CN111878331A - Supercritical CO2 and air combined cycle solar power generation system and method - Google Patents

Supercritical CO2 and air combined cycle solar power generation system and method Download PDF

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Publication number
CN111878331A
CN111878331A CN202010907696.1A CN202010907696A CN111878331A CN 111878331 A CN111878331 A CN 111878331A CN 202010907696 A CN202010907696 A CN 202010907696A CN 111878331 A CN111878331 A CN 111878331A
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air
carbon dioxide
heat
communicated
outlet
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CN111878331B (en
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高炜
张一帆
张磊
吴帅帅
乔永强
张纯
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Xian Thermal Power Research Institute Co Ltd
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Xian Thermal Power Research Institute Co Ltd
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F03—MACHINES OR ENGINES FOR LIQUIDS; WIND, SPRING, OR WEIGHT MOTORS; PRODUCING MECHANICAL POWER OR A REACTIVE PROPULSIVE THRUST, NOT OTHERWISE PROVIDED FOR
    • F03G—SPRING, WEIGHT, INERTIA OR LIKE MOTORS; MECHANICAL-POWER PRODUCING DEVICES OR MECHANISMS, NOT OTHERWISE PROVIDED FOR OR USING ENERGY SOURCES NOT OTHERWISE PROVIDED FOR
    • F03G6/00—Devices for producing mechanical power from solar energy
    • F03G6/02—Devices for producing mechanical power from solar energy using a single state working fluid
    • F03G6/04—Devices for producing mechanical power from solar energy using a single state working fluid gaseous
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01D—NON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
    • F01D15/00—Adaptations of machines or engines for special use; Combinations of engines with devices driven thereby
    • F01D15/08—Adaptations for driving, or combinations with, pumps
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K17/00—Using steam or condensate extracted or exhausted from steam engine plant
    • F01K17/06—Returning energy of steam, in exchanged form, to process, e.g. use of exhaust steam for drying solid fuel or plant
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K25/00—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for
    • F01K25/08—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using special vapours
    • F01K25/10—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using special vapours the vapours being cold, e.g. ammonia, carbon dioxide, ether
    • F01K25/103—Carbon dioxide
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K27/00—Plants for converting heat or fluid energy into mechanical energy, not otherwise provided for
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K7/00—Steam engine plants characterised by the use of specific types of engine; Plants or engines characterised by their use of special steam systems, cycles or processes; Control means specially adapted for such systems, cycles or processes; Use of withdrawn or exhaust steam for feed-water heating
    • F01K7/32—Steam engine plants characterised by the use of specific types of engine; Plants or engines characterised by their use of special steam systems, cycles or processes; Control means specially adapted for such systems, cycles or processes; Use of withdrawn or exhaust steam for feed-water heating the engines using steam of critical or overcritical pressure
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F03—MACHINES OR ENGINES FOR LIQUIDS; WIND, SPRING, OR WEIGHT MOTORS; PRODUCING MECHANICAL POWER OR A REACTIVE PROPULSIVE THRUST, NOT OTHERWISE PROVIDED FOR
    • F03G—SPRING, WEIGHT, INERTIA OR LIKE MOTORS; MECHANICAL-POWER PRODUCING DEVICES OR MECHANISMS, NOT OTHERWISE PROVIDED FOR OR USING ENERGY SOURCES NOT OTHERWISE PROVIDED FOR
    • F03G6/00—Devices for producing mechanical power from solar energy
    • F03G6/06—Devices for producing mechanical power from solar energy with solar energy concentrating means
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24S—SOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
    • F24S20/00—Solar heat collectors specially adapted for particular uses or environments
    • F24S20/20—Solar heat collectors for receiving concentrated solar energy, e.g. receivers for solar power plants
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E10/00—Energy generation through renewable energy sources
    • Y02E10/40—Solar thermal energy, e.g. solar towers
    • Y02E10/46—Conversion of thermal power into mechanical power, e.g. Rankine, Stirling or solar thermal engines
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00—Combustion technologies with mitigation potential
    • Y02E20/16—Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)

