CN105019954A - Combined-cycle energy supply system - Google Patents

Combined-cycle energy supply system Download PDF

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CN105019954A
CN105019954A CN201510297513.8A CN201510297513A CN105019954A CN 105019954 A CN105019954 A CN 105019954A CN 201510297513 A CN201510297513 A CN 201510297513A CN 105019954 A CN105019954 A CN 105019954A
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generator
heat exchanger
condenser
adsorber
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CN105019954B (en
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李华玉
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Abstract

The invention provides a combined-cycle energy supply system, and belongs to the technical field of heat energy utilization, refrigerating and heat pumps. The combined-cycle energy supply system is mainly composed of a turbine motor, a compressor, a low-temperature throttling valve, a low-temperature heat exchanger, an absorber, a generator, a condenser, an evaporator, a throttling valve, a solution pump and a solution heat exchanger. The compressor, the evaporator, the low-temperature throttling valve and the low-temperature heat exchanger form a compression type inverse circulatory system. The absorber, the generator, the condenser, the evaporator, the throttling valve, the solution pump and the solution heat exchanger form an absorption type reverse circulatory system. The turbine motor supplies power to the compression type reverse circulation and provides drive heat load for absorption type reverse circulation. The compression type reverse circulation obtains low-temperature heat load and supplies heat to absorption type reverse circulation through the evaporator. The absorption type reverse circulation supplies heat to the outside through the absorber and the condenser. In this way, the combined-cycle energy supply system is formed.

Description

Combined cycle energy supplying system
Technical field:
The invention belongs to heat energy utilization, refrigeration and technical field of heat pumps.
Background technique:
In cold and heat supply field, utilizing for realizing the high effect of heat energy, between the factors such as the kind of thermal source, residual heat resources or cooled medium, heated medium, apparatus design and working medium, often there is restriction and contradiction.Such as Winter heat supply, if thermal source is the steam of elevated pressures, and heat supply needs temperature lower than the hot water of 100 DEG C, and does not have other Low Temperature Thermal resource, now adopts the steam of high parameter directly to water heating, cannot realize the efficiency utilization of heat energy; When considering to adopt absorption heat pump technology, also solution selection, Security, many-sided restriction such as the rationality of the temperature difference, Low Temperature Thermal source resource and grade between driving heat load and solution will be faced.For this reason, make the situation of thermal source for high pressure steam, the application proposes the combined cycle energy supplying system that turbo machine, compression type reverse circulation and absorption reverse circulation combine, and to realize efficient cooling and heat supply, ensures the high efficiency of heat energy utilization.
Summary of the invention:
Main purpose of the present invention to provide combined cycle energy supplying system, and concrete summary of the invention subitem is described below:
1. combined cycle energy supplying system, formed primarily of turbo machine, compressor, cryogenic throttle valve, low temperature heat exchanger, adsorber, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger; Outside has high pressure steam passage to be communicated with turbo machine, turbo machine also have low pressure steam passage be communicated with generator after generator have condensate line 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 generator with solution heat exchanger through solution pump, 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, condenser also has cryogen liquid pipeline to be communicated with vaporizer through throttle valve, and adsorber and condenser also have heated medium pipeline and ft connection respectively; Compressor, vaporizer, cryogenic throttle valve and low temperature heat exchanger form compression type reverse circulation system, and adsorber, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger form absorption reverse circulation system; Turbo machine provides power to compression type reverse circulation or externally provides power simultaneously, turbo machine 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 and the external heat supply of condenser, forms combined cycle energy supplying system.
2. combined cycle energy supplying system, in the combined cycle energy supplying system described in the 1st, increase by the second compressor, the finisher being had by compressor refrigerant steam channel to be communicated with vaporizer has cryogen liquid pipeline to be communicated with through cryogenic throttle valve the finisher being adjusted to compressor and having refrigerant steam channel to be communicated with vaporizer with low temperature heat exchanger again has refrigerant steam channel to be communicated with the second compressor again, the finisher that second compressor also has refrigerant steam channel to be communicated with vaporizer has cryogen liquid pipeline to be communicated with low temperature heat exchanger through cryogenic throttle valve again, form combined cycle energy supplying system.
3. combined cycle energy supplying system, formed primarily of turbo machine, compressor, the second condenser, cryogenic throttle valve, low temperature heat exchanger, adsorber, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger; Outside has high pressure steam passage to be communicated with turbo machine, turbo machine also have low pressure steam passage be communicated with generator after generator have condensate line 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 generator with solution heat exchanger through solution pump, 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, condenser also has cryogen liquid pipeline to be communicated with vaporizer through throttle valve, vaporizer also has cryogenic media pipeline and ft connection, and adsorber and condenser also have heated medium pipeline and ft connection respectively; Compressor, the second condenser, cryogenic throttle valve and low temperature heat exchanger form compression type reverse circulation system, and adsorber, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger form absorption reverse circulation system; Turbo machine provides power to compression type reverse circulation or externally provides power simultaneously, turbo machine 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 and the external heat supply of condenser, forms combined cycle energy supplying system.
4. combined cycle energy supplying system, in the combined cycle energy supplying system described in the 3rd, increase by the second compressor, compressor is had refrigerant steam channel be communicated with the second condenser after the second condenser have again cryogen liquid pipeline through cryogenic throttle valve to be communicated with low temperature heat exchanger be adjusted to compressor have refrigerant steam channel to be communicated with the second condenser after the second condenser have refrigerant steam channel to be communicated with the second compressor again, second compressor also have refrigerant steam channel be communicated with the second condenser after the second condenser have cryogen liquid pipeline to be communicated with low temperature heat exchanger through cryogenic throttle valve again, form combined cycle energy supplying system.
5. combined cycle energy supplying system, formed primarily of turbo machine, compressor, cooler, cryogenic throttle valve, low temperature heat exchanger, adsorber, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger; Outside has high pressure steam passage to be communicated with turbo machine, turbo machine also have low pressure steam passage be communicated with generator after generator have condensate line 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 generator with solution heat exchanger through solution pump, 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, condenser also has cryogen liquid pipeline to be communicated with vaporizer through throttle valve, and adsorber and condenser also have heated medium pipeline and ft connection respectively; Compressor, cooler, vaporizer, cryogenic throttle valve and low temperature heat exchanger form compression type reverse circulation system, and adsorber, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger form the absorption reverse circulation system of row; Turbo machine provides power to compression type reverse circulation or externally provides power simultaneously, turbo machine 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 and the external heat supply of condenser, forms combined cycle energy supplying system.
6. combined cycle energy supplying system, in the combined cycle energy supplying system described in the 5th, increase by the second compressor, the aftercooler being had by compressor refrigerant steam channel to be communicated with cooler has refrigerant steam channel to be communicated with vaporizer to be adjusted to compressor the aftercooler having refrigerant steam channel to be communicated with cooler to have refrigerant steam channel to be communicated with the second compressor more again, the aftercooler that second compressor also has refrigerant steam channel to be communicated with cooler has refrigerant steam channel to be communicated with vaporizer again, forms combined cycle energy supplying system.
7. combined cycle energy supplying system, formed primarily of turbo machine, compressor, the second compressor, the second condenser, cryogenic throttle valve, the second cryogenic throttle valve, low temperature heat exchanger, adsorber, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger, outside has high pressure steam passage to be communicated with turbo machine, turbo machine also have low pressure steam passage be communicated with generator after generator have condensate line 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 generator with solution heat exchanger through solution pump, 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, condenser also has cryogen liquid pipeline to be communicated with vaporizer through throttle valve, and adsorber and condenser also have heated medium pipeline and ft connection respectively, 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, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger form absorption reverse circulation system, turbo machine provides power to compression type reverse circulation or externally provides power simultaneously, turbo machine 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 and the external heat supply of condenser, forms combined cycle energy supplying system.
8. combined cycle energy supplying system, formed primarily of turbo machine, compressor, the second condenser, cryogenic throttle valve, the second cryogenic throttle valve, low temperature heat exchanger, adsorber, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger, outside has high pressure steam passage to be communicated with turbo machine, turbo machine also have low pressure steam passage be communicated with generator after generator have condensate line 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 generator with solution heat exchanger through solution pump, 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, condenser also has cryogen liquid pipeline to be communicated with vaporizer through throttle valve, and adsorber and condenser also have heated medium pipeline and ft connection respectively, 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, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger form absorption reverse circulation system, turbo machine provides power to compression type reverse circulation or externally provides power simultaneously, turbo machine 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 and the external heat supply of condenser, forms combined cycle energy supplying system.
9. combined cycle energy supplying system, formed primarily of turbo machine, compressor, decompressor, vaporizer, low temperature heat exchanger, adsorber, generator, condenser, throttle valve, solution pump and solution heat exchanger; Outside has high pressure steam passage to be communicated with turbo machine, turbo machine also have low pressure steam passage be communicated with generator after generator have condensate line 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 generator with solution heat exchanger through solution pump, 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, condenser also has cryogen liquid pipeline to be communicated with vaporizer through throttle valve, and adsorber and condenser also have heated medium pipeline and ft connection respectively; Compressor, vaporizer, decompressor and low temperature heat exchanger form compression type reverse circulation system, and vaporizer, adsorber, generator, condenser, throttle valve, solution pump and solution heat exchanger form absorption reverse circulation system; Turbo machine provides power to compression type reverse circulation or externally provides power simultaneously, turbo machine 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 and the external heat supply of condenser, forms combined cycle energy supplying system.
10. combined cycle energy supplying system, in the combined cycle energy supplying system described in the 9th, increase by the second compressor, the finisher being had by compressor refrigerant gas passage to be communicated with vaporizer has refrigerant gas passage to be communicated with decompressor to be adjusted to compressor the finisher having refrigerant gas passage to be communicated with vaporizer to have refrigerant gas passage to be communicated with the second compressor more again, the finisher that second compressor also has refrigerant gas passage to be communicated with vaporizer has refrigerant gas passage to be communicated with decompressor again, forms combined cycle energy supplying system.
11. combined cycle energy supplying systems, formed primarily of turbo machine, compressor, vaporizer, decompressor, low temperature heat exchanger, regenerator, adsorber, generator, condenser, throttle valve, solution pump and solution heat exchanger; Outside has high pressure steam passage to be communicated with turbo machine, turbo machine also have low pressure steam passage be communicated with generator after generator have condensate line 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 generator with solution heat exchanger through solution pump, 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, condenser also has cryogen liquid pipeline to be communicated with vaporizer through throttle valve, and adsorber and condenser also have heated medium pipeline and ft connection respectively; Compressor, vaporizer, decompressor, low temperature heat exchanger and regenerator form compression type reverse circulation system, and vaporizer, adsorber, generator, condenser, throttle valve, solution pump and solution heat exchanger form absorption reverse circulation system; Turbo machine provides power to compression type reverse circulation or externally provides power simultaneously, turbo machine 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 and the external heat supply of condenser, forms combined cycle energy supplying system.
12. combined cycle energy supplying systems, in the combined cycle energy supplying system described in the 11st, increase by the second compressor, the finisher being had by compressor refrigerant gas passage to be communicated with vaporizer has refrigerant gas passage to be communicated with through regenerator the finisher being adjusted to compressor and having refrigerant gas passage to be communicated with logical vaporizer with decompressor again has refrigerant gas passage to be communicated with the second compressor again, the finisher that second compressor also has refrigerant gas passage to be communicated with vaporizer has refrigerant gas passage to be communicated with decompressor through regenerator again, forms combined cycle energy supplying system.
13. combined cycle energy supplying systems, formed primarily of turbo machine, compressor, decompressor, cooler, low temperature heat exchanger, vaporizer, adsorber, generator, condenser, throttle valve, solution pump and solution heat exchanger; Outside has high pressure steam passage to be communicated with turbo machine, turbo machine also have low pressure steam passage be communicated with generator after generator have condensate line 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 generator with solution heat exchanger through solution pump, 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, condenser also has cryogen liquid pipeline to be communicated with vaporizer through throttle valve, vaporizer also has cryogenic media pipeline and ft connection, and adsorber and condenser also have heated medium pipeline and ft connection respectively; Compressor, cooler, decompressor and low temperature heat exchanger form compression type reverse circulation system, and adsorber, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger form absorption reverse circulation system; Turbo machine provides power to compression type reverse circulation or externally provides power simultaneously, turbo machine 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 and the external heat supply of condenser, forms combined cycle energy supplying system.
