Movatterモバイル変換


[0]ホーム

URL:


CN111102142A - A tower solar thermal power generation system based on supercritical fluid - Google Patents

A tower solar thermal power generation system based on supercritical fluid
Download PDF

Info

Publication number
CN111102142A
CN111102142ACN201911221220.6ACN201911221220ACN111102142ACN 111102142 ACN111102142 ACN 111102142ACN 201911221220 ACN201911221220 ACN 201911221220ACN 111102142 ACN111102142 ACN 111102142A
Authority
CN
China
Prior art keywords
heat
supercritical
power generation
temperature
thermal power
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201911221220.6A
Other languages
Chinese (zh)
Inventor
郭鹏程
刘寿春
颜建国
王军辉
郑小波
孙帅辉
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Xian University of Technology
Original Assignee
Xian University of Technology
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Xian University of TechnologyfiledCriticalXian University of Technology
Priority to CN201911221220.6ApriorityCriticalpatent/CN111102142A/en
Publication of CN111102142ApublicationCriticalpatent/CN111102142A/en
Pendinglegal-statusCriticalCurrent

Links

Images

Classifications

Landscapes

Abstract

Translated fromChinese

本发明公开了一种基于超临界流体的塔式太阳能热发电系统,包括三个子系统和发电机,子系统分别为集热系统、传热储热系统和热力循环系统;集热系统包括布置于光照充足区域的定日镜场,和用于吸收来自定日镜场反射的太阳光的集热器;传热储热系统由集热器、高温储热器、热交换器、低温储热器和进料泵通过管道依次首尾相连组成,传热储热系统内的工质为超临界碳氢化合物;热力循环系统由热交换器、汽轮机、冷凝器和压缩机通过管道依次首尾相连组成,热力循环系统中的循环工质为超临界CO2,汽轮机与发电机同轴相连。本发明所提出的技术方案能提高塔式太阳能热电站的能量转换效率,提升系统的安全稳定性,并降低发电成本。

Figure 201911221220

The invention discloses a tower type solar thermal power generation system based on supercritical fluid, comprising three subsystems and a generator. The subsystems are respectively a heat collection system, a heat transfer and heat storage system and a thermodynamic circulation system; A field of heliostats in a well-lit area, and a collector for absorbing sunlight reflected from the field of heliostats; a heat transfer and heat storage system consists of a collector, a high-temperature storage, a heat exchanger, and a low-temperature storage The heat transfer and heat storage system is composed of supercritical hydrocarbons; the thermal cycle system is composed of heat exchangers, steam turbines, condensers and compressors connected end to end through pipelines. The circulating working medium in the circulating system is supercritical CO2 , and the steam turbine and the generator are coaxially connected. The technical scheme proposed by the present invention can improve the energy conversion efficiency of the tower solar thermal power station, improve the safety and stability of the system, and reduce the cost of power generation.

