CN113531920A - Solar energy-gas combined cycle power generation system - Google Patents

Solar energy-gas combined cycle power generation system Download PDF

Info

Publication number
CN113531920A
CN113531920A CN202110998620.9A CN202110998620A CN113531920A CN 113531920 A CN113531920 A CN 113531920A CN 202110998620 A CN202110998620 A CN 202110998620A CN 113531920 A CN113531920 A CN 113531920A
Authority
CN
China
Prior art keywords
pressure
steam
solar
low
water
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
CN202110998620.9A
Other languages
Chinese (zh)
Inventor
曹勇
安欣
张开鹏
王勇刚
唐伟
杨光锐
李继福
曲广浩
吴猛
刘炎伟
何未雨
李钊
吴晋
张海龙
王邦行
杨明强
王嘉琦
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 Thermal Power Research Institute Co Ltd
Original Assignee
Xian Thermal Power Research Institute Co Ltd
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 Thermal Power Research Institute Co Ltd filed Critical Xian Thermal Power Research Institute Co Ltd
Priority to CN202110998620.9A priority Critical patent/CN113531920A/en
Publication of CN113531920A publication Critical patent/CN113531920A/en
Pending legal-status Critical Current

Links

Images

Classifications

    • 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
    • F24S20/40—Solar heat collectors combined with other heat sources, e.g. using electrical heating or heat from ambient air
    • 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
    • F01D15/10—Adaptations for driving, or combinations with, electric generators
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02C—GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
    • F02C3/00—Gas-turbine plants characterised by the use of combustion products as the working fluid
    • F02C3/04—Gas-turbine plants characterised by the use of combustion products as the working fluid having a turbine driving a compressor
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22—STEAM GENERATION
    • F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B1/00—Methods of steam generation characterised by form of heating method
    • F22B1/02—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
    • F22B1/18—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22—STEAM GENERATION
    • F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B37/00—Component parts or details of steam boilers
    • F22B37/02—Component parts or details of steam boilers applicable to more than one kind or type of steam boiler
    • F22B37/26—Steam-separating arrangements
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00—Arrangements of devices for treating smoke or fumes
    • F23J15/06—Arrangements of devices for treating smoke or fumes of coolers
    • 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
    • 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]
    • 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
    • Y02E20/30—Technologies for a more efficient combustion or heat usage

Abstract

A solar energy-gas combined cycle power generation system comprises a gas-steam combined cycle subsystem and a solar energy direct steam subsystem. The gas-steam combined cycle subsystem comprises a gas turbine, a waste heat boiler, a steam turbine set and a water feed pump set, and the solar direct steam subsystem comprises a groove type solar heat collection preheating area, a heat collection evaporation area, a heat collection overheating area, a circulating pump and a steam-water separator. Exhaust gas of the gas turbine heats feed water of a high-pressure part of the waste heat boiler to generate high-pressure steam, the feed water of a low-pressure part can reach saturation temperature through the evaporator and the solar heat collector after being preheated, and the tail hot water heater heats feed water of an inlet of a preheating area of the solar heat collector to reduce the exhaust gas temperature of the waste heat boiler. The invention not only improves the heat exchange efficiency of the waste heat boiler, but also improves the utilization efficiency of energy, and can flexibly change the operation mode to achieve the stable operation of the unit according to the change of the direct solar radiation intensity, thereby realizing the multi-energy complementation and the cascade utilization.