14. combined cycle energy supplying systems, in the combined cycle energy supplying system described in the 13rd, increase by the second compressor, had by compressor refrigerant gas passage to be communicated with decompressor through cooler to be adjusted to compressor and to have refrigerant gas passage to be communicated with the second compressor through cooler, second compressor also has refrigerant gas passage to be communicated with decompressor through cooler, forms combined cycle energy supplying system.
15. combined cycle energy supplying systems, formed primarily of turbo machine, compressor, cooler, decompressor, low temperature heat exchanger, regenerator, vaporizer, adsorber, generator, condenser, throttle valve, solution pump and solution heat exchanger; Outside has high pressure steam passage to be communicated with turbo machine, turbo machine also have low pressure steam passage be communicated with generator after generator have condensate line 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 generator with solution heat exchanger through solution pump, 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, condenser also has cryogen liquid pipeline to be communicated with vaporizer through throttle valve, vaporizer also has cryogenic media pipeline and ft connection, and adsorber and condenser also have heated medium pipeline and ft connection respectively; Compressor, cooler, decompressor, low temperature heat exchanger and regenerator form compression type reverse circulation system, and vaporizer, adsorber, generator, condenser, throttle valve, solution pump and solution heat exchanger form absorption reverse circulation system; Turbo machine provides power to compression type reverse circulation or externally provides power simultaneously, turbo machine 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 and the external heat supply of condenser, forms combined cycle energy supplying system.
16. combined cycle energy supplying systems, in the combined cycle energy supplying system described in the 15th, increase by the second compressor, had by compressor refrigerant gas passage to be communicated with decompressor through cooler and regenerator to be adjusted to compressor and to have refrigerant gas passage to be communicated with the second compressor through cooler, second compressor has refrigerant gas passage to be communicated with decompressor with regenerator through cooler again, forms combined cycle energy supplying system.
17. combined cycle energy supplying systems, formed primarily of turbo machine, compressor, cooler, vaporizer, decompressor, low temperature heat exchanger, adsorber, generator, condenser, throttle valve, solution pump and solution heat exchanger; Outside has high pressure steam passage to be communicated with turbo machine, turbo machine also have low pressure steam passage be communicated with generator after generator have condensate line 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 generator with solution heat exchanger through solution pump, 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, condenser also has cryogen liquid pipeline to be communicated with vaporizer through throttle valve, and adsorber and condenser also have heated medium pipeline and ft connection respectively; Compressor, cooler, vaporizer, decompressor and low temperature heat exchanger form compression type reverse circulation system, and vaporizer, adsorber, generator, condenser, throttle valve, solution pump and solution heat exchanger form absorption reverse circulation system; Turbo machine provides power to compression type reverse circulation or externally provides power simultaneously, turbo machine 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 and the external heat supply of condenser, forms combined cycle energy supplying system.
18. combined cycle energy supplying systems, in the combined cycle energy supplying system described in the 17th, increase by the second compressor, refrigerant gas passage is had by compressor to have refrigerant gas passage to be communicated with decompressor to be again adjusted to compressor through the finisher that cooler is communicated with vaporizer and have refrigerant gas passage to have refrigerant gas passage to be communicated with the second compressor again through the finisher that cooler is communicated with vaporizer, second compressor also has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor again through the finisher that cooler is communicated with vaporizer, form combined cycle energy supplying system.
19. combined cycle energy supplying systems, formed primarily of turbo machine, compressor, cooler, vaporizer, regenerator, decompressor, low temperature heat exchanger, adsorber, generator, condenser, throttle valve, solution pump and solution heat exchanger; Outside has high pressure steam passage to be communicated with turbo machine, turbo machine also have low pressure steam passage be communicated with generator after generator have condensate line 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 generator with solution heat exchanger through solution pump, 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, condenser also has cryogen liquid pipeline to be communicated with vaporizer through throttle valve, and adsorber and condenser also have heated medium pipeline and ft connection respectively; Compressor, cooler, vaporizer, regenerator, decompressor and low temperature heat exchanger form compression type reverse circulation system, and vaporizer, adsorber, generator, condenser, throttle valve, solution pump and solution heat exchanger form absorption reverse circulation system; Turbo machine provides power to compression type reverse circulation or externally provides power simultaneously, turbo machine 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 and the external heat supply of condenser, forms combined cycle energy supplying system.
20. combined cycle energy supplying systems, in the combined cycle energy supplying system described in the 19th, increase by the second compressor, had by compressor refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor through regenerator again through the finisher that cooler is communicated with vaporizer to be adjusted to compressor and to have refrigerant gas passage to have refrigerant gas passage to be communicated with the second compressor again through the finisher that cooler is communicated with vaporizer, second compressor also has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor through regenerator again through the finisher that cooler is communicated with vaporizer, form combined cycle energy supplying system.
21. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in 1-20 item, increase by the second generator, second throttle, second solution pump and the second solution heat exchanger, adsorber is set up dilute solution pipeline and is communicated with the second generator with the second solution heat exchanger through the second solution pump, second generator also has concentrated solution pipeline to be communicated with adsorber through the second 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 second generator after the second generator have cryogen liquid pipeline to be communicated with condenser through second throttle again, second 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 1-20 item, increase by the second generator, second throttle and the second solution heat exchanger, had by adsorber dilute solution pipeline to be communicated with generator through solution pump and solution heat exchanger to be adjusted to adsorber and to have dilute solution pipeline through solution pump, solution heat exchanger is communicated with generator with the second solution heat exchanger, had by generator concentrated solution pipeline to be communicated with adsorber through solution heat exchanger to be adjusted to generator and to have concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger, second generator has concentrated solution pipeline to be communicated with adsorber through 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 second generator after the second generator have cryogen liquid pipeline to be communicated with condenser through second throttle again, second generator also has refrigerant steam channel to be communicated with condenser, form combined cycle energy supplying system.
23. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in 1-20 item, increase by the second generator, second throttle, second solution pump and the second solution heat exchanger, had by adsorber dilute solution pipeline to be communicated with generator through solution pump and solution heat exchanger to be adjusted to adsorber and to have dilute solution pipeline to be communicated with the second generator with solution heat exchanger through solution pump, second generator has concentrated solution pipeline to be communicated with generator with the second solution heat exchanger through the second solution pump again, had by generator concentrated solution pipeline to be communicated with adsorber through solution heat exchanger to be adjusted to generator and to have concentrated solution pipeline to be communicated with adsorber with solution heat exchanger through the second 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 second generator after the second generator have cryogen liquid pipeline to be communicated with condenser through second throttle again, second 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 the 21st, increase by the 3rd generator, 3rd throttle valve, 3rd solution pump and the 3rd solution heat exchanger, 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 adsorber through the 3rd solution heat exchanger, had by second generator refrigerant steam channel to be communicated with condenser to be adjusted to the second 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 the 3rd throttle valve 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 the 22nd, increase by the 3rd generator, 3rd throttle valve and the 3rd solution heat exchanger, adsorber there is dilute solution pipeline through solution pump, solution heat exchanger and the second solution heat exchanger are communicated with generator and are adjusted to adsorber and have dilute solution pipeline through solution pump, solution heat exchanger, 3rd solution heat exchanger is communicated with generator with the second solution heat exchanger, had by second generator concentrated solution pipeline to be communicated with adsorber through solution heat exchanger to be adjusted to the second 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 adsorber through solution heat exchanger again, had by second generator refrigerant steam channel to be communicated with condenser to be adjusted to the second 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 the 3rd throttle valve 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 the 23rd, increase by the 3rd generator, 3rd throttle valve, 3rd solution pump and the 3rd solution heat exchanger, had by adsorber dilute solution pipeline to be communicated with the second generator through solution pump and solution heat exchanger to be adjusted to adsorber and to have dilute solution pipeline to be communicated with the 3rd generator with solution heat exchanger through solution pump, 3rd generator has concentrated solution pipeline to be communicated with the second generator with the 3rd solution heat exchanger through the 3rd solution pump again, had by generator concentrated solution pipeline to be communicated with adsorber through the second solution heat exchanger and solution heat exchanger to be adjusted to generator and to have concentrated solution pipeline through the second solution heat exchanger, 3rd solution heat exchanger is communicated with adsorber with solution heat exchanger, had by second generator refrigerant steam channel to be communicated with condenser to be adjusted to the second 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 the 3rd throttle valve again, 3rd generator also has refrigerant steam channel to be communicated with condenser, form combined cycle energy supplying system.
27. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in 24-26 item, generator is had refrigerant steam channel be communicated with the second generator after the second generator have again cryogen liquid pipeline through second throttle to be communicated with condenser be adjusted to generator have refrigerant steam channel to be communicated with the second generator after the second generator have cryogen liquid pipeline to be communicated with condenser with second throttle through the 3rd generator again, form combined cycle energy supplying system.
28. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in 1-20 item, increase by the second generator, second solution pump, second solution heat exchanger and the second adsorber, turbo machine is had low pressure steam passage be communicated with generator after generator have again condensate line and ft connection be adjusted to turbo machine have low pressure steam passage be communicated with generator and the second generator successively after the second generator have condensate line 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 second adsorber, second adsorber also has dilute solution pipeline to be communicated with the second generator with the second solution heat exchanger through the second solution pump, second generator also has concentrated solution pipeline to be communicated with the second adsorber through the second solution heat exchanger, second generator also has refrigerant steam channel to be communicated with adsorber, second adsorber also has heated medium pipeline and ft connection, form combined cycle energy supplying system.
29. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in 1-27 item, increase heat exchanger, the rear heat exchange that being had by generator condensate line and ft connection to be adjusted to generator has condensate line to be communicated with heat exchanger has condensate line and ft connection again, heat exchanger also has heated medium pipeline and ft connection, forms combined cycle energy supplying system.
30. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in the 28th, increase heat exchanger, the rear heat exchange that being had by second generator condensate line and ft connection to be adjusted to the second generator has condensate line to be communicated with heat exchanger has condensate line and ft connection again, heat exchanger also has heated medium pipeline and ft connection, forms combined cycle energy supplying system.
31. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in 1-30 item, low pressure steam passage is had by turbo machine to be communicated with generator to be adjusted to the turbo machine passage that draws gas to be communicated with generator, turbo machine sets up exhaust steam passage and ft connection, forms combined cycle energy supplying system.
32. combined cycle energy supplying systems are in the arbitrary combined cycle energy supplying system described in 1-31 item, increase working machine, and turbo machine provides power to working machine and compressor simultaneously, 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.
In figure, A-turbo machine, B-compressor, C-cryogenic throttle valve, D-low temperature heat exchanger, E-second compressor, F-second condenser, G-cooler, H-second cryogenic throttle valve, I-decompressor, J-regenerator, K-working machine; 1-adsorber, 2-generator, 3-condenser, 4-vaporizer, 5-throttle valve, 6-solution pump, 7-solution heat exchanger, 8-heat exchanger, 9-second generator, 10-second throttle, 11-second solution pump, 12-second solution heat exchanger, 13-the 3rd generator, 14-the 3rd throttle valve, 15-the 3rd solution pump, 16-the 3rd solution heat exchanger, 17-second 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) cryogenic throttle valve C---by the throttle valve called after cryogenic 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.
(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.
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.
Combined cycle energy supplying system shown in Fig. 1 is achieved in that
(1), in structure, it formed primarily of turbo machine, compressor, cryogenic throttle valve, low temperature heat exchanger, adsorber, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger; Outside has high pressure steam passage to be communicated with turbo machine A, turbo machine A also have low pressure steam passage be communicated with generator 2 after generator 2 have condensate line and ft connection again; The finisher 4 that compressor B has refrigerant steam channel to be communicated with vaporizer 4 has cryogen liquid pipeline to be communicated with low temperature heat exchanger D through cryogenic throttle valve C again, low temperature heat exchanger D also has refrigerant steam channel to be communicated with compressor B, and low temperature heat exchanger D also has cryogenic media pipeline and ft connection; Vaporizer 4 also has refrigerant steam channel to be communicated with adsorber 1, adsorber 1 also has dilute solution pipeline to be communicated with generator 2 with solution heat exchanger 7 through solution pump 6, generator 2 also has concentrated solution pipeline to be communicated with adsorber 1 through solution heat exchanger 7, generator 2 also has refrigerant steam channel to be communicated with condenser 3, condenser 3 also has cryogen liquid pipeline to be communicated with vaporizer 4 through throttle valve 5, and adsorber 1 and condenser 3 also have heated medium pipeline and ft connection respectively; Compressor, vaporizer, cryogenic throttle valve and low temperature heat exchanger form compression type reverse circulation system, and adsorber, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger form absorption reverse circulation system.