Figure 201911221220

Description

Tower type solar thermal power generation system based on supercritical fluid
Technical Field
The invention belongs to the technical field of solar thermal power generation, and relates to a tower type solar thermal power generation system based on supercritical fluid.
Background
Solar energy utilization techniques include photovoltaic power generation, thermal power generation, and other forms of heat utilization techniques. Among these technologies, a solar thermal power generation technology (also referred to as a photothermal power generation technology) has an extremely important meaning. Solar thermal power generation is a conversion process of light-heat-electricity, and firstly, direct radiation energy of solar energy is gathered on a heat absorber to heat transfer fluid in the heat absorber, so that the light energy is converted into heat energy. Then, high-temperature and high-pressure steam is generated by utilizing the heat energy of the heat transfer fluid, and the conversion from the heat energy to the electric energy is realized through a steam turbine generator set. The solar thermal power generation technology has the unique advantages that other new energy sources are difficult to replace. Firstly, the solar thermal generator set can keep continuous and stable operation by configuring the heat storage system and is not influenced by illumination change, and if the capacity of the heat storage system is large enough, the solar thermal generator set can realize 24-hour continuous power generation. And secondly, the solar thermal power generator unit can rapidly adjust the output of the steam turbine generator unit according to the requirement of the power load of the power grid, namely participating in primary frequency modulation and secondary frequency modulation of the power grid. And thirdly, the solar thermal power generation has stable power output and good regulation performance, is suitable for the concentrated large-scale construction of a solar power generation base, and replaces a coal-fired unit as a main unit in a power system. Therefore, the solar thermal power generation technology can play an extremely important role in the future world energy structure, especially in the future national energy structure.
The solar photo-thermal power generation mainly comprises the forms of groove type, tower type, linear Fresnel type, disc type and the like. Among the technical forms, the tower type technology has the advantages of high light condensation multiple, high heat collection temperature, high photo-thermal conversion efficiency and the like, and is a mainstream technology of large-scale solar photo-thermal power generation. At present, the mainstream technical route of tower type solar thermal power generation is as follows: reflecting sunlight to an absorber arranged at the top of the high tower by utilizing a plurality of directional mirrors for independently tracking the sunlight to heat the heat transfer fluid in the absorber; in the heat exchanger, the heat transfer fluid transfers energy to water to generate high-temperature high-pressure superheated steam; the superheated steam drives the turbine to drive the generator, thereby producing electricity.
The tower solar technology has higher requirements on the working temperature, the operating pressure, the safety (flammability, explosiveness, toxicity and the like), the acquisition cost, the compatibility with pipeline materials and the like of the heat transfer fluid. In the current tower type solar photo-thermal power station, the heat transfer fluid which is most widely applied is high-temperature molten salt. Although molten salt is widely used as a heat transfer and storage medium by virtue of the advantages of low use temperature, low cost, easy obtainment and the like, the molten salt also has the problems of pipe blockage risk caused by high solidification point, leakage risk caused by strong corrosion at high temperature, complex heat preservation and the like. Therefore, a heat transfer fluid with better comprehensive performance is continuously searched, and the method has important significance for promoting the safety and stability of the tower type solar power station. In recent years, due to the development of supercritical technology, supercritical fluid becomes a novel heat transfer fluid, has good application in many fields, and has wide application prospect in tower type solar power station technology.