Description

Solar energy-gas combined cycle power generation system
Technical Field
The invention relates to the technical field of power generation equipment, in particular to a solar energy-gas combined cycle power generation system.
Background
Solar energy is inexhaustible clean energy and has very wide development prospect. Solar thermal power generation has been developed to various degrees around the world, but its large-scale commercial application has been hampered due to solar energy discontinuity and instability. The gas-steam combined cycle power generation is a clean energy power generation mode, has small environmental pollution, short construction period and reliable and stable operation, and the core equipment of the gas-steam combined cycle is a gas turbine which is very stable in operation but has larger influence on the performance by environmental factors. In order to improve the thermal efficiency of the gas-steam combined cycle, the exhaust gas temperature of the waste heat boiler can be reduced as far as possible within a certain range. The two energy utilization forms have certain defects, and the complementary power generation form can effectively reduce the influence of high-temperature weather on the output of the unit and also can enable the unit to generate power continuously and stably.
The utilization of single energy variety is subject to multi-directional elbow, so in the future development process, it is a great trend to build a comprehensive energy system with multiple energy sources organically integrated and complemented.
Disclosure of Invention
The invention aims to provide a solar energy-gas combined cycle power generation system, which is an energy complementary power generation mode, and improves the operation performance of the system by replacing an evaporator of a waste heat boiler with a solar heat collection field and utilizing a boiler tail heater as a solar heat collection preheating mode, and the mode can effectively improve the heat exchange efficiency of the waste heat boiler and the continuous stability of solar power generation.
In order to achieve the purpose, the invention adopts the following technical scheme:
a solar energy-gas combined cycle power generation system comprises a gas-steam combined cycle power generation electronic system and a solar energy direct steam subsystem, wherein the two subsystems are connected through a pipeline;
the gas-steam combined cycle power generation subsystem comprises a gas turbine, a gas turbine generator, a waste heat boiler, a condenser, a steam turbine generator, a condensate pump and a high-pressure water feed pump;
the gas turbine compressor is used for absorbing air from the outside atmosphere and compressing the air, the compressed air is mixed with fuel sprayed into a combustion chamber and then is combusted, the generated high-temperature and high-pressure flue gas enters the gas turbine to do work to drive the compressor to rotate and a gas turbine generator to generate electricity, the exhaust gas of the gas turbine enters the waste heat boiler and is discharged to the atmosphere through a chimney through a high-pressure superheater, a high-pressure evaporator, a high-pressure economizer, a low-pressure superheater, a low-pressure evaporator, a low-pressure economizer and a tail heat exchanger of the waste heat boiler respectively; high-pressure heat exchange steam generated in the high-pressure heat exchange area directly enters a high-pressure cylinder of a steam turbine to do work, and feed water in the low-pressure heat exchange area can enter a low-pressure evaporator or a heat collection evaporation area of a solar direct steam system through a low-pressure steam pocket after passing through a low-pressure economizer to generate low-pressure superheated steam; the tail heat exchanger preheats the feed water to 80-90 ℃ and then supplies the feed water to a heat collection preheating area of solar direct steam; the high-pressure water feeding pump is connected with the low-pressure steam pocket, and the high-pressure water feeding pump boosts the pressure of water in the low-pressure steam pocket and supplies the water to the high-pressure economizer;
the solar direct steam subsystem comprises a heat collection preheating area, a heat collection evaporation area, a steam-water separator, a circulating pump and a heat collection overheating area; the feed water of the heat collection preheating zone comes from an outlet of a hot water heat exchanger of the waste heat boiler, the feed water enters the heat collection evaporation zone to reach saturation temperature after being preheated, then is separated by a steam-water separator, the saturated water returns to the heat collection evaporation zone through a circulating pump to be heated continuously, the separated saturated steam generates low-pressure superheated steam after passing through the heat collection superheating zone, the low-pressure superheated steam generated by the solar direct steam system and the low-pressure superheated steam generated by the waste heat boiler are combined and then enter a low-pressure superheated steam header, and the low-pressure superheated steam and the exhaust steam of the high-pressure cylinder are mixed and then enter a low-pressure cylinder of a steam turbine to do work; the exhaust steam of the low pressure cylinder enters a condenser, and condensed water is supplied to a low pressure economizer and a hot water heat exchanger of the waste heat boiler after passing through a condensate pump, so that a thermodynamic cycle is achieved.