Abstract

A supercritical CO2 and air combined cycle solar power generation system, a supercritical CO2 and air combined cycle solar power generation system and a method thereof, comprises a gas compressor, wherein the gas compressor is sequentially connected with an air heat regenerator, an air turbine, a solar heat collector and an air-carbon dioxide heat exchanger, the outlet of the air-carbon dioxide heat exchanger is communicated with the inlet of the air heat exchanger, and the outlet of the air heat exchanger is communicated with the outside air; the outlet of the carbon dioxide turbine is communicated with the inlet of a carbon dioxide heat regenerator, the outlet of the carbon dioxide heat regenerator is communicated with the inlet of a precooler, the outlet of the precooler is communicated with the inlet of a carbon dioxide compressor, the outlet of the carbon dioxide compressor is communicated with the inlet of the carbon dioxide heat regenerator, the outlet of the carbon dioxide heat regenerator is communicated with the inlet of an air-carbon dioxide heat exchanger, and the outlet of the air-carbon dioxide heat exchanger is communicated with the inlet of the carbon dioxide turbine. The invention has the characteristics of reduced material cost and high power generation efficiency.

Description

Supercritical CO2 and air combined cycle solar power generation system and method
Technical Field
The invention relates to the technical field of solar power generation, in particular to a supercritical CO2 and air combined cycle solar power generation system and method.
Background
Solar energy is an inexhaustible clean energy, and since solar photo-thermal power generation can reach the same high temperature as the solar temperature theoretically, as is well known, the higher the temperature is, the higher the thermal efficiency is, the more the solar photo-thermal power generation is emphasized.
The photothermal power generation needs to convert light energy into heat energy, and then the thermoelectric conversion is realized through the thermodynamic cycle, and at present, among numerous thermodynamic cycles, the supercritical brayton cycle is the most advantageous cycle form. The novel supercritical working media such as carbon dioxide, helium and nitrous oxide have the inherent advantages of high energy density, high heat transfer efficiency, simple system and the like, can greatly improve the heat-power conversion efficiency, reduce the equipment volume and have very high economical efficiency. Especially, after the temperature of the hot end reaches more than 500 ℃, the advantages of the supercritical carbon dioxide Brayton cycle become more and more obvious along with the temperature, and the thermal efficiency of the Brayton cycle gradually increases to the distance from the traditional steam cycle or other working medium cycles.
However, the heat collection temperature of the tower solar energy is not high at present, wherein the material problem accounts for a large part of the reasons, the high-temperature material actually applied to the power generation of the steam turbine set is within 620 ℃ and is far lower than the heat source temperature which can be reached by the solar heat collector, in addition, the solar photo-thermal power generation generally needs to consider heat storage, and the large-scale heat storage device is generally arranged on the ground, so the distances between the heat collector at the tower top and the heat storage device as well as the power generation set are far, and the main steam pressure of the power generation set with high efficiency is also far, so the pipe wall is very thick, if the pipe is made of high-temperature resistant alloy materials and is conveyed for a long distance, the cost is very huge.
Disclosure of Invention
In order to overcome the technical problems, the invention aims to provide a supercritical CO2 and air combined cycle solar power generation system and method, which have the characteristics of material cost reduction and high power generation efficiency.
In order to achieve the purpose, the invention adopts the technical scheme that:
a supercritical CO2 and air combined cycle solar power generation system comprises an air compressor 1, wherein an outlet of the air compressor 1 is communicated with a low-temperature side inlet of an air heat regenerator 2, a low-temperature side outlet of the air heat regenerator 2 is communicated with an inlet of an air turbine 3, an outlet of the air turbine 3 is communicated with an inlet of a solar heat collector 4, an outlet of the solar heat collector 4 is communicated with an air side inlet of an air-carbon dioxide heat exchanger 5, an air side outlet of the air-carbon dioxide heat exchanger 5 is communicated with a high-temperature side inlet of the air heat exchanger 2, and a high-temperature side outlet of the air heat exchanger 2 is communicated with outside air;