At present, the conventional thermal power generation technology is still utilized in the 'heat-electricity' conversion link in a solar tower power station, namely, Rankine cycle is utilized to realize conversion from heat energy to mechanical energy and then to electric energy. However, the efficiency of the rankine cycle is unsatisfactory due to the limitations of the steam parameters. Therefore, researchers are continuously exploring new and efficient thermodynamic cycle systems to improve the conversion efficiency of energy. In recent years, supercritical CO2 Brayton cycle gradually becomes a research hotspot, and the phase state of a working medium does not change in the cycle, so that the compression work is greatly reduced, and the cycle efficiency is remarkably improved.
Therefore, the invention provides a novel tower type solar thermal power generation system based on supercritical fluid.
Disclosure of Invention
The invention aims to provide a tower type solar thermal power generation system based on supercritical fluid, which solves the problems that in the prior art, a heat transfer medium in a heat transfer and heat storage system has the risk of pipe blockage due to high solidification point, leakage due to strong corrosion at high temperature and complex and difficult heat preservation.
The technical scheme adopted by the invention is that the tower type solar thermal power generation system based on the supercritical fluid comprises three subsystems and a generator, wherein the subsystems are respectively a heat collection system, a heat transfer and storage system and a thermal circulation system; the heat collecting system comprises a heliostat field arranged in a region with sufficient illumination and a heat collector used for absorbing sunlight reflected from the heliostat field; the heat transfer and storage system is formed by sequentially connecting a heat collector, a high-temperature heat reservoir, a heat exchanger, a low-temperature heat reservoir and a feed pump end to end through pipelines, and a working medium in the heat transfer and storage system is a supercritical hydrocarbon; the thermodynamic cycle system consists of heat exchanger, steam turbine, condenser and compressor connected successively in end-to-end mode via pipeline, and the circulating medium in the thermodynamic cycle system is supercritical CO2And the steam turbine is connected with the generator in a driving way.
The invention is also characterized in that:
the cycle operation process of the heat transfer and storage system is as follows: the supercritical hydrocarbon absorbs solar light energy gathered by a heliostat field in the heat collector, then the high-temperature heat reservoir stores the high-temperature supercritical hydrocarbon which flows out after absorbing heat in the heat collector, then the high-temperature hydrocarbon in the heat exchanger transfers the energy to a circulating working medium in a thermodynamic cycle system, then the low-temperature heat reservoir stores the low-temperature supercritical hydrocarbon which flows out after exchanging heat by the heat exchanger, and the feed pump boosts the pressure of the low-temperature supercritical hydrocarbon and then conveys the low-temperature supercritical hydrocarbon into the heat collector to absorb solar energy again.
The circulation operation process of the thermodynamic circulation system comprises the following steps: high temperature supercritical hydrocarbons in heat exchangers transferring energy to supercritical CO in thermodynamic cycle systems2So as to make supercritical CO2The temperature and the pressure are increased, then the turbine blade is pushed to do work, and the supercritical CO is converted into the CO2The carried heat energy is converted into mechanical energy of a steam turbine, the steam turbine drives a generator which is coaxially connected with the steam turbine to generate electricity, and a condenser arranged at the outlet of the steam turbine is used for converting the supercritical CO which does work2Condensing at constant pressure, and then subjecting the supercritical CO to a compressor disposed after the condenser2The compression is carried out in an isentropic way, so that the pressure is increased and the heat is absorbed again in the heat exchanger.
The temperature range of the low-temperature heat reservoir is below 400 ℃, and the temperature range of the high-temperature heat reservoir is above 400 ℃.
The heat collector is a heat absorption tower.
The heat absorption tower is a steel structure system with a frame-support structure.
The heat absorption tower is a concrete structure system with a frame-shear wall structure or a single-cylinder structure.
The invention has the beneficial effects that:
1. the novel tower type solar photo-thermal power generation system provided by the invention has higher energy conversion efficiency and better safety and stability, and compared with the traditional Rankine cycle, the novel tower type solar photo-thermal power generation system has supercritical CO2The efficiency of the Brayton cycle is obviously improved, the maximum thermal efficiency can reach 55 percent and generally can reach more than 45 percent, and the safety of the thermodynamic cycle system is improved and the service life is prolonged due to the reduction of cycle parameters;