The invention has the further improvement that the waste heat boiler is in double-pressure natural circulation, and the parameters of the low-pressure superheated steam generated by the low-pressure heat exchange area of the waste heat boiler are matched with the parameters of the superheated steam generated by the solar direct steam system.
The invention is further improved in that a heat collection evaporation area of a solar direct steam system is used for replacing a low-pressure evaporator of a waste heat boiler.
The invention has the further improvement that a hot water heater is additionally arranged at the tail part of the waste heat boiler to heat the feed water of the solar heat collection preheating area, so that the heat exchange efficiency of the waste heat boiler is improved, and the investment of the solar heat collection preheating area can be reduced.
The solar direct steam system is further improved in that a groove type heat collector is adopted by the solar direct steam system, and a groove type solar heat collection field is divided into a preheating area, an evaporation area and a superheating area according to different heat collection temperatures.
The invention has the further improvement that after the waste heat boiler low-pressure evaporator is put into the solar heat collection field, the waste heat boiler low-pressure evaporator is completely or partially replaced, at the moment, the temperature of the flue gas is unchanged or partially reduced when the flue gas flows through the low-pressure evaporator, and water vapor with saturated temperature generated by the low-pressure evaporator and the solar heat collection field enters the low-pressure steam pocket for steam-water separation.
The invention has the further improvement that the tail heater of the waste heat boiler heats the condensed water to 80-90 ℃, the temperature of the condensed water is close to the exhaust gas temperature of the waste heat boiler, and the condensed water is used as the feed water of the preheating area of the solar heat collection field after being heated.
The invention has the further improvement that the steam-water mixture in the evaporation area of the solar heat collection field passes through a steam-water separator, the separated water enters the overheating area of the heat collection field, and the separated water returns to the evaporation area through a circulating pump.
The invention is further improved in that the waste heat boiler is in a double-pressure horizontal natural circulation mode.
The invention has at least the following beneficial technical effects:
1. solar energy and gas are complementary, and compared with single solar power generation, the power station can continuously operate under the condition of not increasing energy storage, so that the stability of the unit is effectively improved; compared with single gas power generation, solar power generation is increased, and the power generation power of clean energy is improved.
2. The two energy sources are coupled through the waste heat boiler, the solar heat collection is utilized to replace a low-pressure evaporator of the waste heat boiler, and the operation is flexible and reliable.
3. The solar heat collection water supply is heated by the heater at the tail of the waste heat boiler, so that on one hand, the exhaust gas temperature of the waste heat boiler is reduced, and the heat exchange efficiency of the waste heat boiler is further improved; on the other hand, the investment of a solar heat collection preheating area is also reduced.
Drawings
FIG. 1 is a schematic diagram of a solar-gas combined cycle power generation system of the present invention.
Description of reference numerals:
1. the system comprises a compressor, 2, a combustion chamber, 3, a gas turbine, 4, a gas turbine generator, 5, a high-pressure superheater, 6, a high-pressure evaporator, 7, a high-pressure economizer, 8, a high-pressure steam pocket, 9, a low-pressure superheater, 10, a low-pressure evaporator, 11, a low-pressure economizer, 12, a low-pressure steam pocket, 13, a high-pressure water feed pump, 14, a tail heat exchanger, 15, a heat collection preheating zone, 16, a heat collection evaporation zone, 17, a steam-water separator, 18, a circulating pump, 19, a heat collection overheating zone, 20, a condenser, 21, a low-pressure steam main pipe, 22, a steam turbine high-pressure cylinder, 23, a steam turbine low-pressure cylinder, 24, a steam turbine generator, 25 and a condensate pump.
Detailed Description
The following further describes embodiments of the present invention with reference to the drawings.