(2), in flow process, high pressure steam enters turbo machine A step-down work done and provides to compressor B, and the low pressure steam after work done is externally discharged after flowing through generator 2, exothermic condensation, compressor, vaporizer, cryogenic throttle valve and low temperature heat exchanger carry out compression type reverse circulation---and refrigerant vapour enters compressor B boosting and heats up, flow through vaporizer 4 heat release and become cryogen liquid, cryogen liquid enters low temperature heat exchanger D through cryogenic throttle valve C throttling, absorbs heat into refrigerant vapour and provide to compressor B, adsorber, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger carry out absorption reverse circulation---and the dilute solution of adsorber 1 enters generator 2 through solution pump 6 and solution heat exchanger 7, heat absorption release refrigerant vapour also provides to condenser 3, the concentrated solution of generator 2 enters adsorber 1 through solution heat exchanger 7, absorb refrigerant vapour heat release in heated medium, the refrigerant vapour heat release of condenser 3 becomes cryogen liquid in heated medium, the cryogen liquid of condenser 3 enters vaporizer 4 through throttle valve 5 throttling, absorb heat into refrigerant vapour and provide to adsorber 1, turbo machine 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 by vaporizer to absorption reverse circulation heat supply, absorption reverse circulation, by adsorber and the external heat supply of condenser, forms combined cycle energy supplying system.
Combined cycle energy supplying system 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 4 being had by compressor B refrigerant steam channel to be communicated with vaporizer 4 has cryogen liquid pipeline to be communicated with through cryogenic throttle valve C the finisher 4 being adjusted to compressor B and having refrigerant steam channel to be communicated with vaporizer 4 with low temperature heat exchanger D again has refrigerant steam channel to be communicated with the second compressor E again, and the finisher 4 that the second compressor E also has refrigerant steam channel to be communicated with vaporizer 4 has cryogen liquid pipeline to be communicated with low temperature heat exchanger D through cryogenic throttle valve C again; The refrigerant vapour that compressor B produces enters the second compressor E after flowing through vaporizer 4 heat release cooling, and the refrigerant vapour that the second compressor E produces provides to vaporizer 4, forms combined cycle energy supplying system.
Combined cycle energy supplying system shown in Fig. 3 is achieved in that
(1), in structure, it formed primarily of turbo machine, compressor, the second condenser, cryogenic throttle valve, low temperature heat exchanger, adsorber, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger; Outside has high pressure steam passage to be communicated with turbo machine A, turbo machine A also have low pressure steam passage be communicated with generator 2 after generator 2 have condensate line and ft connection again; Compressor B have refrigerant steam channel be communicated with the second condenser F after the second condenser F have cryogen liquid pipeline to be communicated with low temperature heat exchanger D through cryogenic throttle valve C again, low temperature heat exchanger D also has refrigerant steam channel to be communicated with compressor B, low temperature heat exchanger D also has cryogenic media pipeline and ft connection, and the second condenser F also has heated medium pipeline and ft connection; Vaporizer 4 has refrigerant steam channel to be communicated with adsorber 1, adsorber 1 also has dilute solution pipeline to be communicated with generator 2 with solution heat exchanger 7 through solution pump 6, generator 2 also has concentrated solution pipeline to be communicated with adsorber 1 through solution heat exchanger 7, generator 2 also has refrigerant steam channel to be communicated with condenser 3, condenser 3 also has cryogen liquid pipeline to be communicated with vaporizer 4 through throttle valve 5, vaporizer 4 also has cryogenic media pipeline and ft connection, and adsorber 1 and condenser 3 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with the energy supplying system of combined cycle shown in Fig. 1, difference is: compressor, the second condenser, cryogenic throttle valve and low temperature heat exchanger carry out compression type reverse circulation---refrigerant vapour enters compressor B, boosting flows through the second condenser F after heating up and heat release becomes cryogen liquid, and cryogen liquid enters low temperature heat exchanger D through cryogenic throttle valve C throttling, absorbs heat into refrigerant vapour and provide to compressor B; Vaporizer 4 directly obtains Low Temperature Thermal load from cryogenic media.
Combined cycle energy supplying system 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 B is had refrigerant steam channel be communicated with the second condenser F after the second condenser F have again cryogen liquid pipeline through cryogenic throttle valve C to be communicated with low temperature heat exchanger D be adjusted to compressor B have refrigerant steam channel to be communicated with the second condenser F after the second condenser F have refrigerant steam channel to be communicated with the second compressor E again, the second compressor E also have refrigerant steam channel be communicated with the second condenser F after the second condenser F have cryogen liquid pipeline to be communicated with low temperature heat exchanger D through cryogenic throttle valve C again; The refrigerant vapour that compressor B produces enters the second compressor E after flowing through the second condenser F heat release cooling, and the refrigerant vapour that the second compressor E produces provides to the second condenser F again, forms combined cycle energy supplying system.
Combined cycle energy supplying system shown in Fig. 5 is achieved in that
(1), in structure, it formed primarily of turbo machine, compressor, cooler, cryogenic throttle valve, low temperature heat exchanger, adsorber, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger; Outside has high pressure steam passage to be communicated with turbo machine A, turbo machine A also have low pressure steam passage be communicated with generator 2 after generator 2 have condensate line and ft connection again; The aftercooler G that compressor B has refrigerant steam channel to be communicated with cooler G has refrigerant steam channel to be communicated with vaporizer 4 again, vaporizer 4 also has cryogen liquid pipeline to be communicated with low temperature heat exchanger D through cryogenic throttle valve C, low temperature heat exchanger D also has refrigerant steam channel to be communicated with compressor B, low temperature heat exchanger D also has cryogenic media pipeline and ft connection, and cooler G also has heated medium pipeline and ft connection; Vaporizer 4 also has refrigerant steam channel to be communicated with adsorber 1, adsorber 1 also has dilute solution pipeline to be communicated with generator 2 with solution heat exchanger 7 through solution pump 6, generator 2 also has concentrated solution pipeline to be communicated with adsorber 1 through solution heat exchanger 7, generator 2 also has refrigerant steam channel to be communicated with condenser 3, condenser 3 also has cryogen liquid pipeline to be communicated with vaporizer 4 through throttle valve 5, and adsorber 1 and condenser 3 also have heated medium pipeline and ft connection respectively.
(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 B, boosting flows through cooler G after heating up and heat release cooling, refrigerant vapour after cooling flows through vaporizer 4 heat release and becomes cryogen liquid, and cryogen liquid enters low temperature heat exchanger D through cryogenic throttle valve C throttling, absorbs heat into refrigerant vapour and provide to compressor B.
Combined cycle energy supplying system 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 G being had by compressor B refrigerant steam channel to be communicated with cooler G has refrigerant steam channel to be communicated with vaporizer 4 to be adjusted to compressor B the aftercooler G having refrigerant steam channel to be communicated with cooler G to have refrigerant steam channel to be communicated with the second compressor E more again, and the aftercooler G that the second compressor E also has refrigerant steam channel to be communicated with cooler G has refrigerant steam channel to be communicated with vaporizer 4 again; The refrigerant vapour that compressor B produces is supplied to the second compressor E after flowing through cooler G heat release cooling, and the refrigerant vapour that the second compressor E produces is supplied to vaporizer 4 after flowing through cooler G heat release cooling, forms combined cycle energy supplying system.
Combined cycle energy supplying system shown in Fig. 7 is achieved in that
(1), in structure, it formed primarily of turbo machine, compressor, the second compressor, the second condenser, cryogenic throttle valve, the second cryogenic throttle valve, low temperature heat exchanger, adsorber, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger, outside has high pressure steam passage to be communicated with turbo machine A, turbo machine A also have low pressure steam passage be communicated with generator 2 after generator 2 have condensate line and ft connection again, compressor B has low pressure refrigerant steam channel to be communicated with vaporizer 4, vaporizer 4 also has low pressure cryogen liquid pipeline low temperature heat exchanger D after cryogenic throttle valve C is communicated with low temperature heat exchanger D to have refrigerant steam channel to be communicated with compressor B again, compressor B also has low pressure refrigerant steam channel to be communicated with the second compressor E, second compressor E also has high pressure refrigerant steam channel to be communicated with the second condenser F, second condenser F also has high pressure cryogen liquid pipeline low temperature heat exchanger D after vaporizer 4 and the second cryogenic throttle valve H are communicated with low temperature heat exchanger D to have refrigerant steam channel to be communicated with compressor B again, low temperature heat exchanger D also has cryogenic media pipeline and ft connection, second condenser F also has heated medium pipeline and ft connection, vaporizer 4 also has refrigerant steam channel to be communicated with adsorber 1, adsorber 1 also has dilute solution pipeline to be communicated with generator 2 with solution heat exchanger 7 through solution pump 6, generator 2 also has concentrated solution pipeline to be communicated with adsorber 1 through solution heat exchanger 7, generator 2 also has refrigerant steam channel to be communicated with condenser 3, condenser 3 also has cryogen liquid pipeline to be communicated with vaporizer 4 through throttle valve 5, and adsorber 1 and condenser 3 also have heated medium pipeline and ft connection respectively.
(2), in flow process, high pressure steam enters turbo machine A step-down work done and provides to compressor B, and the low pressure steam after work done is externally discharged after flowing through generator 2, exothermic condensation, 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 B, the rear portion of compressed one-tenth low pressure refrigerant vapour is supplied to the second compressor E, another part flows through vaporizer 4 and heat release enters low temperature heat exchanger D through cryogenic throttle valve C throttling after becoming low pressure cryogen liquid again, absorb heat into refrigerant vapour and provide to compressor B, the high pressure refrigerant vapour that second compressor E produces flows through the second condenser F and heat release becomes high pressure cryogen liquid in heated medium, high pressure cryogen liquid flows through after vaporizer 4 is lowered the temperature and enters low temperature heat exchanger D through the second cryogenic throttle valve H throttling again, absorb heat into refrigerant vapour and provide to compressor B, adsorber, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger carry out absorption reverse circulation---and the dilute solution of adsorber 1 enters generator 2 through solution pump 6 and solution heat exchanger 7, heat absorption release refrigerant vapour also provides to condenser 3, the concentrated solution of generator 2 enters adsorber 1 through solution heat exchanger 7, absorb refrigerant vapour heat release in heated medium, the refrigerant vapour heat release of condenser 3 becomes cryogen liquid in heated medium, the cryogen liquid of condenser 3 enters vaporizer 4 after throttle valve 5 throttling, absorb heat into refrigerant vapour and provide to adsorber 1, turbo machine 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 and the external heat supply of condenser, forms combined cycle energy supplying system.
Combined cycle energy supplying system shown in Fig. 8 is achieved in that
(1), in structure, it formed primarily of turbo machine, compressor, the second condenser, cryogenic throttle valve, the second cryogenic throttle valve, low temperature heat exchanger, adsorber, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger, outside has high pressure steam passage to be communicated with turbo machine A, turbo machine A also have low pressure steam passage be communicated with generator 2 after generator 2 have condensate line and ft connection again, compressor B has low pressure refrigerant steam channel to be communicated with vaporizer 4, vaporizer 4 also has low pressure cryogen liquid pipeline low temperature heat exchanger D after cryogenic throttle valve C is communicated with low temperature heat exchanger D to have refrigerant steam channel to be communicated with compressor B again, compressor B also has high pressure refrigerant steam channel to be communicated with the second condenser F, second condenser F also has high pressure cryogen liquid pipeline low temperature heat exchanger D after vaporizer 4 and the second cryogenic throttle valve H are communicated with low temperature heat exchanger D to have refrigerant steam channel to be communicated with compressor B again, low temperature heat exchanger D also has cryogenic media pipeline and ft connection, second condenser F also has heated medium pipeline and ft connection, vaporizer 4 also has refrigerant steam channel to be communicated with adsorber 1, adsorber 1 also has dilute solution pipeline to be communicated with generator 2 with solution heat exchanger 7 through solution pump 6, generator 2 also has concentrated solution pipeline to be communicated with adsorber 1 through solution heat exchanger 7, generator 2 also has refrigerant steam channel to be communicated with condenser 3, condenser 3 also has cryogen liquid pipeline to be communicated with vaporizer 4 through throttle valve 5, and adsorber 1 and condenser 3 also have heated medium pipeline and ft connection respectively.