the outlet of the carbon dioxide turbine 6 is communicated with the high-temperature side inlet of the carbon dioxide heat regenerator 7, the high-temperature side outlet of the carbon dioxide heat regenerator 7 is communicated with the carbon dioxide side inlet of the precooler 8, the carbon dioxide side outlet of the precooler 8 is communicated with the inlet of the carbon dioxide compressor 9, the outlet of the carbon dioxide compressor 9 is communicated with the low-temperature side inlet of the carbon dioxide heat regenerator 7, the low-temperature side outlet of the carbon dioxide heat regenerator 7 is communicated with the carbon dioxide side inlet of the air-carbon dioxide heat exchanger 5, and the carbon dioxide side outlet of the air-carbon dioxide heat exchanger 5 is communicated with the inlet of the carbon.
A method for a supercritical CO2 and air combined cycle solar power generation system comprises the steps that firstly, an air compressor 1 absorbs air from outside atmosphere to be compressed, then the air is sent to a cold side of an air heat regenerator 2 to absorb heat, the heated compressed air enters an air turbine 3 to expand and do work, the expanded low-pressure air enters a solar heat collector 4 to absorb heat, the air heated to high temperature enters an air-carbon dioxide heat exchanger 5 to release heat, the air after heat release still has high temperature, then enters a hot side of the air heat regenerator 2 to continue heat release, and finally the air is discharged to the outside atmosphere;
the supercritical carbon dioxide cycle is a closed cycle, high-pressure supercritical carbon dioxide which absorbs heat released by high-temperature air in the air-carbon dioxide heat exchanger 5 enters the carbon dioxide turbine 6 to do work and becomes low-pressure supercritical carbon dioxide after expansion work, the low-pressure supercritical carbon dioxide firstly enters the hot side of the carbon dioxide heat regenerator 7 to release waste heat and then enters the precooler 8 to be continuously cooled, the cooled low-pressure low-temperature supercritical carbon dioxide enters the carbon dioxide compressor 9 to be pressurized, the pressurized supercritical carbon dioxide enters the cold side of the carbon dioxide heat regenerator 7 to absorb heat and then enters the air-carbon dioxide heat exchanger 5 to continuously absorb heat, finally the temperature reaches the highest temperature, and finally the cooled low-pressure low-temperature supercritical carbon dioxide enters the carbon dioxide turbine 6 to.
The invention has the beneficial effects that:
according to the supercritical CO2 and air combined cycle solar power generation system, firstly, the exhaust of an air Brayton cycle turbine is used as a heat absorption working medium of a solar heat collector, and the pressure is close to normal pressure, so that the heat collector and a channel material for conveying fluid can be selected and commonly used, and the problem of strength at high temperature is not considered. When the high-temperature hot fluid is conveyed to the energy storage system and the vicinity of the unit, the high-temperature alloy material is selected, so that the material cost can be greatly reduced. In addition, the invention adopts a supercritical carbon dioxide generator set, has the characteristic of small volume and can also reduce the material consumption. In addition, the system adopts the combination of air Brayton cycle and a supercritical carbon dioxide generator set, so that the generating efficiency is higher.
Drawings
FIG. 1 is a schematic structural diagram of the present invention.
The system comprises an air compressor 1, an air heat regenerator 2, an air turbine 3, a solar heat collector 4, an air-carbon dioxide heat exchanger 5, a carbon dioxide turbine 6, a carbon dioxide heat regenerator 7, a precooler 8 and a carbon dioxide compressor 9.
Detailed Description
The present invention will be described in further detail with reference to examples.