2. the heat transfer capacity of the supercritical hydrocarbon adopted in the invention is stronger than that of molten salt, and the specific heat of the supercritical hydrocarbon is also larger than that of the molten salt, which is beneficial to enhancing the energy transfer capacity of the heat transfer and storage system;
3. the system has lower power generation cost, the heat transfer and storage system and the thermodynamic cycle system are compact due to the improvement of power density, the sizes of key equipment such as a heat storage device, a heat exchanger, a steam turbine and the like can be reduced, and the supercritical CO is used for generating the heat energy2And supercritical hydrocarbon are easy to obtain, and the cost of the working medium can be reduced.
Drawings
FIG. 1 is a schematic structural diagram of a supercritical fluid-based tower-type solar thermal power generation system according to the present invention;
FIG. 2 is a schematic structural diagram of a heat collecting system in a supercritical fluid-based tower-type solar thermal power generation system according to the present invention;
FIG. 3 is a schematic structural diagram of a heat transfer and storage system in a supercritical fluid-based tower-type solar thermal power generation system according to the present invention;
fig. 4 is a schematic structural diagram of a thermodynamic cycle system in a supercritical fluid-based tower-type solar thermal power generation system according to the present invention.
In the figure, 1, a heliostat field, 2, a heat collector, 3, a feed pump, 4, a low-temperature heat reservoir, 5, supercritical hydrocarbons, 6, a high-temperature heat reservoir, 7, a heat exchanger, 8, a compressor, 9, a condenser and 10,supercritical CO211, a steam turbine and 12 a generator.
Detailed Description
The present invention will be described in detail below with reference to the accompanying drawings and specific embodiments.
The invention relates to a tower type solar thermal power generation system based on supercritical fluid, which comprises three subsystems and agenerator 12, wherein the subsystems are a heat collecting system, a heat transfer and storage system and a thermal circulation system respectively, as shown in figures 1 to 4; the heat collection system comprises aheliostat field 1 arranged in a region with sufficient illumination and aheat collector 2 for absorbing sunlight reflected from the heliostat field; the heat transfer and storage system is composed of aheat collector 2, a high-temperature heat reservoir 6, aheat exchanger 7, a low-temperature heat reservoir 4 and afeed pump 3 which are sequentially connected end to end through pipelines, and a working medium in the heat transfer and storage system is asupercritical hydrocarbon 5; the thermodynamic cycle system is composed of aheat exchanger 7, asteam turbine 11, acondenser 9 and acompressor 8 which are sequentially connected end to end through pipelines, and the circulating working medium in the thermodynamic cycle system issupercritical CO210, asteam turbine 11 is coaxially connected with agenerator 12.
The temperature range of the low-temperature heat reservoir 4 is below 400 ℃, the temperature range of the high-temperature heat reservoir 6 is above 400 ℃, and the temperature limit is different with the difference of the heat storage working medium.
As shown in fig. 2, theheat collector 2 is a heat absorption tower. The heat absorption tower belongs to a high-rise structure, the mass of equipment is mainly and intensively arranged at the top, and the requirement on the strength and the rigidity of the heat absorption tower is high, so that a steel structure system or a concrete structure system can be adopted.
The heat absorption tower is a steel structure system with a frame-support structure.
The heat absorption tower is a concrete structure system with a frame-shear wall structure or a single-cylinder structure.
As shown in fig. 3, the cycle operation process of the heat transfer and storage system is as follows: thesupercritical hydrocarbon 5 absorbs solar light energy gathered by theheliostat field 1 in theheat collector 2, then the high-temperature heat reservoir 6 stores the high-temperature supercritical hydrocarbon which flows out after absorbing heat in theheat collector 2, then the high-temperature hydrocarbon in theheat exchanger 7 transfers energy to a circulating working medium in a thermodynamic circulating system, then the low-temperature heat reservoir 4 stores the low-temperature supercritical hydrocarbon which exchanges heat through theheat exchanger 7, and thefeeding pump 3 boosts the pressure of the low-temperature supercritical hydrocarbon and then conveys the low-temperature supercritical hydrocarbon into theheat collector 2 to absorb solar energy again.