(2), in flow process, high pressure steam enters turbo machine A step-down work done and provides to compressor B, and the low pressure steam after work done is externally discharged after flowing through generator 2, exothermic condensation, 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 B, 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 4 and heat release enters low temperature heat exchanger D through cryogenic throttle valve C throttling after becoming low pressure cryogen liquid again, absorb heat into refrigerant vapour and provide to compressor B, the high pressure refrigerant vapour that compressor B produces flows through the second condenser F and heat release becomes high pressure cryogen liquid in heated medium, high pressure cryogen liquid flows through after vaporizer 4 is lowered the temperature and enters low temperature heat exchanger D through the second cryogenic throttle valve H throttling again, absorb heat into refrigerant vapour and provide to compressor B, adsorber, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger carry out absorption reverse circulation---and the dilute solution of adsorber 1 enters generator 2 through solution pump 6 and solution heat exchanger 7, heat absorption release refrigerant vapour also provides to condenser 3, the concentrated solution of generator 2 enters adsorber 1 through solution heat exchanger 7, absorb refrigerant vapour heat release in heated medium, the refrigerant vapour heat release of condenser 3 becomes cryogen liquid in heated medium, the cryogen liquid of condenser 3 enters vaporizer 4 after throttle valve 5 throttling, absorb heat into refrigerant vapour and provide to adsorber 1, turbo machine 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 and the external heat supply of condenser, forms combined cycle energy supplying system.
Combined cycle energy supplying system shown in Fig. 9 is achieved in that
(1), in structure, it formed primarily of turbo machine, compressor, decompressor, vaporizer, low temperature heat exchanger, adsorber, generator, condenser, throttle valve, solution pump and solution heat exchanger; Outside has high pressure steam passage to be communicated with turbo machine A, turbo machine A also have low pressure steam passage be communicated with generator 2 after generator 2 have condensate line and ft connection again; The finisher 4 that compressor B has refrigerant gas passage to be communicated with vaporizer 4 has refrigerant gas passage to be communicated with decompressor I again, decompressor I also has refrigerant gas passage to be communicated with compressor B through low temperature heat exchanger D, and low temperature heat exchanger D also has cryogenic media pipeline and ft connection; Vaporizer 4 also has refrigerant steam channel to be communicated with adsorber 1, adsorber 1 also has dilute solution pipeline to be communicated with generator 2 with solution heat exchanger 7 through solution pump 6, generator 2 also has concentrated solution pipeline to be communicated with adsorber 1 through solution heat exchanger 7, generator 2 also has refrigerant steam channel to be communicated with condenser 3, condenser 3 also has cryogen liquid pipeline to be communicated with vaporizer 4 through throttle valve 5, and adsorber 1 and condenser 3 also have heated medium pipeline and ft connection respectively.
(2), in flow process, high pressure steam enters turbo machine A step-down work done and provides to compressor B, and the low pressure steam after work done is externally discharged after flowing through generator 2, exothermic condensation, compressor, vaporizer, decompressor and low temperature heat exchanger carry out compression type reverse circulation---and refrigerant gas enters compressor B boosting and heats up, flow through vaporizer 4 and heat release cooling, flow through decompressor I step-down work done, flow through low temperature heat exchanger D, heat absorption heats up and provides to compressor B, adsorber, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger carry out absorption reverse circulation---and the dilute solution of adsorber 1 enters generator 2 through solution pump 6 and solution heat exchanger 7, heat absorption release refrigerant vapour also provides to condenser 3, the concentrated solution of generator 2 enters adsorber 1 through solution heat exchanger 7, absorb refrigerant vapour heat release in heated medium, the refrigerant vapour heat release of condenser 3 becomes cryogen liquid in heated medium, the cryogen liquid of condenser 3 enters vaporizer 4 through throttle valve 5 throttling, absorb heat into refrigerant vapour and provide to adsorber 1, turbo machine 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 by vaporizer to absorption reverse circulation heat supply, absorption reverse circulation, by adsorber and the external heat supply of condenser, forms combined cycle energy supplying system.
Combined cycle energy supplying system 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 4 being had by compressor B refrigerant gas passage to be communicated with vaporizer 4 has refrigerant gas passage to be communicated with decompressor I to be adjusted to compressor B the finisher 4 having refrigerant gas passage to be communicated with vaporizer 4 to have refrigerant gas passage to be communicated with the second compressor E more again, the finisher 4 that second compressor E also has refrigerant gas passage to be communicated with vaporizer 4 has refrigerant gas passage to be communicated with decompressor I again, forms combined cycle energy supplying system.
Combined cycle energy supplying system shown in Figure 11 is achieved in that
(1), in structure, it formed primarily of turbo machine, compressor, vaporizer, decompressor, low temperature heat exchanger, regenerator, adsorber, generator, condenser, throttle valve, solution pump and solution heat exchanger; Outside has high pressure steam passage to be communicated with turbo machine A, turbo machine A also have low pressure steam passage be communicated with generator 2 after generator 2 have condensate line and ft connection again; The finisher 4 that compressor B has refrigerant gas passage to be communicated with vaporizer 4 has refrigerant gas passage to be communicated with decompressor I through regenerator J again, decompressor I also has refrigerant gas passage to be communicated with compressor B with regenerator J through low temperature heat exchanger D, and low temperature heat exchanger D also has cryogenic media pipeline and ft connection; Vaporizer 4 also has refrigerant steam channel to be communicated with adsorber 1, adsorber 1 also has dilute solution pipeline to be communicated with generator 2 with solution heat exchanger 7 through solution pump 6, generator 2 also has concentrated solution pipeline to be communicated with adsorber 1 through solution heat exchanger 7, generator 2 also has refrigerant steam channel to be communicated with condenser 3, condenser 3 also has cryogen liquid pipeline to be communicated with vaporizer 4 through throttle valve 5, and adsorber 1 and condenser 3 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with the energy supplying system of combined cycle shown in Fig. 9, difference is: the refrigerant gas that compressor B produces is supplied to regenerator J after flowing through vaporizer 4 heat release cooling, and refrigerant gas is supplied to decompressor I after flowing through regenerator J heat release cooling; Refrigerant gas, by after decompressor I work done, flows through low temperature heat exchanger D and regenerator J, progressively heat absorption successively and is supplied to compressor B after heating up.
Combined cycle energy supplying system 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 4 being had by compressor B refrigerant gas passage to be communicated with vaporizer 4 has refrigerant gas passage to be communicated with through regenerator J the finisher 4 being adjusted to compressor B and having refrigerant gas passage to be communicated with logical vaporizer 4 with decompressor I again has refrigerant gas passage to be communicated with the second compressor E again, the finisher 4 that second compressor E also has refrigerant gas passage to be communicated with vaporizer 4 has refrigerant gas passage to be communicated with decompressor I through regenerator J again, forms combined cycle energy supplying system.
Combined cycle energy supplying system shown in Figure 13 is achieved in that
(1), in structure, it formed primarily of turbo machine, compressor, decompressor, cooler, low temperature heat exchanger, vaporizer, adsorber, generator, condenser, throttle valve, solution pump and solution heat exchanger; Outside has high pressure steam passage to be communicated with turbo machine A, turbo machine A also have low pressure steam passage be communicated with generator 2 after generator 2 have condensate line and ft connection again; Compressor B has refrigerant gas passage to be communicated with decompressor I through cooler G, decompressor I also has refrigerant gas passage to be communicated with compressor B through low temperature heat exchanger D, low temperature heat exchanger D also has cryogenic media pipeline and ft connection, and cooler G also has heated medium pipeline and ft connection; Vaporizer 4 also has refrigerant steam channel to be communicated with adsorber 1, adsorber 1 also has dilute solution pipeline to be communicated with generator 2 with solution heat exchanger 7 through solution pump 6, generator 2 also has concentrated solution pipeline to be communicated with adsorber 1 through solution heat exchanger 7, generator 2 also has refrigerant steam channel to be communicated with condenser 3, condenser 3 also has cryogen liquid pipeline to be communicated with vaporizer 4 through throttle valve 5, vaporizer 4 also has cryogenic media pipeline and ft connection, and adsorber 1 and condenser 3 also have heated medium pipeline and ft connection respectively.
(2), in flow process, high pressure steam enters turbo machine A step-down work done and provides to compressor B, and the low pressure steam after work done is externally discharged after flowing through generator 2, exothermic condensation, compressor, cooler, decompressor and low temperature heat exchanger carry out compression type reverse circulation---and refrigerant gas enters compressor B boosting and heats up, flow through cooler G and heat release cooling, flow through decompressor I step-down work done, flow through low temperature heat exchanger D, heat absorption intensification backward compressor B provide, adsorber, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger carry out absorption reverse circulation---and the dilute solution of adsorber 1 enters generator 2 through solution pump 6 and solution heat exchanger 7, heat absorption release refrigerant vapour also provides to condenser 3, the concentrated solution of generator 2 enters adsorber 1 through solution heat exchanger 7, absorb refrigerant vapour heat release in heated medium, the refrigerant vapour heat release of condenser 3 becomes cryogen liquid in heated medium, the cryogen liquid of condenser 3 enters vaporizer 4 after throttle valve 5 throttling, absorb heat into refrigerant vapour and provide to adsorber 1, turbo machine 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 and the external heat supply of condenser, forms combined cycle energy supplying system.
Combined cycle energy supplying system 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 B refrigerant gas passage to be communicated with decompressor I through cooler G to be adjusted to compressor B and to have refrigerant gas passage to be communicated with the second compressor E through cooler G, the second compressor E also has refrigerant gas passage to be communicated with decompressor I through cooler G; The refrigerant gas that compressor B produces is supplied to the second compressor E after flowing through cooler G heat release cooling, and the refrigerant gas that the second compressor E produces is supplied to decompressor I after flowing through cooler G heat release, forms combined cycle energy supplying system.
Combined cycle energy supplying system shown in Figure 15 is achieved in that
(1), in structure, it formed primarily of turbo machine, compressor, cooler, decompressor, low temperature heat exchanger, regenerator, vaporizer, adsorber, generator, condenser, throttle valve, solution pump and solution heat exchanger; Outside has high pressure steam passage to be communicated with turbo machine A, turbo machine A also have low pressure steam passage be communicated with generator 2 after generator 2 have condensate line and ft connection again; Compressor B has refrigerant gas passage to be communicated with decompressor I with regenerator J through cooler G, decompressor I also has refrigerant gas passage to be communicated with compressor B with regenerator J through low temperature heat exchanger D, low temperature heat exchanger D also has cryogenic media pipeline and ft connection, and cooler G also has heated medium pipeline and ft connection; Vaporizer 4 has refrigerant steam channel to be communicated with adsorber 1, adsorber 1 also has dilute solution pipeline to be communicated with generator 2 with solution heat exchanger 7 through solution pump 6, generator 2 also has concentrated solution pipeline to be communicated with adsorber 1 through solution heat exchanger 7, generator 2 also has refrigerant steam channel to be communicated with condenser 3, condenser 3 also has cryogen liquid pipeline to be communicated with vaporizer 4 through throttle valve 5, vaporizer 4 also has cryogenic media pipeline and ft connection, and adsorber 1 and condenser 3 also have heated medium pipeline and ft connection respectively.
(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 B produces is supplied to decompressor I after flowing through cooler G and regenerator J, heat release cooling successively, refrigerant gas flows through decompressor I step-down work done, and refrigerant gas flows through low temperature heat exchanger D and regenerator J successively, the backward compressor B of heat absorption intensification provides.
Combined cycle energy supplying system 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 B refrigerant gas passage to be communicated with decompressor I through cooler G and regenerator J to be adjusted to compressor B and to have refrigerant gas passage to be communicated with the second compressor E through cooler G, the second compressor E has refrigerant gas passage to be communicated with decompressor I with regenerator J through cooler G again; The refrigerant gas that compressor B produces is supplied to the second compressor E after flowing through cooler G heat release cooling, the refrigerant gas that second compressor E produces is supplied to decompressor I after flowing through cooler G and regenerator J, progressively heat release cooling successively, forms combined cycle energy supplying system.