Referring to fig. 1, the supercritical CO2 and air combined cycle solar power generation system according to the present invention comprises a compressor 1, an air heat regenerator 2, an air turbine 3, a solar heat collector 4, an air-carbon dioxide heat exchanger 5, a carbon dioxide turbine 6, a carbon dioxide heat regenerator 7, a precooler 8, and a carbon dioxide compressor 9, wherein an inlet of the compressor 1 is communicated with the outside air, an outlet of the compressor 1 is communicated with a low temperature side inlet of the air heat regenerator 2, a low temperature side outlet of the air heat regenerator 2 is communicated with an inlet of the air turbine, an outlet of the air turbine 3 is communicated with an inlet of the solar heat collector 4, an outlet of the solar heat collector 4 is communicated with an air side inlet of the air-carbon dioxide heat exchanger 5, an air side outlet of the air-carbon dioxide heat exchanger 5 is communicated with a high temperature side inlet of, the outlet of the high-temperature side of the air heat exchanger 2 is communicated with the outside air, the outlet of the carbon dioxide turbine 6 is communicated with the inlet of the high-temperature side of the carbon dioxide regenerator 7, the outlet of the high-temperature side of the carbon dioxide regenerator 7 is communicated with the inlet of the carbon dioxide side of the precooler 8, the outlet of the carbon dioxide side of the precooler 8 is communicated with the inlet of the carbon dioxide compressor 9, the outlet of the carbon dioxide compressor 9 is communicated with the inlet of the low-temperature side of the carbon dioxide regenerator 7, the outlet of the low-temperature side of the carbon dioxide regenerator 7 is communicated with the inlet of the carbon dioxide side of the air-carbon dioxide heat exchanger 5, and the outlet of.
The system firstly adopts the exhaust of the air Brayton cycle turbine as the heat absorption working medium of the solar heat collector, and the pressure is close to the normal pressure, so that the heat collector and the channel material for conveying fluid can be selected and commonly used, and the problem of strength at high temperature does not need to be considered. When the high-temperature hot fluid is conveyed to the energy storage system and the vicinity of the unit, the high-temperature alloy material is selected, so that the material cost can be greatly reduced. In addition, the invention adopts a supercritical carbon dioxide generator set, has the characteristic of small volume and can also reduce the material consumption. In addition, the system adopts the combination of air Brayton cycle and a supercritical carbon dioxide generator set, so that the generating efficiency is higher.
The specific working process of the invention is as follows:
firstly, an air compressor 1 absorbs air from the outside atmosphere to compress the air, then the air is sent to the cold side of an air heat regenerator 2 to absorb heat, the heated compressed air enters an air turbine 3 to expand and do work, the expanded low-pressure air enters a solar heat collector 4 to absorb heat, the air heated to high temperature enters an air-carbon dioxide heat exchanger 5 to release heat, the air after heat release still has higher temperature, then the air enters the hot side of the air heat regenerator 2 to continue heat release, and finally the air is discharged into the outside atmosphere;
the supercritical carbon dioxide cycle is a closed cycle, high-pressure supercritical carbon dioxide which absorbs heat released by high-temperature air in the air-carbon dioxide heat exchanger 5 enters the carbon dioxide turbine 6 to do work and becomes low-pressure supercritical carbon dioxide after expansion work, the low-pressure supercritical carbon dioxide firstly enters the hot side of the carbon dioxide heat regenerator 7 to release waste heat and then enters the precooler 8 to be continuously cooled, the cooled low-pressure low-temperature supercritical carbon dioxide enters the carbon dioxide compressor 9 to be pressurized, the pressurized supercritical carbon dioxide enters the cold side of the carbon dioxide heat regenerator 7 to absorb heat and then enters the air-carbon dioxide heat exchanger 5 to continuously absorb heat, finally the temperature reaches the highest temperature, and finally the cooled low-pressure low-temperature supercritical carbon dioxide enters the carbon dioxide turbine 6 to.
The above-mentioned embodiments, objects, technical solutions and advantages of the present invention are further described in detail, it should be understood that the above-mentioned embodiments are only illustrative of the present invention and are not intended to limit the present invention, and any modifications, equivalents, improvements and the like made within the spirit and principle of the present invention should be included in the protection scope of the present invention.