As shown in fig. 4, the cycle operation process of the thermodynamic cycle system is as follows: high temperature supercritical hydrocarbons inheat exchanger 7 transfer energy to supercritical CO in thermodynamic cycle system2So as to make supercritical CO2The temperature and the pressure rise to be in a high-temperature and high-pressure state, the blades of thesteam turbine 11 are pushed to do work, and the supercritical CO is converted into the supercritical CO2The carried heat energy is converted into mechanical energy of asteam turbine 11, thesteam turbine 11 drives agenerator 12 to generate electricity, and acondenser 9 arranged at the outlet of thesteam turbine 11 applies work to the supercritical CO2Is subjected to isobaric condensation, and then to supercritical CO by means of acompressor 8 placed after thecondenser 9210 are isentropically compressed, causing them to rise in pressure and to enter theheat exchanger 7 where they again absorb heat.
The invention relates to a tower type solar thermal power generation system based on supercritical fluid, which comprises the following working processes:
firstly, in a heat collection system, sunlight is reflected by aheliostat field 1 and then reaches aheat collector 2, then theheat collector 2 collects high-heat sunlight for pre-storage of energy, and the construction of a heat absorption high tower is designed and constructed according to specific requirements. Generally, steel structure towers are more expensive than concrete towers, and the difference is larger as the height of the tower increases. However, in some areas in northwest of China, cold areas in winter and windy areas, concrete materials are difficult to obtain, concrete construction is difficult, and a steel structure is adopted instead of a better scheme. When a concrete structure system is adopted, a frame-shear wall structure or a single-cylinder structure is adopted, the single-cylinder structure is low in manufacturing cost and relatively high in construction speed. When a steel structure system is used, a frame-support structure is adopted, and if not necessary, the structure is not recommended to be closed by a profiled steel sheet.
Secondly, in the heat transfer and heat storage system, low-temperature liquid hydrocarbon 5 is sent to the towertop heat collector 2 by thefeed pump 3 and absorbs the light energy gathered by theheliostat field 1. The heat transfer capacity of the low-temperature liquid hydrocarbon is stronger than that of molten salt, the specific heat of the low-temperature liquid hydrocarbon is larger than that of the molten salt, the energy transfer capacity of a heat transfer and storage system is enhanced, the compatibility of the supercritical hydrocarbon to metal materials is better, and the corrosion to the materials can be reduced.
The high-temperature supercritical hydrocarbon formed after the low-temperature liquid hydrocarbon absorbs heat enters theheat exchanger 7 for energy exchange and heat transfer. Theheat exchanger 7 is a device capable of realizing energy exchange between a heat absorbing medium and a heat storage medium, and between the heat storage medium and a working medium, wherein the energy exchange between the heat absorbing medium and the heat storage medium is realized by energy storage, and the energy exchange between the heat storage medium and the working medium is realized by energy storage and release.
Then the hightemperature heat storage 6 stores the surplus heat, the hightemperature heat storage 6 has the characteristics of high temperature resistance and high pressure resistance, and the heat required by the low temperature liquid hydrocarbon entering theheat exchanger 7 for heat exchange can be supplied alternately for a long time day and night.
Finally, the supercritical CO enters the high-temperature and high-pressure state through heat exchange2The expansion in theturbine 11 pushes theturbine 11 to drive thegenerator 12 to generate electricity. Supercritical CO after work2Condensed by acondenser 9, compressed by acompressor 8 and then processed again by Brayton cycle. Based on supercritical CO2Brayton cycle power generation technology with supercritical CO2Instead of in a conventional Rankine cycleThe water vapor can obviously reduce the water consumption of the power station and reduce the project investment.
The invention relates to a tower type solar thermal power generation system based on supercritical fluid, which has the advantages that: the invention can improve the energy conversion efficiency of the tower type solar thermal power station, improve the safety and stability of the system and reduce the power generation cost.