Combined cycle energy supplying system shown in Figure 17 is achieved in that
(1), in structure, it formed primarily of turbo machine, compressor, cooler, vaporizer, decompressor, low temperature heat exchanger, adsorber, generator, condenser, throttle valve, solution pump and solution heat exchanger; Outside has high pressure steam passage to be communicated with turbo machine A, turbo machine A also have low pressure steam passage be communicated with generator 2 after generator 2 have condensate line and ft connection again; Compressor B has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor I again through the finisher 4 that cooler G is communicated with vaporizer 4, decompressor I also has refrigerant gas passage to be communicated with compressor B through low temperature heat exchanger D, low temperature heat exchanger D also has cryogenic media pipeline and ft connection, and cooler G also has heated medium pipeline and ft connection; Vaporizer 4 also has refrigerant steam channel to be communicated with adsorber 1, adsorber 1 also has dilute solution pipeline to be communicated with generator 2 with solution heat exchanger 7 through solution pump 6, generator 2 also has concentrated solution pipeline to be communicated with adsorber 1 through solution heat exchanger 7, generator 2 also has refrigerant steam channel to be communicated with condenser 3, condenser 3 also has cryogen liquid pipeline to be communicated with vaporizer 4 through throttle valve 5, and adsorber 1 and condenser 3 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with the energy supplying system of combined cycle shown in Fig. 9, difference is: compressor B produce refrigerant gas flow through successively cooler G and vaporizer 4, progressively heat release cooling after be supplied to decompressor I, 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.
Combined cycle energy supplying system 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 B refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor I to be again adjusted to compressor B through the finisher 4 that cooler G is communicated with vaporizer 4 and have refrigerant gas passage to have refrigerant gas passage to be communicated with the second compressor E again through the finisher 4 that cooler G is communicated with vaporizer 4, the second compressor E also has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor I again through the finisher 4 that cooler G is communicated with vaporizer 4; The refrigerant gas that compressor B produces flows through cooler G successively and vaporizer 4, heat release are supplied to the second compressor E after lowering the temperature, the refrigerant gas that second compressor E produces flows through cooler G successively and vaporizer 4, heat release are supplied to decompressor I after lowering the temperature, and forms combined cycle energy supplying system.
Combined cycle energy supplying system shown in Figure 19 is achieved in that
(1), in structure, it formed primarily of turbo machine, compressor, cooler, vaporizer, regenerator, decompressor, low temperature heat exchanger, adsorber, generator, condenser, throttle valve, solution pump and solution heat exchanger; Outside has high pressure steam passage to be communicated with turbo machine A, turbo machine A also have low pressure steam passage be communicated with generator 2 after generator 2 have condensate line and ft connection again; Compressor B has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor I through regenerator J again through the finisher 4 that cooler G is communicated with vaporizer 4, decompressor I also has refrigerant gas passage to be communicated with compressor B with regenerator J through low temperature heat exchanger D, low temperature heat exchanger D also has cryogenic media pipeline and ft connection, and cooler G also has heated medium pipeline and ft connection; Vaporizer 4 also has refrigerant steam channel to be communicated with adsorber 1, adsorber 1 also has dilute solution pipeline to be communicated with generator 2 with solution heat exchanger 7 through solution pump 6, generator 2 also has concentrated solution pipeline to be communicated with adsorber 1 through solution heat exchanger 7, generator 2 also has refrigerant steam channel to be communicated with condenser 3, condenser 3 also has cryogen liquid pipeline to be communicated with vaporizer 4 through throttle valve 5, and adsorber 1 and condenser 3 also have heated medium pipeline and ft connection respectively.
(2) in flow process, compared with the energy supplying system of combined cycle shown in Figure 17, difference is: the refrigerant gas that compressor B produces is supplied to decompressor I after flowing through cooler G, vaporizer 4 and regenerator J heat release cooling successively, and the refrigerant gas that decompressor I discharges flows through low temperature heat exchanger D and regenerator J successively, heat absorption is supplied to compressor B after heating up.
Combined cycle energy supplying system 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 B refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor I through regenerator J again through the finisher 4 that cooler G is communicated with vaporizer 4 to be adjusted to compressor B and to have refrigerant gas passage to have refrigerant gas passage to be communicated with the second compressor E again through the finisher 4 that cooler G is communicated with vaporizer 4, the second compressor E also has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor I through regenerator J again through the finisher 4 that cooler G is communicated with vaporizer 4; The refrigerant gas that compressor B produces flows through cooler G successively and vaporizer 4, heat release are supplied to the second compressor E after lowering the temperature, the refrigerant gas that second compressor E produces is supplied to decompressor I after flowing through cooler G, vaporizer 4 and regenerator J heat release cooling successively, forms combined cycle energy supplying system.
Combined cycle energy supplying system shown in Figure 21 is achieved in that
(1) in structure, in the energy supplying system of combined cycle shown in Fig. 1, increase heat exchanger, the rear heat exchange 8 that being had by generator 2 condensate line and ft connection to be adjusted to generator 2 has condensate line to be communicated with heat exchanger 8 has condensate line and ft connection again, and heat exchanger 8 also has heated medium pipeline and ft connection, increase by the second generator, second throttle, second solution pump and the second solution heat exchanger, adsorber 1 is set up dilute solution pipeline and is communicated with the second generator 9 with the second solution heat exchanger 12 through the second solution pump 11, second generator 9 also has concentrated solution pipeline to be communicated with adsorber 1 through the second solution heat exchanger 12, had by generator 2 refrigerant steam channel to be communicated with condenser 3 to be adjusted to generator 2 have refrigerant steam channel be communicated with the second generator 9 after the second generator 9 have cryogen liquid pipeline to be communicated with condenser 3 through second throttle 10 again, second generator 9 also has refrigerant steam channel to be communicated with condenser 3.
(2) in flow process, the low pressure steam that turbo machine A discharges flows through generator 2 heat release and becomes solidifying water, and solidifying current are externally discharged after heat exchanger 8, heat release cooling; Generator 2 produces refrigerant vapour and is supplied to the second generator 9 do driving thermal medium, the part dilute solution of adsorber 1 enters the second generator 9 through the second solution pump 11 and the second solution heat exchanger 12, refrigerant vapour flows through the second generator 9, heating enters the solution release refrigerant vapour in it and provides to condenser 3, the concentrated solution of the second generator 9 enters adsorber 1 through the second solution heat exchanger 12, enter condenser 3 through second throttle 10 throttling after the refrigerant vapour heat release flowing through the second generator 9 becomes cryogen liquid, form combined cycle energy supplying system.
Combined cycle energy supplying system shown in Figure 22 is achieved in that
(1) in structure, in the energy supplying system of combined cycle shown in Fig. 1, increase heat exchanger, the rear heat exchange 8 that being had by generator 2 condensate line and ft connection to be adjusted to generator 2 has condensate line to be communicated with heat exchanger 8 has condensate line and ft connection again, and heat exchanger 8 also has heated medium pipeline and ft connection, increase by the second generator, second throttle and the second solution heat exchanger, had by adsorber 1 dilute solution pipeline to be communicated with generator 2 through solution pump 6 and solution heat exchanger 7 to be adjusted to adsorber 1 and to have dilute solution pipeline through solution pump 6, solution heat exchanger 7 is communicated with generator 2 with the second solution heat exchanger 12, had by generator 2 concentrated solution pipeline to be communicated with adsorber 1 through solution heat exchanger 7 to be adjusted to generator 2 and to have concentrated solution pipeline to be communicated with the second generator 9 through the second solution heat exchanger 12, second generator 9 has concentrated solution pipeline to be communicated with adsorber 1 through solution heat exchanger 7 again, had by generator 2 refrigerant steam channel to be communicated with condenser 3 to be adjusted to generator 2 have refrigerant steam channel be communicated with the second generator 9 after the second generator 9 have cryogen liquid pipeline to be communicated with condenser 3 through second throttle 10 again, second generator 9 also has refrigerant steam channel to be communicated with condenser 3.
(2) in flow process, the low pressure steam that turbo machine A discharges flows through generator 2 heat release and becomes solidifying water, and solidifying current are externally discharged after heat exchanger 8, heat release cooling, generator 2 produces refrigerant vapour and is supplied to the second generator 9 do driving thermal medium, the concentrated solution of adsorber 1 is through solution pump 6, solution heat exchanger 7 and the second solution heat exchanger 12 enter generator 2, the concentrated solution of generator 2 enters the second generator 9 through the second solution heat exchanger 12, refrigerant vapour flows through the second generator 9, heating enters the solution release refrigerant vapour in it and provides to condenser 3, the concentrated solution of the second generator 9 enters adsorber 1 through solution heat exchanger 7, condenser 3 is entered through second throttle 10 throttling after the refrigerant vapour heat release flowing through the second generator 9 becomes cryogen liquid, form combined cycle energy supplying system.
Combined cycle energy supplying system shown in Figure 23 is achieved in that
(1) in structure, in the energy supplying system of combined cycle shown in Fig. 1, increase heat exchanger, the rear heat exchange 8 that being had by generator 2 condensate line and ft connection to be adjusted to generator 2 has condensate line to be communicated with heat exchanger 8 has condensate line and ft connection again, and heat exchanger 8 also has heated medium pipeline and ft connection, increase by the second generator, second throttle, second solution pump and the second solution heat exchanger, had by adsorber 1 dilute solution pipeline to be communicated with generator 2 through solution pump 6 and solution heat exchanger 7 to be adjusted to adsorber 1 and to have dilute solution pipeline to be communicated with the second generator 9 with solution heat exchanger 7 through solution pump 6, second generator 9 has concentrated solution pipeline to be communicated with generator 2 with the second solution heat exchanger 12 through the second solution pump 11 again, had by generator 2 concentrated solution pipeline to be communicated with adsorber 1 through solution heat exchanger 7 to be adjusted to generator 2 and to have concentrated solution pipeline to be communicated with adsorber 1 with solution heat exchanger 7 through the second solution heat exchanger 12, had by generator 2 refrigerant steam channel to be communicated with condenser 3 to be adjusted to generator 2 have refrigerant steam channel be communicated with the second generator 9 after the second generator 9 have cryogen liquid pipeline to be communicated with condenser 3 through second throttle 10 again, second generator 9 also has refrigerant steam channel to be communicated with condenser 3.
(2) in flow process, the low pressure steam that turbo machine A discharges flows through generator 2 heat release and becomes solidifying water, and solidifying current are externally discharged after heat exchanger 8, heat release cooling, generator 2 produces refrigerant vapour and is supplied to the second generator 9 do driving thermal medium, the dilute solution of adsorber 1 enters the second generator 9 through solution pump 6 and solution heat exchanger 7, refrigerant vapour flows through the second generator 9, heating enters the solution release refrigerant vapour in it and provides to condenser 3, the concentrated solution of the second generator 9 enters generator 2 through the second solution pump 11 and the second solution heat exchanger 12, the concentrated solution of generator 2 enters adsorber 1 through the second solution heat exchanger 12 and solution heat exchanger 7, condenser 3 is entered through second throttle 10 throttling after the refrigerant vapour heat release flowing through the second generator 9 becomes cryogen liquid, form combined cycle energy supplying system.
Combined cycle energy supplying system shown in Figure 24 is achieved in that
(1) in structure, in the energy supplying system of combined cycle shown in Figure 21, increase by the 3rd generator, 3rd throttle valve, 3rd solution pump and the 3rd solution heat exchanger, adsorber 1 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 adsorber 1 through the 3rd solution heat exchanger 16, had by second generator 9 refrigerant steam channel to be communicated with condenser 3 to be adjusted to the second generator 9 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 3 through the 3rd throttle valve 14 again, 3rd generator 13 also has refrigerant steam channel to be communicated with condenser 3.
(2) in flow process, the refrigerant vapour that second generator 9 produces is supplied to the 3rd generator 13 and does to drive thermal medium, the part dilute solution of adsorber 1 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 3, the concentrated solution of the 3rd generator 13 enters adsorber 1 through the 3rd solution heat exchanger 16, condenser 3 is entered through the 3rd throttle valve 14 throttling after the refrigerant vapour heat release flowing through the 3rd generator 13 becomes cryogen liquid, form combined cycle energy supplying system.
Combined cycle energy supplying system shown in Figure 25 is achieved in that
(1) in structure, in the energy supplying system of combined cycle shown in Figure 22, there is by the second generator 9 cryogen liquid pipeline to be communicated with condenser 3 through second throttle 10 and be adjusted to the second generator 9 and have cryogen liquid pipeline to be communicated with condenser 3 with second throttle 10 through the 3rd generator 13, increase by the 3rd generator, 3rd throttle valve and the 3rd solution heat exchanger, adsorber 1 there is dilute solution pipeline through solution pump 6, solution heat exchanger 7 and the second solution heat exchanger 12 are communicated with generator 2 and are adjusted to adsorber 1 and have dilute solution pipeline through solution pump 6, solution heat exchanger 7, 3rd solution heat exchanger 16 is communicated with generator 2 with the second solution heat exchanger 12, had by second generator 9 concentrated solution pipeline to be communicated with adsorber 1 through solution heat exchanger 7 to be adjusted to the second generator 9 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 adsorber 1 through solution heat exchanger 7 again, had by second generator 9 refrigerant steam channel to be communicated with condenser 3 to be adjusted to the second generator 9 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 3 through the 3rd throttle valve 14 again, 3rd generator 13 also has refrigerant steam channel to be communicated with condenser 3.