Referring to the attached figure 1, the invention aims to establish an energy utilization form of solar energy and gas-steam combined cycle complementation, and aims to solve the utilization form of single energy, increase the complementation utilization of clean energy and improve the efficiency and the continuity of system operation.
In order to achieve the purpose, the solar energy-gas combined cycle power generation system provided by the invention comprises a gas turbine generator set consisting of a gas compressor 1, a combustion chamber 2, a gas turbine 3 and a gas turbine generator 4. The waste heat boiler consists of a high-pressure superheater 5, a high-pressure evaporator 6, a high-pressure economizer 7, a high-pressure steam drum 8, a high-pressure water feeding pump 13, a low-pressure superheater 9, a low-pressure evaporator 10, a low-pressure economizer 11, a low-pressure steam drum 12 and a tail heat exchanger 14. The solar direct steam system consists of a heat collection preheating area 15, a heat collection evaporation area 16, a steam-water separator 17, a circulating pump 18 and a heat collection overheating area 19. The equipment of the steam turbine generator unit comprises a condenser 20, a low-pressure steam main pipe 21, a high-pressure steam turbine cylinder 22, a low-pressure steam turbine cylinder 23, a steam turbine generator 24 and a condensate pump 25.
The waste heat boiler high-pressure superheated steam is connected with a high-pressure cylinder of a steam turbine through a high-pressure steam pipeline, the low-pressure superheated steam of the waste heat boiler, the solar heat collection superheated steam and the high-pressure cylinder exhaust steam are connected with a low-pressure steam main pipe through a low-pressure steam pipeline, and the low-pressure steam main pipe enters a low-pressure cylinder of the steam turbine through a steam pipeline. And the high-pressure cylinder and the low-pressure cylinder of the steam turbine do work and then drive the steam turbine generator.
The exhaust gas temperature of the gas turbine is above 540 ℃, the temperature of the high-pressure superheated steam is 500 ℃, and the pressure is 5 MPa. The temperature of the low-pressure superheated steam is 200 ℃, the pressure is 0.5MPa, and the outlet temperature of the tail heat exchanger is 80 ℃. The outlet pressure of the condensate pump is 1MPa, and the outlet pressure of the high-pressure feed pump is 5.9 MPa.
The use and method of the system is further described below: in rainy days or nights, the solar illumination intensity is insufficient, the heat collection temperature cannot meet the design requirement, and the solar heat collection field cannot be put into operation. At the moment, the unit is required to cut off the connection between the water supply and the tail heat exchanger and the connection between the solar heat collection overheating area and the low-pressure steam main pipe, and the gas-steam combined cycle unit continues to operate. When the unit is started. The method comprises the following steps of firstly starting a gas turbine, introducing exhaust gas into a waste heat boiler, slowly raising the temperature and boosting the pressure of the waste heat boiler after the gas turbine is stabilized at a low load, increasing the load of a gas turbine after a certain pressure is reached, and slowly increasing the parameters of the waste heat boiler to reach a rated value. Secondly, in the process of heating and boosting the temperature of the waste heat boiler, high-pressure and low-pressure superheated steam is required to go to a condenser through a bypass system, the bypass is slowly closed after the temperature and the pressure reach rated values, and main steam enters a steam turbine to do work. And finally, after all the parameters reach the rated working value, loading the gas turbine, and coordinately increasing the load of the gas turbine to the rated value.
When the direct solar radiation intensity reaches the minimum required value after the gas-steam combined cycle unit is stabilized, the condensed water is gradually started to the heat collection preheating area of the solar field according to the radiation intensity, and the water supply flow of the heat collection field is adjusted according to the parameter change of the heat collection superheated steam. The outlet of the low-pressure economizer of the waste heat boiler is slowly opened to the solar heat collection evaporation area, and the inlet flow and the outlet flow are adjusted according to the outlet parameters of the heat collection evaporation area.
The invention aims to provide a method, and specific unit start-stop and operation strategies, wherein relevant knowledge is well known to professional technicians.
The above description is only for the preferred embodiment of the present invention, but the scope of the present invention is not limited thereto, and any person skilled in the art should be able to cover the technical solutions and the inventive concepts of the present invention within the technical scope of the present invention.