Claims (7)

Translated fromChinese
1.一种基于超临界流体的塔式太阳能热发电系统,其特征在于,包括三个子系统和发电机(12),所述子系统分别为集热系统、传热储热系统和热力循环系统;所述集热系统包括布置于光照充足区域的定日镜场(1),和用于吸收来自所述定日镜场反射的太阳光的集热器(2);所述传热储热系统由所述集热器(2)、高温储热器(6)、热交换器(7)、低温储热器(4)和进料泵(3)通过管道依次首尾相连组成,所述传热储热系统内的工质为超临界碳氢化合物(5);所述热力循环系统由所述热交换器(7)、汽轮机(11)、冷凝器(9)和压缩机(8)通过管道依次首尾相连组成,所述热力循环系统中的循环工质为超临界CO2(10),所述汽轮机(11)与发电机(12)驱动相连。1. a tower type solar thermal power generation system based on supercritical fluid, is characterized in that, comprises three subsystems and generator (12), and described subsystems are heat collecting system, heat transfer heat storage system and thermodynamic circulation system respectively ; the heat collection system comprises a heliostat field (1) arranged in a well-lit area, and a heat collector (2) for absorbing sunlight reflected from the heliostat field; the heat transfer heat storage The system consists of the heat collector (2), the high temperature heat accumulator (6), the heat exchanger (7), the low temperature heat accumulator (4) and the feed pump (3) which are connected end to end through pipelines. The working medium in the thermal heat storage system is supercritical hydrocarbon (5); the thermodynamic cycle system is passed through the heat exchanger (7), the steam turbine (11), the condenser (9) and the compressor (8) The pipelines are connected end to end in sequence, the circulating working medium in the thermodynamic cycle system is supercritical CO2 (10), and the steam turbine (11) is drivingly connected to the generator (12).2.根据权利要求1所述的一种基于超临界流体的塔式太阳能热发电系统,其特征在于,所述传热储热系统的循环运行过程为:所述超临界碳氢化合物(5)在集热器(2)内吸收定日镜场(1)聚集的太阳光能,然后所述高温储热器(6)储存在集热器(2)内吸热后流出的高温超临界碳氢化合物,然后在所述热交换器(7)内高温碳氢化合物将能量传递给所述热力循环系统中的循环工质,再通过所述低温储热器(4)储存热交换器(7)流出的低温超临界碳氢化合物,所述进料泵(3)将低温超临界碳氢化合物升压后输送至集热器(2)内再次吸收太阳能。2. A supercritical fluid-based tower solar thermal power generation system according to claim 1, wherein the cycle operation process of the heat transfer and heat storage system is: the supercritical hydrocarbon (5) The solar energy collected by the heliostat field (1) is absorbed in the heat collector (2), and then the high temperature heat storage device (6) stores the high temperature supercritical carbon that flows out after absorbing heat in the heat collector (2). Hydrogen compounds, and then the high-temperature hydrocarbons in the heat exchanger (7) transfer energy to the circulating working fluid in the thermal cycle system, and then store the heat exchanger (7) through the low-temperature heat accumulator (4). ) outflowing low-temperature supercritical hydrocarbons, the feed pump (3) boosts the low-temperature supercritical hydrocarbons and transports them to the collector (2) to absorb solar energy again.3.根据权利要求2所述的一种基于超临界流体的塔式太阳能热发电系统,其特征在于,所述热力循环系统的循环运行过程为:在所述热交换器(7)内高温超临界碳氢化合物将能量传递给所述热力循环系统中的超临界CO2,使得超临界CO2温度、压力升高,推动汽轮机(11)的叶片做功,将超临界CO2携带的热能转变为汽轮机(11)的机械能,汽轮机(11)带动发电机(12)发电,置于汽轮机(11)出口所述冷凝器(9)将做完工的超临界CO2等压冷凝,然后通过置于冷凝器(9)之后的所述压缩机(8)对超临界CO2(10)进行等熵压缩,使之压力升高,并进入所述热交换器(7)内再次吸热。3. A supercritical fluid-based tower solar thermal power generation system according to claim 2, wherein the cycle operation process of the thermodynamic cycle system is: in the heat exchanger (7), a high temperature superheating The critical hydrocarbon transfers energy to the supercritical CO2 in the thermodynamic cycle system, so that the temperature and pressure of the supercritical CO2 increase, push the blades of the steam turbine (11) to do work, and convert the thermal energy carried by the supercritical CO2 into The mechanical energy of the steam turbine (11), the steam turbine (11) drives the generator (12) to generate electricity, and the condenser (9) is placed at the outlet of the steam turbine (11) to isobarically condense the completed supercritical CO2 , and then the condenser (9) is placed in the condenser The compressor (8) after the device (9) performs isentropic compression on the supercritical CO2 (10) to increase its pressure, and enters the heat exchanger (7) to absorb heat again.4.根据权利要求1所述的一种基于超临界流体的塔式太阳能热发电系统,其特征在于,所述低温储热器(4)的温度范围是400摄氏度以下,高温储热器(6)的温度范围是400摄氏度以上。4. A kind of tower type solar thermal power generation system based on supercritical fluid according to claim 1, is characterized in that, the temperature range of described low temperature heat accumulator (4) is below 400 degrees Celsius, and high temperature heat accumulator (6) ) temperature range is above 400 degrees Celsius.5.根据权利要求1所述的一种基于超临界流体的塔式太阳能热发电系统,其特征在于,所述集热器(2)为吸热高塔。5 . The supercritical fluid-based tower solar thermal power generation system according to claim 1 , wherein the heat collector ( 2 ) is a high heat absorption tower. 6 .6.根据权利要求5所述的一种基于超临界流体的塔式太阳能热发电系统,其特征在于,所述吸热高塔为框架—支撑结构的钢结构体系。6 . The supercritical fluid-based tower solar thermal power generation system according to claim 5 , wherein the heat-absorbing tower is a steel structure system of a frame-support structure. 7 .7.根据权利要求5所述的一种基于超临界流体的塔式太阳能热发电系统,其特征在于,所述吸热高塔为框架—剪力墙结构或单筒式结构的混凝土结构体系。7 . The supercritical fluid-based tower solar thermal power generation system according to claim 5 , wherein the heat-absorbing high tower is a concrete structure system of a frame-shear wall structure or a single-tube structure. 8 .
CN201911221220.6A2019-12-032019-12-03 A tower solar thermal power generation system based on supercritical fluidPendingCN111102142A (en)