(2) in flow process, the cryogen liquid that second generator 9 produces and refrigerant vapour are supplied to the 3rd generator 13 and do to drive thermal medium, the dilute solution of adsorber 1 is through solution pump 6, solution heat exchanger 7, 3rd solution heat exchanger 16 and the second solution heat exchanger 12 enter generator 2, the concentrated solution of generator 2 enters the second generator 9 through the second solution heat exchanger 12, the concentrated solution of the second generator 9 enters the 3rd generator 13 through the 3rd solution heat exchanger 16, refrigerant vapour and cryogen liquid flow through the 3rd generator 13, heating enters the solution release refrigerant vapour in it and provides to condenser 3, the concentrated solution of the 3rd generator 13 enters adsorber 1 through solution heat exchanger 7, condenser 3 is entered through the 3rd throttle valve 14 throttling after the refrigerant vapour heat release flowing through the 3rd generator 13 becomes cryogen liquid, form combined cycle energy supplying system.
Combined cycle energy supplying system shown in Figure 26 is achieved in that
(1) in structure, in the energy supplying system of combined cycle shown in Figure 23, increase by the 3rd generator, 3rd throttle valve, 3rd solution pump and the 3rd solution heat exchanger, had by adsorber 1 dilute solution pipeline to be communicated with the second generator 9 through solution pump 6 and solution heat exchanger 7 to be adjusted to adsorber 1 and to have dilute solution pipeline to be communicated with the 3rd generator 13 with solution heat exchanger 7 through solution pump 6,3rd generator 13 has concentrated solution pipeline to be communicated with the second generator 9 with the 3rd solution heat exchanger 16 through the 3rd solution pump 15 again, had by generator 2 concentrated solution pipeline to be communicated with adsorber 1 through the second solution heat exchanger 12 and solution heat exchanger 7 to be adjusted to generator 2 and to have concentrated solution pipeline through the second solution heat exchanger 12,3rd solution heat exchanger 16 is communicated with adsorber 1 with solution heat exchanger 7, had by second generator 9 refrigerant steam channel to be communicated with condenser 3 to be adjusted to the second generator 9 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 3 through the 3rd throttle valve 14 again, 3rd generator 13 also has refrigerant steam channel to be communicated with condenser 3.
(2) in flow process, the refrigerant vapour that second generator 9 produces is supplied to the 3rd generator 13 and does to drive thermal medium, the dilute solution of adsorber 1 enters the 3rd generator 13 through solution pump 6 and solution heat exchanger 7, refrigerant vapour flows through the 3rd generator 13, heating enters the solution release refrigerant vapour in it and provides to condenser 3, the concentrated solution of the 3rd generator 13 enters the second generator 9 through the 3rd solution pump 15 and the 3rd solution heat exchanger 16, the concentrated solution of the second generator 9 enters generator 2 through the second solution pump 11 and the second solution heat exchanger 12, the concentrated solution of generator 2 is through the second solution heat exchanger 12, 3rd solution heat exchanger 16 and solution heat exchanger 7 enter adsorber 1, condenser 3 is entered through the 3rd throttle valve 14 throttling after the refrigerant vapour heat release flowing through the 3rd generator 13 becomes cryogen liquid, form combined cycle energy supplying system.
Combined cycle energy supplying system shown in Figure 27 is achieved in that
(1) in structure, in the energy supplying system of combined cycle shown in Fig. 1, increase by the second generator, second solution pump, second solution heat exchanger and the second adsorber, turbo machine A is had low pressure steam passage be communicated with generator 2 after generator 2 have again condensate line and ft connection be adjusted to turbo machine A have low pressure steam passage be communicated with generator 2 and the second generator 9 successively after the second generator 9 have condensate line and ft connection again, being had by vaporizer 4 refrigerant steam channel to be communicated with adsorber 1 to be adjusted to vaporizer 4 has refrigerant steam channel to be communicated with the second adsorber 17, second adsorber 17 also has dilute solution pipeline to be communicated with the second generator 9 with the second solution heat exchanger 12 through the second solution pump 11, second generator 9 also has concentrated solution pipeline to be communicated with the second adsorber 17 through the second solution heat exchanger 12, second generator 9 also has refrigerant steam channel to be communicated with adsorber 1, second adsorber 17 also has heated medium pipeline and ft connection.
(2) in flow process, the low pressure steam that turbo machine A discharges flows through generator 2 successively and the second generator 9, progressively heat release form solidifying water and externally discharge, the refrigerant vapour that vaporizer 4 produces enters the second adsorber 17, the dilute solution of the second adsorber 17 enters the second generator 9 through the second solution pump 11 and the second solution heat exchanger 12, absorbing heat discharges refrigerant vapour and provide to adsorber 1, the concentrated solution of the second generator 9 enters the second adsorber 19 through the second solution heat exchanger 12, absorb refrigerant vapour and heat release in heated medium, form combined cycle energy supplying system.
Combined cycle energy supplying system shown in Figure 28 is achieved in that
In the energy supplying system of combined cycle shown in Fig. 1, increase working machine, had by turbo machine A low pressure steam passage to be communicated with generator 2 to be adjusted to the turbo machine A passage that draws gas to be communicated with generator 2, turbo machine A sets up exhaust steam passage and ft connection; High pressure steam flows through turbo machine A step-down work done and provides respectively to compressor B and working machine K, and turbo machine part A is drawn gas and is supplied to generator 2 do driving thermal medium, and turbo machine A externally discharges exhaust steam, 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) technological scheme is reasonable, realizes heat energy efficiency utilization, realizes 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) the driving heat load reduced after temperature is used for absorption heat pump, ensures to drive between thermal medium and working medium to have the rational temperature difference.
(4) high-temperature hot load can be reduced or solve, low-temperature heat source source or grade, working medium select and the contradiction that realizes between heat energy efficiency utilization, compression heat pump and the absorption heat pump application space in heat energy efficiency utilization field can be expanded.

Claims (32)

1. combined cycle energy supplying system, formed primarily of turbo machine, compressor, cryogenic throttle valve, low temperature heat exchanger, adsorber, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger, outside has high pressure steam passage to be communicated with turbo machine (A), turbo machine (A) also have low pressure steam passage be communicated with generator (2) after generator (2) have condensate line and ft connection again, the finisher (4) that compressor (B) has refrigerant steam channel to be communicated with vaporizer (4) has cryogen liquid pipeline to be communicated with low temperature heat exchanger (D) through cryogenic throttle valve (C) again, low temperature heat exchanger (D) also has refrigerant steam channel to be communicated with compressor (B), and low temperature heat exchanger (D) also has cryogenic media pipeline and ft connection, vaporizer (4) also has refrigerant steam channel to be communicated with adsorber (1), adsorber (1) also has dilute solution pipeline to be communicated with generator (2) with solution heat exchanger (7) through solution pump (6), generator (2) also has concentrated solution pipeline to be communicated with adsorber (1) through solution heat exchanger (7), generator (2) also has refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline to be communicated with vaporizer (4) through throttle valve (5), adsorber (1) and condenser (3) also have heated medium pipeline and ft connection respectively, compressor, vaporizer, cryogenic throttle valve and low temperature heat exchanger form compression type reverse circulation system, and adsorber, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger form absorption reverse circulation system, turbo machine provides power to compression type reverse circulation or externally provides power simultaneously, turbo machine 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 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 (4) being had by compressor (B) refrigerant steam channel to be communicated with vaporizer (4) has cryogen liquid pipeline to be communicated with through cryogenic throttle valve (C) finisher (4) being adjusted to compressor (B) and having refrigerant steam channel to be communicated with vaporizer (4) with low temperature heat exchanger (D) again has refrigerant steam channel to be communicated with the second compressor (E) again, the finisher (4) that second compressor (E) also has refrigerant steam channel to be communicated with vaporizer (4) has cryogen liquid pipeline to be communicated with low temperature heat exchanger (D) through cryogenic throttle valve (C) again, form combined cycle energy supplying system.
3. combined cycle energy supplying system, formed primarily of turbo machine, compressor, the second condenser, cryogenic throttle valve, low temperature heat exchanger, adsorber, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger, outside has high pressure steam passage to be communicated with turbo machine (A), turbo machine (A) also have low pressure steam passage be communicated with generator (2) after generator (2) have condensate line and ft connection again, compressor (B) have refrigerant steam channel be communicated with the second condenser (F) after the second condenser (F) have cryogen liquid pipeline to be communicated with low temperature heat exchanger (D) through cryogenic throttle valve (C) again, low temperature heat exchanger (D) also has refrigerant steam channel to be communicated with compressor (B), low temperature heat exchanger (D) also has cryogenic media pipeline and ft connection, and the second condenser (F) also has heated medium pipeline and ft connection, vaporizer (4) has refrigerant steam channel to be communicated with adsorber (1), adsorber (1) also has dilute solution pipeline to be communicated with generator (2) with solution heat exchanger (7) through solution pump (6), generator (2) also has concentrated solution pipeline to be communicated with adsorber (1) through solution heat exchanger (7), generator (2) also has refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline to be communicated with vaporizer (4) through throttle valve (5), vaporizer (4) also has cryogenic media pipeline and ft connection, adsorber (1) and condenser (3) also have heated medium pipeline and ft connection respectively, compressor, the second condenser, cryogenic throttle valve and low temperature heat exchanger form compression type reverse circulation system, and adsorber, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger form absorption reverse circulation system, turbo machine provides power to compression type reverse circulation or externally provides power simultaneously, turbo machine 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 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 (B) is had refrigerant steam channel be communicated with the second condenser (F) after the second condenser (F) have again cryogen liquid pipeline through cryogenic throttle valve (C) to be communicated with low temperature heat exchanger (D) be adjusted to compressor (B) have refrigerant steam channel to be communicated with the second condenser (F) after the second condenser (F) have refrigerant steam channel to be communicated with the second compressor (E) again, second compressor (E) also have refrigerant steam channel be communicated with the second condenser (F) after the second condenser (F) have cryogen liquid pipeline to be communicated with low temperature heat exchanger (D) through cryogenic throttle valve (C) again, form combined cycle energy supplying system.
5. combined cycle energy supplying system, formed primarily of turbo machine, compressor, cooler, cryogenic throttle valve, low temperature heat exchanger, adsorber, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger, outside has high pressure steam passage to be communicated with turbo machine (A), turbo machine (A) also have low pressure steam passage be communicated with generator (2) after generator (2) have condensate line and ft connection again, the aftercooler (G) that compressor (B) has refrigerant steam channel to be communicated with cooler (G) has refrigerant steam channel to be communicated with vaporizer (4) again, vaporizer (4) also has cryogen liquid pipeline to be communicated with low temperature heat exchanger (D) through cryogenic throttle valve (C), low temperature heat exchanger (D) also has refrigerant steam channel to be communicated with compressor (B), low temperature heat exchanger (D) also has cryogenic media pipeline and ft connection, and cooler (G) also has heated medium pipeline and ft connection, vaporizer (4) also has refrigerant steam channel to be communicated with adsorber (1), adsorber (1) also has dilute solution pipeline to be communicated with generator (2) with solution heat exchanger (7) through solution pump (6), generator (2) also has concentrated solution pipeline to be communicated with adsorber (1) through solution heat exchanger (7), generator (2) also has refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline to be communicated with vaporizer (4) through throttle valve (5), adsorber (1) and condenser (3) also have heated medium pipeline and ft connection respectively, compressor, cooler, vaporizer, cryogenic throttle valve and low temperature heat exchanger form compression type reverse circulation system, and adsorber, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger form the absorption reverse circulation system of row, turbo machine provides power to compression type reverse circulation or externally provides power simultaneously, turbo machine 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 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 (G) being had by compressor (B) refrigerant steam channel to be communicated with cooler (G) has refrigerant steam channel to be communicated with vaporizer (4) to be adjusted to compressor (B) aftercooler (G) having refrigerant steam channel to be communicated with cooler (G) to have refrigerant steam channel to be communicated with the second compressor (E) more again, the aftercooler (G) that second compressor (E) also has refrigerant steam channel to be communicated with cooler (G) has refrigerant steam channel to be communicated with vaporizer (4) again, form combined cycle energy supplying system.
