.
37. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-20, increase exhaust heat boiler and the second recycle pump, boiler (B) 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 boiler (B) have blast tube be communicated with exhaust heat boiler (N) after exhaust heat boiler (N) have blast tube and ft connection again, exhaust heat boiler (N), the second recycle pump (O) 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.
38. combined cycle energy supplying systems, in arbitrary combined cycle energy supplying system according to claim 37, increase by the second heat exchanger, second heat exchanger (12) has heated medium pipeline and ft connection, and take following wherein arbitrary technical measures to form combined cycle energy supplying system: 1. by exhaust heat boiler (N), rely on the second recycle pump (O) and circulating thermal medium pipeline to form closed loop between generator (3) and the second generator (4) and be adjusted to exhaust heat boiler (N), generator (3), the second recycle pump (O) and circulating thermal medium pipeline is relied on to form closed loop between second generator (4) and the second heat exchanger (12), 2. by exhaust heat boiler (N), rely on the second recycle pump (O) and circulating thermal medium pipeline to form closed loop between generator (3) and the second generator (4) to be adjusted to exhaust heat boiler (N), generator (3), the second generator (4), between the second heat exchanger (12) and vaporizer (6), to rely on the second recycle pump (O) and circulating thermal medium pipeline formation closed loop, 3. by exhaust heat boiler (N), rely on the second recycle pump (O) and circulating thermal medium pipeline to form closed loop between generator (3) and the second generator (4) to be adjusted to exhaust heat boiler (N), generator (3), the second generator (4), the second heat exchanger (12), between vaporizer (6) and low temperature heat exchanger (F), to rely on the second recycle pump (O) and circulating thermal medium pipeline formation closed loop.
39. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-20, increase exhaust heat boiler, second recycle pump, 3rd generator, 3rd solution pump, 3rd solution heat exchanger and the 3rd adsorber, boiler (B) 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 boiler (B) have blast tube be communicated with exhaust heat boiler (N) after exhaust heat boiler (N) have blast tube and ft connection again, exhaust heat boiler (N), generator (3), the second recycle pump (O) 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.
40. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-39, increase working machine, steam power plant forward circulation provides power respectively to working machine (P), provides power and provide driving heat load to absorption reverse circulation to compression type reverse circulation, forms combined cycle energy supplying system.
41. combined cycle energy supplying systems, are in the arbitrary combined cycle energy supplying system described in claim 1-40, fuel and air passageways are changed to high temperature heat source medium channel, blast tube is changed to low-temperature heat source medium channel, form combined cycle energy supplying system.
CN201510330916.8A 2014-06-09 2015-06-08 Combined cycle energy supplying system Active CN105041396B (en)

Priority Applications (1)

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

Applications Claiming Priority (3)

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

Publications (2)

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

Family

ID=54448315

Family Applications (1)

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

Country Status (1)

Country Link
CN (1) CN105041396B (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106352595A (en) * 2015-12-30 2017-01-25 李华玉 First-type thermally driven compression-absorption heat pump
CN106440471A (en) * 2016-05-30 2017-02-22 李华玉 Combined heating and power system
WO2022161112A1 (en) * 2021-01-27 2022-08-04 李华玉 Dual-fuel combined cycle steam power device
WO2022166504A1 (en) * 2021-02-07 2022-08-11 李华玉 Dual-fuel combined cycle steam power plant

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1804511A (en) * 2006-01-23 2006-07-19 李华玉 Compression-absorption combined heat pump heating system
CN201181133Y (en) * 2008-03-03 2009-01-14 清华大学 Combined cooling, heating and power supplying system
CN102419026A (en) * 2011-07-27 2012-04-18 李华玉 Absorption-type heat source temperature changer
CN102635970A (en) * 2012-04-09 2012-08-15 李华玉 Grading condensation third-type absorption heat pump

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1804511A (en) * 2006-01-23 2006-07-19 李华玉 Compression-absorption combined heat pump heating system
CN201181133Y (en) * 2008-03-03 2009-01-14 清华大学 Combined cooling, heating and power supplying system
CN102419026A (en) * 2011-07-27 2012-04-18 李华玉 Absorption-type heat source temperature changer
CN102635970A (en) * 2012-04-09 2012-08-15 李华玉 Grading condensation third-type absorption heat pump

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106352595A (en) * 2015-12-30 2017-01-25 李华玉 First-type thermally driven compression-absorption heat pump
CN106440471A (en) * 2016-05-30 2017-02-22 李华玉 Combined heating and power system
WO2022161112A1 (en) * 2021-01-27 2022-08-04 李华玉 Dual-fuel combined cycle steam power device
WO2022166504A1 (en) * 2021-02-07 2022-08-11 李华玉 Dual-fuel combined cycle steam power plant

Also Published As

Publication number Publication date
CN105041396B (en) 2019-02-15

Similar Documents

Publication Publication Date Title
CN104929706A (en) Combined circulating energy supply system
CN105041471A (en) Combined circulation energy supplying system
CN108679880B (en) Double-working medium combined cycle compression heat pump
CN104948245A (en) Combined-cycle energy supply system
CN106440510B (en) Second-class thermally-driven compression heat pump
CN104963732A (en) Combined circulating energy supplying system
CN104929704A (en) Combined circulating energy supply system
CN102650478B (en) Trans-critical-compression/absorption composite refrigeration device utilizing low-grade heat
CN103851823B (en) Compound generation first-class absorption type heat pump
CN105041472A (en) Combined cycle energy supply system
CN105041396A (en) Combined cycle energy supply system
TW201300639A (en) Power system with low temperature heat source
CN210089175U (en) Jet type transcritical carbon dioxide two-stage compression refrigeration system
CN106403371B (en) First-class thermally-driven compression heat pump
CN106468490B (en) Third-class thermally-driven compression heat pump
CN105019954B (en) Combined cycle energy supplying system
CN104963733A (en) Combined cycle energy supply system
CN104989472A (en) Combined cycle energy supply system
CN105953467A (en) Fourth kind thermal-driving compression-absorption type heat pump
CN103148631B (en) Compound generation first-class absorption type heat pump
CN105953465B (en) Fourth type thermal driving compression-absorption heat pump
CN104990302B (en) Injection compression refrigerating system with gas-liquid separator and utilization low grade heat energy
CN106225309A (en) First kind thermal drivers compression absorption heat pump
CN106440491B (en) First-class thermally driven compression-absorption heat pump
CN106403370B (en) First-class thermally-driven compression heat pump

Legal Events

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