Priority Applications (1)

Application NumberPriority DateFiling DateTitle
CN201911221220.6ACN111102142A (en)2019-12-032019-12-03 A tower solar thermal power generation system based on supercritical fluid

Applications Claiming Priority (1)

Application NumberPriority DateFiling DateTitle
CN201911221220.6ACN111102142A (en)2019-12-032019-12-03 A tower solar thermal power generation system based on supercritical fluid

Publications (1)

Publication NumberPublication Date
CN111102142Atrue CN111102142A (en)2020-05-05

Family

ID=70421046

Family Applications (1)

Application NumberTitlePriority DateFiling Date
CN201911221220.6APendingCN111102142A (en)2019-12-032019-12-03 A tower solar thermal power generation system based on supercritical fluid

Country Status (1)

CountryLink
CN (1)CN111102142A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
CN112128070A (en)*2020-09-242020-12-25北京前沿动力科技股份有限公司Solar photo-thermal carbon dioxide Brayton cycle system of ORC (organic Rankine cycle) intercooling compressor
CN114810522A (en)*2021-01-292022-07-29中国能源建设集团规划设计有限公司 a power generation system
CN115574363A (en)*2022-10-112023-01-06西安科技大学 A solar-wind energy development and utilization system and method based on heat storage in coal mine goaf
WO2024021296A1 (en)*2022-07-262024-02-01南京工业大学Ultra-supercritical solar tower-type water working medium heat absorber
CN118242778A (en)*2024-04-292024-06-25浙江可胜技术股份有限公司 A tower solar thermal utilization system
CN119393926A (en)*2024-10-142025-02-07西安热工研究院有限公司 A carbon dioxide heat pump energy storage system coupled with solar energy utilization

Citations (9)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
CN101968042A (en)*2010-10-192011-02-09中山大学Multistage full-effect solar heat power generation method
CN102400867A (en)*2010-09-082012-04-04中国科学院工程热物理研究所 Supercritical CO2 solar thermal power generation system with heat storage
CN102859190A (en)*2010-04-192013-01-02道康宁公司Solar thermal power plant
CN105673107A (en)*2016-01-202016-06-15中国科学院工程热物理研究所Trough and tower collecting compound driven supercritical carbon dioxide generating system and method
WO2016172144A1 (en)*2015-04-232016-10-27University Of Florida Research Foundation, Inc.Method for the generation of power
CN107060925A (en)*2017-05-112017-08-18中国科学院力学研究所A kind of overcritical working medium constant pressure energy storage system
CN108361163A (en)*2017-12-052018-08-03北京石油化工学院Electricity generation system
CN109296511A (en)*2018-11-092019-02-01中国科学技术大学 A supercritical carbon dioxide Brayton cycle tower solar thermal power generation system
CN209704778U (en)*2019-01-102019-11-29上海发电设备成套设计研究院有限责任公司A kind of tower-type solar thermal power generating system

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
CN102859190A (en)*2010-04-192013-01-02道康宁公司Solar thermal power plant
CN102400867A (en)*2010-09-082012-04-04中国科学院工程热物理研究所 Supercritical CO2 solar thermal power generation system with heat storage
CN101968042A (en)*2010-10-192011-02-09中山大学Multistage full-effect solar heat power generation method
WO2016172144A1 (en)*2015-04-232016-10-27University Of Florida Research Foundation, Inc.Method for the generation of power
CN105673107A (en)*2016-01-202016-06-15中国科学院工程热物理研究所Trough and tower collecting compound driven supercritical carbon dioxide generating system and method
CN107060925A (en)*2017-05-112017-08-18中国科学院力学研究所A kind of overcritical working medium constant pressure energy storage system
CN108361163A (en)*2017-12-052018-08-03北京石油化工学院Electricity generation system
CN109296511A (en)*2018-11-092019-02-01中国科学技术大学 A supercritical carbon dioxide Brayton cycle tower solar thermal power generation system
CN209704778U (en)*2019-01-102019-11-29上海发电设备成套设计研究院有限责任公司A kind of tower-type solar thermal power generating system

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
罗毓珊 等: "高参数小管径内煤油的传热特性研究", 《工程热物流学报》*

Cited By (8)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
CN112128070A (en)*2020-09-242020-12-25北京前沿动力科技股份有限公司Solar photo-thermal carbon dioxide Brayton cycle system of ORC (organic Rankine cycle) intercooling compressor
CN114810522A (en)*2021-01-292022-07-29中国能源建设集团规划设计有限公司 a power generation system
CN114810522B (en)*2021-01-292025-01-10中国电力工程顾问集团有限公司 A power generation system
WO2024021296A1 (en)*2022-07-262024-02-01南京工业大学Ultra-supercritical solar tower-type water working medium heat absorber
CN115574363A (en)*2022-10-112023-01-06西安科技大学 A solar-wind energy development and utilization system and method based on heat storage in coal mine goaf
CN115574363B (en)*2022-10-112023-09-19西安科技大学 A light-wind energy development and utilization system and method based on heat storage in coal mine goafs
CN118242778A (en)*2024-04-292024-06-25浙江可胜技术股份有限公司 A tower solar thermal utilization system
CN119393926A (en)*2024-10-142025-02-07西安热工研究院有限公司 A carbon dioxide heat pump energy storage system coupled with solar energy utilization

Similar Documents

PublicationPublication DateTitle
CN208380763U (en)A kind of Bretton solar-thermal generating system of improvement
CN111102142A (en) A tower solar thermal power generation system based on supercritical fluid
CN209145783U (en) A supercritical carbon dioxide Brayton cascade cycle solar thermal power generation system
WO2012022273A1 (en)Solar power ammonia thermoelectric conversion system
CN104896764A (en)Solar thermal power generation method and device
CN115013096B (en) A thermal power generation, photothermal power generation and supercritical carbon dioxide coupled power generation system and method
CN102661259B (en)Integrated solar thermal power generation system
CN204572366U (en)Enclosed Boulez is adopted to pause the tower-type solar thermal power generating system of circulation
CN106499601B (en)Closed helium turbine tower type solar thermal power generation system with heat storage function
CN203348019U (en)System improving complex conversion efficiency of heat and electricity between terrestrial heat energy and solar energy
CN107313904A (en)Solar air carbon dioxide association circulating power generation system
CN104764217A (en)Generalized closed Brayton type tower type solar thermal power generation method and system
CN201916139U (en) Tower type solar cycle thermal power generation system
WO2020029422A1 (en)Disk type solar photothermal gradient utilization system
CN209145784U (en) A supercritical carbon dioxide Brayton cycle tower solar thermal power generation system
CN204693854U (en)A kind of solar energy thermal-power-generating device
CN114922789A (en)Compressed carbon dioxide liquid energy storage system based on solar energy and operation method thereof
CN106762487B (en)Direct-expansion solar combined heat and power system with two-stage heat storage water tank
CN211777845U (en)Geothermal photo-thermal combined type continuous power generation system
CN118882213A (en) Energy utilization system and method for coupling solar thermal storage and carbon dioxide energy storage
CN108506177A (en)Solar energy overlapping organic Rankine cycle power generation system based on gas-liquid two-phase heat collector
CN208347995U (en)Solar energy overlapping organic Rankine cycle power generation system based on gas-liquid two-phase heat collector
CN203348020U (en)Geothermal power generation system adopting photo-thermal secondary evaporation
CN109869924A (en) A solar thermal utilization test system and its working method
CN204572364U (en)Enclosed Boulez pauses type tower-type solar thermal power generating system

Legal Events

DateCodeTitleDescription
PB01Publication
PB01Publication
SE01Entry into force of request for substantive examination
SE01Entry into force of request for substantive examination
RJ01Rejection of invention patent application after publication
RJ01Rejection of invention patent application after publication

Application publication date:20200505


[8]ページ先頭

©2009-2025 Movatter.jp