7. combined cycle energy supplying system, formed primarily of turbo machine, compressor, the second compressor, the second condenser, cryogenic throttle valve, the second cryogenic throttle valve, low temperature heat exchanger, adsorber, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger, outside has high pressure steam passage to be communicated with turbo machine (A), turbo machine (A) also have low pressure steam passage be communicated with generator (2) after generator (2) have condensate line and ft connection again, compressor (B) has low pressure refrigerant steam channel to be communicated with vaporizer (4), vaporizer (4) also has low pressure cryogen liquid pipeline low temperature heat exchanger (D) after cryogenic throttle valve (C) is communicated with low temperature heat exchanger (D) to have refrigerant steam channel to be communicated with compressor (B) again, compressor (B) also has low pressure refrigerant steam channel to be communicated with the second compressor (E), second compressor (E) also has high pressure refrigerant steam channel to be communicated with the second condenser (F), second condenser (F) also has high pressure cryogen liquid pipeline low temperature heat exchanger (D) after vaporizer (4) and the second cryogenic throttle valve (H) are communicated with low temperature heat exchanger (D) to have refrigerant steam channel to be communicated with compressor (B) again, low temperature heat exchanger (D) also has cryogenic media pipeline and ft connection, second condenser (F) also has heated medium pipeline and ft connection, vaporizer (4) also has refrigerant steam channel to be communicated with adsorber (1), adsorber (1) also has dilute solution pipeline to be communicated with generator (2) with solution heat exchanger (7) through solution pump (6), generator (2) also has concentrated solution pipeline to be communicated with adsorber (1) through solution heat exchanger (7), generator (2) also has refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline to be communicated with vaporizer (4) through throttle valve (5), adsorber (1) and condenser (3) also have heated medium pipeline and ft connection respectively, 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, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger form absorption reverse circulation system, turbo machine provides power to compression type reverse circulation or externally provides power simultaneously, turbo machine 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 and the external heat supply of condenser, forms combined cycle energy supplying system.
8. combined cycle energy supplying system, formed primarily of turbo machine, compressor, the second condenser, cryogenic throttle valve, the second cryogenic throttle valve, low temperature heat exchanger, adsorber, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger, outside has high pressure steam passage to be communicated with turbo machine (A), turbo machine (A) also have low pressure steam passage be communicated with generator (2) after generator (2) have condensate line and ft connection again, compressor (B) has low pressure refrigerant steam channel to be communicated with vaporizer (4), vaporizer (4) also has low pressure cryogen liquid pipeline low temperature heat exchanger (D) after cryogenic throttle valve (C) is communicated with low temperature heat exchanger (D) to have refrigerant steam channel to be communicated with compressor (B) again, compressor (B) also has high pressure refrigerant steam channel to be communicated with the second condenser (F), second condenser (F) also has high pressure cryogen liquid pipeline low temperature heat exchanger (D) after vaporizer (4) and the second cryogenic throttle valve (H) are communicated with low temperature heat exchanger (D) to have refrigerant steam channel to be communicated with compressor (B) again, low temperature heat exchanger (D) also has cryogenic media pipeline and ft connection, second condenser (F) also has heated medium pipeline and ft connection, vaporizer (4) also has refrigerant steam channel to be communicated with adsorber (1), adsorber (1) also has dilute solution pipeline to be communicated with generator (2) with solution heat exchanger (7) through solution pump (6), generator (2) also has concentrated solution pipeline to be communicated with adsorber (1) through solution heat exchanger (7), generator (2) also has refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline to be communicated with vaporizer (4) through throttle valve (5), adsorber (1) and condenser (3) also have heated medium pipeline and ft connection respectively, 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, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger form absorption reverse circulation system, turbo machine provides power to compression type reverse circulation or externally provides power simultaneously, turbo machine 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 and the external heat supply of condenser, forms combined cycle energy supplying system.
9. combined cycle energy supplying system, formed primarily of turbo machine, compressor, decompressor, vaporizer, low temperature heat exchanger, adsorber, generator, condenser, throttle valve, solution pump and solution heat exchanger, outside has high pressure steam passage to be communicated with turbo machine (A), turbo machine (A) also have low pressure steam passage be communicated with generator (2) after generator (2) have condensate line and ft connection again, the finisher (4) that compressor (B) has refrigerant gas passage to be communicated with vaporizer (4) has refrigerant gas passage to be communicated with decompressor (I) again, decompressor (I) also has refrigerant gas passage to be communicated with compressor (B) through low temperature heat exchanger (D), and low temperature heat exchanger (D) also has cryogenic media pipeline and ft connection, vaporizer (4) also has refrigerant steam channel to be communicated with adsorber (1), adsorber (1) also has dilute solution pipeline to be communicated with generator (2) with solution heat exchanger (7) through solution pump (6), generator (2) also has concentrated solution pipeline to be communicated with adsorber (1) through solution heat exchanger (7), generator (2) also has refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline to be communicated with vaporizer (4) through throttle valve (5), adsorber (1) and condenser (3) also have heated medium pipeline and ft connection respectively, compressor, vaporizer, decompressor and low temperature heat exchanger form compression type reverse circulation system, and vaporizer, adsorber, generator, condenser, throttle valve, solution pump and solution heat exchanger form absorption reverse circulation system, turbo machine provides power to compression type reverse circulation or externally provides power simultaneously, turbo machine 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 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 (4) being had by compressor (B) refrigerant gas passage to be communicated with vaporizer (4) has refrigerant gas passage to be communicated with decompressor (I) to be adjusted to compressor (B) finisher (4) having refrigerant gas passage to be communicated with vaporizer (4) to have refrigerant gas passage to be communicated with the second compressor (E) more again, the finisher (4) that second compressor (E) also has refrigerant gas passage to be communicated with vaporizer (4) has refrigerant gas passage to be communicated with decompressor (I) again, form combined cycle energy supplying system.
11. combined cycle energy supplying systems, formed primarily of turbo machine, compressor, vaporizer, decompressor, low temperature heat exchanger, regenerator, adsorber, generator, condenser, throttle valve, solution pump and solution heat exchanger, outside has high pressure steam passage to be communicated with turbo machine (A), turbo machine (A) also have low pressure steam passage be communicated with generator (2) after generator (2) have condensate line and ft connection again, the finisher (4) that compressor (B) has refrigerant gas passage to be communicated with vaporizer (4) has refrigerant gas passage to be communicated with decompressor (I) through regenerator (J) again, decompressor (I) also has refrigerant gas passage to be communicated with compressor (B) with regenerator (J) through low temperature heat exchanger (D), and low temperature heat exchanger (D) also has cryogenic media pipeline and ft connection, vaporizer (4) also has refrigerant steam channel to be communicated with adsorber (1), adsorber (1) also has dilute solution pipeline to be communicated with generator (2) with solution heat exchanger (7) through solution pump (6), generator (2) also has concentrated solution pipeline to be communicated with adsorber (1) through solution heat exchanger (7), generator (2) also has refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline to be communicated with vaporizer (4) through throttle valve (5), adsorber (1) and condenser (3) also have heated medium pipeline and ft connection respectively, compressor, vaporizer, decompressor, low temperature heat exchanger and regenerator form compression type reverse circulation system, and vaporizer, adsorber, generator, condenser, throttle valve, solution pump and solution heat exchanger form absorption reverse circulation system, turbo machine provides power to compression type reverse circulation or externally provides power simultaneously, turbo machine 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 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 (4) being had by compressor (B) refrigerant gas passage to be communicated with vaporizer (4) has refrigerant gas passage to be communicated with through regenerator (J) finisher (4) being adjusted to compressor (B) and having refrigerant gas passage to be communicated with logical vaporizer (4) with decompressor (I) again has refrigerant gas passage to be communicated with the second compressor (E) again, the finisher (4) that second compressor (E) also has refrigerant gas passage to be communicated with vaporizer (4) has refrigerant gas passage to be communicated with decompressor (I) through regenerator (J) again, form combined cycle energy supplying system.
13. combined cycle energy supplying systems, formed primarily of turbo machine, compressor, decompressor, cooler, low temperature heat exchanger, vaporizer, adsorber, generator, condenser, throttle valve, solution pump and solution heat exchanger, outside has high pressure steam passage to be communicated with turbo machine (A), turbo machine (A) also have low pressure steam passage be communicated with generator (2) after generator (2) have condensate line and ft connection again, compressor (B) has refrigerant gas passage to be communicated with decompressor (I) through cooler (G), decompressor (I) also has refrigerant gas passage to be communicated with compressor (B) through low temperature heat exchanger (D), low temperature heat exchanger (D) also has cryogenic media pipeline and ft connection, and cooler (G) also has heated medium pipeline and ft connection, vaporizer (4) has refrigerant steam channel to be communicated with adsorber (1), adsorber (1) also has dilute solution pipeline to be communicated with generator (2) with solution heat exchanger (7) through solution pump (6), generator (2) also has concentrated solution pipeline to be communicated with adsorber (1) through solution heat exchanger (7), generator (2) also has refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline to be communicated with vaporizer (4) through throttle valve (5), vaporizer (4) also has cryogenic media pipeline and ft connection, adsorber (1) and condenser (3) also have heated medium pipeline and ft connection respectively, compressor, cooler, decompressor and low temperature heat exchanger form compression type reverse circulation system, and adsorber, generator, condenser, vaporizer, throttle valve, solution pump and solution heat exchanger form absorption reverse circulation system, turbo machine provides power to compression type reverse circulation or externally provides power simultaneously, turbo machine 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 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 (B) refrigerant gas passage to be communicated with decompressor (I) through cooler (G) to be adjusted to compressor (B) and to have refrigerant gas passage to be communicated with the second compressor (E) through cooler (G), second compressor (E) also has refrigerant gas passage to be communicated with decompressor (I) through cooler (G), forms combined cycle energy supplying system.
15. combined cycle energy supplying systems, formed primarily of turbo machine, compressor, cooler, decompressor, low temperature heat exchanger, regenerator, vaporizer, adsorber, generator, condenser, throttle valve, solution pump and solution heat exchanger, outside has high pressure steam passage to be communicated with turbo machine (A), turbo machine (A) also have low pressure steam passage be communicated with generator (2) after generator (2) have condensate line and ft connection again, compressor (B) has refrigerant gas passage to be communicated with decompressor (I) with regenerator (J) through cooler (G), decompressor (I) also has refrigerant gas passage to be communicated with compressor (B) with regenerator (J) through low temperature heat exchanger (D), low temperature heat exchanger (D) also has cryogenic media pipeline and ft connection, and cooler (G) also has heated medium pipeline and ft connection, vaporizer (4) has refrigerant steam channel to be communicated with adsorber (1), adsorber (1) also has dilute solution pipeline to be communicated with generator (2) with solution heat exchanger (7) through solution pump (6), generator (2) also has concentrated solution pipeline to be communicated with adsorber (1) through solution heat exchanger (7), generator (2) also has refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline to be communicated with vaporizer (4) through throttle valve (5), vaporizer (4) also has cryogenic media pipeline and ft connection, adsorber (1) and condenser (3) also have heated medium pipeline and ft connection respectively, compressor, cooler, decompressor, low temperature heat exchanger and regenerator form compression type reverse circulation system, and vaporizer, adsorber, generator, condenser, throttle valve, solution pump and solution heat exchanger form absorption reverse circulation system, turbo machine provides power to compression type reverse circulation or externally provides power simultaneously, turbo machine 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 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 (B) refrigerant gas passage to be communicated with decompressor (I) through cooler (G) and regenerator (J) to be adjusted to compressor (B) and to have refrigerant gas passage to be communicated with the second compressor (E) through cooler (G), second compressor (E) has refrigerant gas passage to be communicated with decompressor (I) with regenerator (J) through cooler (G) again, forms combined cycle energy supplying system.
17. combined cycle energy supplying systems, formed primarily of turbo machine, compressor, cooler, vaporizer, decompressor, low temperature heat exchanger, adsorber, generator, condenser, throttle valve, solution pump and solution heat exchanger, outside has high pressure steam passage to be communicated with turbo machine (A), turbo machine (A) also have low pressure steam passage be communicated with generator (2) after generator (2) have condensate line and ft connection again, compressor (B) has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor (I) again through the finisher (4) that cooler (G) is communicated with vaporizer (4), decompressor (I) also has refrigerant gas passage to be communicated with compressor (B) through low temperature heat exchanger (D), low temperature heat exchanger (D) also has cryogenic media pipeline and ft connection, and cooler (G) also has heated medium pipeline and ft connection, vaporizer (4) also has refrigerant steam channel to be communicated with adsorber (1), adsorber (1) also has dilute solution pipeline to be communicated with generator (2) with solution heat exchanger (7) through solution pump (6), generator (2) also has concentrated solution pipeline to be communicated with adsorber (1) through solution heat exchanger (7), generator (2) also has refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline to be communicated with vaporizer (4) through throttle valve (5), adsorber (1) and condenser (3) also have heated medium pipeline and ft connection respectively, compressor, cooler, vaporizer, decompressor and low temperature heat exchanger form compression type reverse circulation system, and vaporizer, adsorber, generator, condenser, throttle valve, solution pump and solution heat exchanger form absorption reverse circulation system, turbo machine provides power to compression type reverse circulation or externally provides power simultaneously, turbo machine 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 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 (B) to have refrigerant gas passage to be communicated with decompressor (I) to be again adjusted to compressor (B) through the finisher (4) that cooler (G) is communicated with vaporizer (4) and have refrigerant gas passage to have refrigerant gas passage to be communicated with the second compressor (E) again through the finisher (4) that cooler (G) is communicated with vaporizer (4), second compressor (E) also has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor (I) again through the finisher (4) that cooler (G) is communicated with vaporizer (4), form combined cycle energy supplying system.
19. combined cycle energy supplying systems, formed primarily of turbo machine, compressor, cooler, vaporizer, regenerator, decompressor, low temperature heat exchanger, adsorber, generator, condenser, throttle valve, solution pump and solution heat exchanger, outside has high pressure steam passage to be communicated with turbo machine (A), turbo machine (A) also have low pressure steam passage be communicated with generator (2) after generator (2) have condensate line and ft connection again, compressor (B) has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor (I) through regenerator (J) again through the finisher (4) that cooler (G) is communicated with vaporizer (4), decompressor (I) also has refrigerant gas passage to be communicated with compressor (B) with regenerator (J) through low temperature heat exchanger (D), low temperature heat exchanger (D) also has cryogenic media pipeline and ft connection, and cooler (G) also has heated medium pipeline and ft connection, vaporizer (4) also has refrigerant steam channel to be communicated with adsorber (1), adsorber (1) also has dilute solution pipeline to be communicated with generator (2) with solution heat exchanger (7) through solution pump (6), generator (2) also has concentrated solution pipeline to be communicated with adsorber (1) through solution heat exchanger (7), generator (2) also has refrigerant steam channel to be communicated with condenser (3), condenser (3) also has cryogen liquid pipeline to be communicated with vaporizer (4) through throttle valve (5), adsorber (1) and condenser (3) also have heated medium pipeline and ft connection respectively, compressor, cooler, vaporizer, regenerator, decompressor and low temperature heat exchanger form compression type reverse circulation system, and vaporizer, adsorber, generator, condenser, throttle valve, solution pump and solution heat exchanger form absorption reverse circulation system, turbo machine provides power to compression type reverse circulation or externally provides power simultaneously, turbo machine 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 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 (B) refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor (I) through regenerator (J) again through the finisher (4) that cooler (G) is communicated with vaporizer (4) to be adjusted to compressor (B) and to have refrigerant gas passage to have refrigerant gas passage to be communicated with the second compressor (E) again through the finisher (4) that cooler (G) is communicated with vaporizer (4), second compressor (E) also has refrigerant gas passage to have refrigerant gas passage to be communicated with decompressor (I) through regenerator (J) again through the finisher (4) that cooler (G) is communicated with vaporizer (4), 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 second generator, second throttle, second solution pump and the second solution heat exchanger, adsorber (1) is set up dilute solution pipeline and is communicated with the second generator (9) with the second solution heat exchanger (12) through the second solution pump (11), second generator (9) also has concentrated solution pipeline to be communicated with adsorber (1) through the second solution heat exchanger (12), had by generator (2) refrigerant steam channel to be communicated with condenser (3) to be adjusted to generator (2) have refrigerant steam channel be communicated with the second generator (9) after the second generator (9) have cryogen liquid pipeline to be communicated with condenser (3) through second throttle (10) again, second generator (9) also has refrigerant steam channel to be communicated with condenser (3), 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 second generator, second throttle and the second solution heat exchanger, had by adsorber (1) dilute solution pipeline to be communicated with generator (2) through solution pump (6) and solution heat exchanger (7) to be adjusted to adsorber (1) and to have dilute solution pipeline through solution pump (6), solution heat exchanger (7) is communicated with generator (2) with the second solution heat exchanger (12), had by generator (2) concentrated solution pipeline to be communicated with adsorber (1) through solution heat exchanger (7) to be adjusted to generator (2) and to have concentrated solution pipeline to be communicated with the second generator (9) through the second solution heat exchanger (12), second generator (9) has concentrated solution pipeline to be communicated with adsorber (1) through solution heat exchanger (7) again, had by generator (2) refrigerant steam channel to be communicated with condenser (3) to be adjusted to generator (2) have refrigerant steam channel be communicated with the second generator (9) after the second generator (9) have cryogen liquid pipeline to be communicated with condenser (3) through second throttle (10) again, second generator (9) also has refrigerant steam channel to be communicated with condenser (3), 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 second generator, second throttle, second solution pump and the second solution heat exchanger, had by adsorber (1) dilute solution pipeline to be communicated with generator (2) through solution pump (6) and solution heat exchanger (7) to be adjusted to adsorber (1) and to have dilute solution pipeline to be communicated with the second generator (9) with solution heat exchanger (7) through solution pump (6), second generator (9) has concentrated solution pipeline to be communicated with generator (2) with the second solution heat exchanger (12) through the second solution pump (11) again, had by generator (2) concentrated solution pipeline to be communicated with adsorber (1) through solution heat exchanger (7) to be adjusted to generator (2) and to have concentrated solution pipeline to be communicated with adsorber (1) with solution heat exchanger (7) through the second solution heat exchanger (12), had by generator (2) refrigerant steam channel to be communicated with condenser (3) to be adjusted to generator (2) have refrigerant steam channel be communicated with the second generator (9) after the second generator (9) have cryogen liquid pipeline to be communicated with condenser (3) through second throttle (10) again, second generator (9) also has refrigerant steam channel to be communicated with condenser (3), form combined cycle energy supplying system.
24. combined cycle energy supplying systems, in arbitrary combined cycle energy supplying system according to claim 21, increase by the 3rd generator, 3rd throttle valve, 3rd solution pump and the 3rd solution heat exchanger, adsorber (1) 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 adsorber (1) through the 3rd solution heat exchanger (16), had by second generator (9) refrigerant steam channel to be communicated with condenser (3) to be adjusted to the second generator (9) 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 (3) through the 3rd throttle valve (14) again, 3rd generator (13) also has refrigerant steam channel to be communicated with condenser (3), form combined cycle energy supplying system.
25. combined cycle energy supplying systems, in arbitrary combined cycle energy supplying system according to claim 22, increase by the 3rd generator, 3rd throttle valve and the 3rd solution heat exchanger, adsorber (1) there is dilute solution pipeline through solution pump (6), solution heat exchanger (7) and the second solution heat exchanger (12) are communicated with generator (2) and are adjusted to adsorber (1) and have dilute solution pipeline through solution pump (6), solution heat exchanger (7), 3rd solution heat exchanger (16) is communicated with generator (2) with the second solution heat exchanger (12), had by second generator (9) concentrated solution pipeline to be communicated with adsorber (1) through solution heat exchanger (7) to be adjusted to the second generator (9) 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 adsorber (1) through solution heat exchanger (7) again, had by second generator (9) refrigerant steam channel to be communicated with condenser (3) to be adjusted to the second generator (9) 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 (3) through the 3rd throttle valve (14) again, 3rd generator (13) also has refrigerant steam channel to be communicated with condenser (3), form combined cycle energy supplying system.
26. combined cycle energy supplying systems, in arbitrary combined cycle energy supplying system according to claim 23, increase by the 3rd generator, 3rd throttle valve, 3rd solution pump and the 3rd solution heat exchanger, had by adsorber (1) dilute solution pipeline to be communicated with the second generator (9) through solution pump (6) and solution heat exchanger (7) to be adjusted to adsorber (1) and to have dilute solution pipeline to be communicated with the 3rd generator (13) with solution heat exchanger (7) through solution pump (6), 3rd generator (13) has concentrated solution pipeline to be communicated with the second generator (9) with the 3rd solution heat exchanger (16) through the 3rd solution pump (15) again, had by generator (2) concentrated solution pipeline to be communicated with adsorber (1) through the second solution heat exchanger (12) and solution heat exchanger (7) to be adjusted to generator (2) and to have concentrated solution pipeline through the second solution heat exchanger (12), 3rd solution heat exchanger (16) is communicated with adsorber (1) with solution heat exchanger (7), had by second generator (9) refrigerant steam channel to be communicated with condenser (3) to be adjusted to the second generator (9) 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 (3) through the 3rd throttle valve (14) again, 3rd generator (13) also has refrigerant steam channel to be communicated with condenser (3), form combined cycle energy supplying system.
27. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 24-26, there is by second generator (9) cryogen liquid pipeline to be communicated with condenser (3) through second throttle (10) to be adjusted to the second generator (9) and to have cryogen liquid pipeline to be communicated with condenser (3) with second throttle (10) through the 3rd generator (13), form combined cycle energy supplying system.
28. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-20, increase by the second generator, second solution pump, second solution heat exchanger and the second adsorber, turbo machine (A) is had low pressure steam passage be communicated with generator (2) after generator (2) have again condensate line and ft connection be adjusted to turbo machine (A) have low pressure steam passage be communicated with generator (2) and the second generator (9) successively after the second generator (9) have condensate line and ft connection again, being had by vaporizer (4) refrigerant steam channel to be communicated with adsorber (1) to be adjusted to vaporizer (4) has refrigerant steam channel to be communicated with the second adsorber (17), second adsorber (17) also has dilute solution pipeline to be communicated with the second generator (9) with the second solution heat exchanger (12) through the second solution pump (11), second generator (9) also has concentrated solution pipeline to be communicated with the second adsorber (17) through the second solution heat exchanger (12), second generator (9) also has refrigerant steam channel to be communicated with adsorber (1), second adsorber (17) also has heated medium pipeline and ft connection, form combined cycle energy supplying system.
29. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-27, increase heat exchanger, the rear heat exchange (8) that being had by generator (2) condensate line and ft connection to be adjusted to generator (2) has condensate line to be communicated with heat exchanger (8) has condensate line and ft connection again, heat exchanger (8) also has heated medium pipeline and ft connection, forms combined cycle energy supplying system.
30. combined cycle energy supplying systems, in arbitrary combined cycle energy supplying system according to claim 28, increase heat exchanger, the rear heat exchange (8) that being had by second generator (9) condensate line and ft connection to be adjusted to the second generator (9) has condensate line to be communicated with heat exchanger (8) has condensate line and ft connection again, heat exchanger (8) also has heated medium pipeline and ft connection, forms combined cycle energy supplying system.
31. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-30, low pressure steam passage is had by turbo machine (A) to be communicated with generator (2) to be adjusted to turbo machine (A) passage that draws gas to be communicated with generator (2), turbo machine (A) sets up exhaust steam passage and ft connection, forms combined cycle energy supplying system.
32. combined cycle energy supplying systems, in the arbitrary combined cycle energy supplying system described in claim 1-31, increase working machine, turbo machine (A) provides power to working machine (K) and compressor (B) simultaneously, forms combined cycle energy supplying system.
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CN106052175A (en) * 2016-05-27 2016-10-26 中石化宁波工程有限公司 Energy-saving composite refrigerating device and refrigerating method
CN106225314A (en) * 2016-04-29 2016-12-14 李华玉 3rd class thermal drivers compression heat pump
CN106352595A (en) * 2015-12-30 2017-01-25 李华玉 First-type thermally driven compression-absorption heat pump
WO2021072993A1 (en) * 2019-10-17 2021-04-22 李华玉 Single-working-medium combined cycle heat pump device

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CN106352595A (en) * 2015-12-30 2017-01-25 李华玉 First-type thermally driven compression-absorption heat pump
CN106225314A (en) * 2016-04-29 2016-12-14 李华玉 3rd class thermal drivers compression heat pump
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