Claims (9)

1. A solar energy-gas combined cycle power generation system is characterized by comprising a gas-steam combined cycle power generation electronic system and a solar energy direct steam subsystem, wherein the two subsystems are connected through a pipeline;
the gas-steam combined cycle power generation subsystem comprises a gas turbine, a gas turbine generator, a waste heat boiler, a condenser, a steam turbine generator, a condensate pump and a high-pressure water feed pump;
the gas turbine compressor is used for absorbing air from the outside atmosphere and compressing the air, the compressed air is mixed with fuel sprayed into a combustion chamber and then is combusted, the generated high-temperature and high-pressure flue gas enters the gas turbine to do work to drive the compressor to rotate and a gas turbine generator to generate electricity, the exhaust gas of the gas turbine enters the waste heat boiler and is discharged to the atmosphere through a chimney through a high-pressure superheater, a high-pressure evaporator, a high-pressure economizer, a low-pressure superheater, a low-pressure evaporator, a low-pressure economizer and a tail heat exchanger of the waste heat boiler respectively; high-pressure heat exchange steam generated in the high-pressure heat exchange area directly enters a high-pressure cylinder of a steam turbine to do work, and feed water in the low-pressure heat exchange area can enter a low-pressure evaporator or a heat collection evaporation area of a solar direct steam system through a low-pressure steam pocket after passing through a low-pressure economizer to generate low-pressure superheated steam; the tail heat exchanger preheats the feed water to 80-90 ℃ and then supplies the feed water to a heat collection preheating area of solar direct steam; the high-pressure water feeding pump is connected with the low-pressure steam pocket, and the high-pressure water feeding pump boosts the pressure of water in the low-pressure steam pocket and supplies the water to the high-pressure economizer;
the solar direct steam subsystem comprises a heat collection preheating area, a heat collection evaporation area, a steam-water separator, a circulating pump and a heat collection overheating area; the feed water of the heat collection preheating zone comes from an outlet of a hot water heat exchanger of the waste heat boiler, the feed water enters the heat collection evaporation zone to reach saturation temperature after being preheated, then is separated by a steam-water separator, the saturated water returns to the heat collection evaporation zone through a circulating pump to be heated continuously, the separated saturated steam generates low-pressure superheated steam after passing through the heat collection superheating zone, the low-pressure superheated steam generated by the solar direct steam system and the low-pressure superheated steam generated by the waste heat boiler are combined and then enter a low-pressure superheated steam header, and the low-pressure superheated steam and the exhaust steam of the high-pressure cylinder are mixed and then enter a low-pressure cylinder of a steam turbine to do work; the exhaust steam of the low pressure cylinder enters a condenser, and condensed water is supplied to a low pressure economizer and a hot water heat exchanger of the waste heat boiler after passing through a condensate pump, so that a thermodynamic cycle is achieved.
2. The solar-gas combined cycle power generation system of claim 1, wherein the exhaust-heat boiler is a dual-pressure natural cycle, and the parameters of the low-pressure superheated steam generated by the low-pressure heat exchange area of the exhaust-heat boiler are matched with the parameters of the superheated steam generated by the solar direct steam system.
3. The solar-gas combined cycle power generation system of claim 1, wherein the low pressure evaporator of the waste heat boiler is replaced with a heat collection evaporation zone of a solar direct steam system.
4. The solar-gas combined cycle power generation system of claim 1, wherein a hot water heater is additionally installed at the rear of the exhaust-heat boiler to heat the feed water of the solar heat collecting preheating zone, so as to improve the heat exchange efficiency of the exhaust-heat boiler and reduce the investment of the solar heat collecting preheating zone.
5. The solar-gas combined cycle power generation system of claim 1, wherein the solar direct steam system employs a trough collector, and the trough solar heat collection field is divided into a preheating zone, an evaporation zone and a superheating zone according to different heat collection temperatures.
6. The solar-gas combined cycle power generation system of claim 1, wherein the exhaust-heat boiler low-pressure evaporator is completely or partially replaced after the solar heat collection field is put into operation, at this time, the temperature of the flue gas is unchanged or is partially reduced when the flue gas flows through the low-pressure evaporator, and water vapor with saturated temperature generated by the low-pressure evaporator and the solar heat collection field enters the low-pressure steam drum to be subjected to steam-water separation.
7. The solar-gas combined cycle power generation system of claim 1, wherein the exhaust-heat boiler tail heater heats the condensed water to 80-90 ℃ which is close to the exhaust gas temperature of the exhaust-heat boiler, and the heated condensed water is used as the feed water for the preheating area of the solar heat collection field.
8. The solar energy-gas combined cycle power generation system of claim 1, wherein the steam-water mixture in the evaporation zone of the solar heat collection field passes through a steam-water separator, the separated water enters the superheat zone of the heat collection field, and the separated water returns to the evaporation zone through a circulating pump.
9. The solar-gas combined cycle power generation system of claim 1, wherein the waste heat boiler is in a dual pressure, horizontal, natural circulation form.
CN202110998620.9A 2021-08-27 2021-08-27 Solar energy-gas combined cycle power generation system Pending CN113531920A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202110998620.9A CN113531920A (en) 2021-08-27 2021-08-27 Solar energy-gas combined cycle power generation system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202110998620.9A CN113531920A (en) 2021-08-27 2021-08-27 Solar energy-gas combined cycle power generation system