Claims (2)

1. A supercritical CO2 and air combined cycle solar power generation system is characterized by comprising a compressor (1), wherein an outlet of the compressor (1) is communicated with a low-temperature side inlet of an air regenerator (2), a low-temperature side outlet of the air regenerator (2) is communicated with an inlet of an air turbine (3), an outlet of the air turbine (3) is communicated with an inlet of a solar heat collector (4), an outlet of the solar heat collector (4) is communicated with an air side inlet of an air-carbon dioxide heat exchanger (5), an air side outlet of the air-carbon dioxide heat exchanger (5) is communicated with a high-temperature side inlet of the air heat exchanger (2), and a high-temperature side outlet of the air heat exchanger (2) is communicated with outside air;
the outlet of the carbon dioxide turbine (6) is communicated with the high-temperature side inlet of the carbon dioxide regenerator (7), the high-temperature side outlet of the carbon dioxide regenerator (7) is communicated with the carbon dioxide side inlet of the precooler (8), the carbon dioxide side outlet of the precooler (8) is communicated with the inlet of the carbon dioxide compressor (9), the outlet of the carbon dioxide compressor (9) is communicated with the low-temperature side inlet of the carbon dioxide regenerator (7), the low-temperature side outlet of the carbon dioxide regenerator (7) is communicated with the carbon dioxide side inlet of the air-carbon dioxide heat exchanger (5), and the carbon dioxide side outlet of the air-carbon dioxide heat exchanger (5) is communicated with the inlet of the carbon dioxide turbine (6).
2. The method of claim 1, wherein the supercritical CO2 and air combined cycle solar power system,
firstly, an air compressor (1) absorbs air from the outside atmosphere to compress the air, then the air is sent to the cold side of an air heat regenerator (2) to absorb heat, the heated compressed air enters an air turbine (3) to expand to do work, the expanded low-pressure air enters a solar heat collector (4) to absorb heat, the air heated to high temperature enters an air-carbon dioxide heat exchanger (5) to release heat, the air after releasing heat still has high temperature, then the air enters the hot side of the air heat regenerator (2) to continue releasing heat, and finally the air is discharged into the outside atmosphere;
the supercritical carbon dioxide cycle is a closed cycle, high-pressure supercritical carbon dioxide absorbing heat released by high-temperature air in an air-carbon dioxide heat exchanger (5) enters a carbon dioxide turbine (6) to do work, the high-pressure supercritical carbon dioxide is expanded to become low-pressure supercritical carbon dioxide after doing work, the low-pressure supercritical carbon dioxide firstly enters a hot side of a carbon dioxide heat regenerator (7) to release waste heat, then enters a precooler (8) to be continuously cooled, the cooled low-pressure low-temperature supercritical carbon dioxide enters a carbon dioxide compressor (9) to be pressurized, the pressurized supercritical carbon dioxide enters a cold side of the carbon dioxide heat regenerator (7) to absorb heat, then enters the air-carbon dioxide heat exchanger (5) to continuously absorb heat, finally the highest temperature is reached, and finally the carbon dioxide turbine (6) completes final cycle.
CN202010907696.1A 2020-09-02 2020-09-02 Supercritical carbon dioxide and air combined cycle solar power generation system and method Active CN111878331B (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112554979A (en) * 2020-11-19 2021-03-26 西安交通大学 Photovoltaic and photo-thermal coupling power generation system
CN112762424A (en) * 2021-01-07 2021-05-07 中国船舶重工集团新能源有限责任公司 Solar thermoelectric coupling system based on combination of heat storage and compression heat pump and operation method thereof

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CN107313904A (en) * 2017-05-27 2017-11-03 集美大学 Solar air carbon dioxide association circulating power generation system
CN109763948A (en) * 2018-12-25 2019-05-17 西安交通大学 A kind of supercritical carbon dioxide solar heat power generation system and operation method
CN111075526A (en) * 2019-12-14 2020-04-28 西安交通大学 Supercritical carbon dioxide Brayton cycle thermal power generation system and process
EP3696378A1 (en) * 2019-02-15 2020-08-19 Zhejiang University Turbine and brayton cycle including same
CN212958971U (en) * 2020-09-02 2021-04-13 西安热工研究院有限公司 Supercritical CO2 and air Brayton combined cycle solar power generation system

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CN104405599A (en) * 2014-09-24 2015-03-11 西安交通大学 Fuel gas-supercritical carbon dioxide united power electricity generation system utilizing solar energy
CN104929709A (en) * 2015-04-16 2015-09-23 集美大学 Solar moist air circulating electricity-water cogeneration system
CN104896764A (en) * 2015-04-29 2015-09-09 南京瑞柯徕姆环保科技有限公司 Solar thermal power generation method and device
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112554979A (en) * 2020-11-19 2021-03-26 西安交通大学 Photovoltaic and photo-thermal coupling power generation system
CN112554979B (en) * 2020-11-19 2021-11-19 西安交通大学 Photovoltaic and photo-thermal coupling power generation system
CN112762424A (en) * 2021-01-07 2021-05-07 中国船舶重工集团新能源有限责任公司 Solar thermoelectric coupling system based on combination of heat storage and compression heat pump and operation method thereof
CN112762424B (en) * 2021-01-07 2022-10-18 中国船舶重工集团新能源有限责任公司 Solar thermoelectric coupling system based on combination of heat storage and compression heat pump and operation method thereof

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