Publications (1)

Publication Number Publication Date
CN113531920A true CN113531920A (en) 2021-10-22

Family

ID=78092198

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202110998620.9A Pending CN113531920A (en) 2021-08-27 2021-08-27 Solar energy-gas combined cycle power generation system

Country Status (1)

Country Link
CN (1) CN113531920A (en)

Similar Documents

Publication Publication Date Title
US9909496B2 (en) Power generation system
CN109681281B (en) Biomass cogeneration system capable of simultaneously recovering exhaust steam and flue gas waste heat
CN101270675A (en) Solar energy and coal-burning unit combined thermal power generation system
CN112855293A (en) Integrated heat storage industrial steam supply cogeneration peak shaving frequency modulation system and operation method
CN108953083B (en) Distributed power generation system and method based on trough type solar gas combined cycle
CN112611010B (en) Adjusting method of flexible adjusting system for power generation load of multi-heat-source cogeneration unit
CN215170241U (en) Energy storage peak regulation coupling system of thermal power plant
CN105804872A (en) Steam reinjection type gas turbine power generation method and device based on solar energy and waste heat recovery
Ibrahim et al. Parametric simulation of triple-pressure reheat combined cycle: A case study
CN108843418A (en) A kind of double pressure high efficiency burnt gas supercritical carbon dioxide association circulating power generation systems
CN201826909U (en) Complementary power generation system combining solar energy and biomass energy
CN108757071A (en) A kind of solar energy-combined cycle complementation co-generation unit
CN108843406B (en) Flue gas reheating type disc type photo-thermal and gas-steam combined cycle power generation system
CN106523155B (en) A kind of chemical formula recycle-water method and apparatus based on solar gas expander system
CN109139400B (en) Solar thermal complementary combined cycle system capable of changing integration mode based on irradiation change
CN205503282U (en) Steam recycles formula gas turbine power generation device based on solar energy and waste heat recovery
CN208380648U (en) A kind of association circulating power generation system of the double pressure supercritical carbon dioxide waste heat boilers of band
CN201723313U (en) Gas turbine combined cycling device for distributed air and fuel humidification
CN110953763A (en) Gas cogeneration system and control method thereof
CN215490405U (en) Solar energy-gas combined cycle power generation system
CN109296413A (en) A kind of the bypass double reheat power generator and method cooling using deep sea water
CN113531920A (en) Solar energy-gas combined cycle power generation system
CN215174935U (en) High-low temperature heat storage peak shaving system of thermal power plant
CN209369886U (en) A kind of bypass double reheat power generator cooling using deep sea water
CN209875234U (en) Biomass direct-combustion cogeneration system

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination