CN217844870U - Multi-tank molten salt energy storage system based on energy gradient utilization - Google Patents
Multi-tank molten salt energy storage system based on energy gradient utilization Download PDFInfo
- Publication number
- CN217844870U CN217844870U CN202221457393.5U CN202221457393U CN217844870U CN 217844870 U CN217844870 U CN 217844870U CN 202221457393 U CN202221457393 U CN 202221457393U CN 217844870 U CN217844870 U CN 217844870U
- Authority
- CN
- China
- Prior art keywords
- molten salt
- steam
- heat
- tank
- temperature
- 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.)
- Active
Links
Images
Classifications
-
- 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
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/14—Thermal energy storage
Landscapes
- Engine Equipment That Uses Special Cycles (AREA)
Abstract
The utility model discloses a many jars of fused salt energy storage system based on energy cascade utilizes. In a molten salt energy storage system using steam as a heat source, the heat in the steam is stored in a stepped manner according to the quality by arranging not less than three molten salt storage tanks with different temperatures, changing a molten salt flow, optimizing heat exchange and the like, so that the heat in a superheat section is stored in a molten salt medium with higher temperature. When the device works in a heat release and steam generation mode, the steam supply parameters can be improved by utilizing the molten salt with higher temperature. In the scene of heat storage and power generation of the system, the steam with higher parameters can improve the working capacity and the power generation efficiency of the system; under the scene of heat storage and steam supply, the steam with higher parameters can meet the steam requirements of more process types, and the adaptability of the molten salt energy storage system is improved.
Description
Technical Field
The utility model relates to an use steam as heat source, fused salt as the energy storage system scheme of heat-retaining medium, can be applied to fields such as flexibility transformation, energy storage peak shaving, industrial heating, steam power generation of coal-fired unit, especially relate to a many jars of fused salt energy storage system based on energy step utilizes.
Background
In recent years, with the rapid reduction of photovoltaic and wind power costs, the installed scale of renewable energy sources in China is rapidly increased. By the end of 2020, the installed capacity of photovoltaic and wind power in China exceeds 24% in all installed devices. However, the output of photovoltaic and wind power changes rapidly along with the fluctuation of resources, thereby bringing impact to the power grid. This conflict is even more pronounced as the renewable energy content increases.
In the total installed capacity of China, the proportion of the thermal power generating units is about 53.5%, the proportion of the generated energy is about 64% of coal and gas, and in 2020, the peak regulation capacity of the thermal power generating units plays a very important role in the safety of a power grid. For the thermal power generating unit with combined heat and power supply, because the power generating load and the heat supply load are coupled together, the contradiction which is difficult to solve exists between peak regulation and heat supply of the thermal power generating unit. For a pure condensation coal-fired power generating unit, after the load of a boiler is reduced to a certain limit value, the peak regulation capability of the thermal power generating unit is limited due to the risks of large air-coal proportioning deviation, uneven hearth heat load, deviation of water circulation from a safety range, instability and flameout of a burner and the like. The unit operation data participating in peak shaving shows that the risks are gradually increased when the boiler operates at the load lower than 50%; the load of the steam turbine can be reduced to below 30% or even lower, so a certain energy storage capacity is needed to solve the problem of output matching of the unit in the peak shaving period.
In recent years, with the promotion of the first photo-thermal power generation demonstration project in China, molten salt is gradually widely accepted as an ideal heat storage medium. The common schemes for peak regulation of thermal power generating units by using the molten salt heat storage technology mainly comprise two schemes: one is to directly heat the molten salt by utilizing valley electricity, and the other is to heat the molten salt by utilizing high-temperature steam in the valley period; and then, the energy stored in the molten salt is utilized to generate electricity or supply heat to the outside in the period of demand of the power grid or users.
In thermal power flexibility improvement, a double-tank system is generally adopted in the existing molten salt energy storage scheme. The system is provided with a high-temperature molten salt tank and a low-temperature molten salt tank which are used for storing molten salts with different temperatures respectively. However, in a molten salt heat storage system using steam as a heat source, a double-tank molten salt energy storage system generally faces the problems of low steam parameters and the like. When the steam generated by the energy storage system is used for acting and generating power, the output power and the generating efficiency of the energy storage system are restricted by lower steam parameters, and the application scene of the technology is also restricted by lower parameters when the steam is used for supplying heat. Therefore, there is a need for a better performing solution to the problems encountered in energy storage applications as described above.
SUMMERY OF THE UTILITY MODEL
In order to solve the technical problem, the utility model designs a many jars of fused salt energy storage system based on energy step utilizes. In a molten salt energy storage system using steam as a heat source, the heat in the steam is stored in a stepped manner according to the quality by arranging a plurality of molten salt storage tanks, changing a molten salt flow, optimizing heat exchange and the like, so that the heat in a superheat section is stored in a molten salt medium with higher temperature. When the heat release and steam generation mode works, the steam supply parameters can be improved by utilizing the molten salt with higher temperature. In the scene of heat storage and power generation of the system, the steam with higher parameters can improve the working capacity and the power generation efficiency of the system; under the scene of heat storage and steam supply, the steam with higher parameters can meet the steam requirements of more process types, and the adaptability of the molten salt energy storage system is improved.
The utility model adopts the following technical scheme:
a multi-tank molten salt energy storage system based on energy gradient utilization comprises not less than three molten salt storage tanks with different temperatures, a steam-molten salt heat exchange system (steam heat release and molten salt heat absorption) for heat storage and a molten salt-steam heat exchange system (molten salt heat release and steam heat absorption) for heat release, wherein the molten salt storage tanks with different temperatures are arranged according to the steam quality in the heat storage process, the steam-molten salt heat exchange system for heat storage is provided with a saturated steam-molten salt heat exchanger and an overheated steam-molten salt heat exchanger, the saturated steam-molten salt heat exchanger or the overheated steam-molten salt heat exchanger is arranged between pipelines communicated with the molten salt storage tanks with different temperatures, heat released by a steam condensation section and an overheated section in a steam pipeline is absorbed through heat exchange and stored into the molten salt storage tanks with different temperatures respectively, the heat is stored in a grading manner according to the quality, the molten salt-steam heat exchange system for heat release is provided with a molten salt-saturated water evaporator and a molten salt-overheated steam heat exchanger, the molten salt-steam evaporator or the overheated steam-saturated water evaporator-superheated steam heat exchanger is arranged between the pipelines communicated with different temperatures respectively, condensate water pipelines absorbs the heat exchange through the molten salt-saturated water pipeline, the molten salt-saturated water heat exchanger to evaporate the heat exchanger gradually, and further generate high-temperature steam heat, and generate high-steam power generation parameters.
The molten salt storage tanks of different temperatures not less than three include low temperature molten salt jar, be used for storing the middle temperature molten salt jar of phase transition latent heat respectively to and be used for storing the thermal high temperature molten salt jar of superheated section, phase transition latent heat section and superheated steam section have different heat transfer characteristics completely: the temperature of the water and water vapor remains substantially constant during evaporation or condensation, while a wide range of temperature variations are typically associated with the heat exchange of superheated steam. In order to improve the high-temperature molten salt temperature of the system, the flow of the molten salt for storing the heat of the superheat section is usually smaller than that of the molten salt for storing the phase-change latent heat section, and the requirements of different target molten salt temperatures can be met by adjusting the flow of the molten salt of the superheated steam section. In the heat release and steam production processes of the system, the evaporation and overheating processes of water are respectively matched with the fused salts of the phase change latent heat section and the overheated steam section, so that steam with higher parameters can be generated for power generation or heat supply, and the energy requirements of various types of users are met.
The heat storage process generally needs to be provided with a saturated steam-molten salt heat exchanger and a superheated steam-molten salt heat exchanger which respectively absorb heat released by a steam condensation section and a superheated section. Taking a three-tank molten salt energy storage system as an example, in the heat storage process, molten salt is pumped out from the low-temperature tank, heat released by saturated steam (part of sensible heat may be generated according to different processes) is absorbed, and most of generated medium-temperature molten salt returns to the medium-temperature molten salt tank. And a part of molten salt is continuously absorbed in the superheated steam-molten salt heat exchanger to be heated and changed into high-temperature molten salt, and the high-temperature molten salt returns to the high-temperature molten salt tank. In the above process, the aim of staged storage of energy by quality (as reflected in the temperature of the molten salt medium) is achieved.
The steam source of the heat storage process steam-molten salt heat exchanger can be a path of superheated steam, and can also be a plurality of paths of steam including superheated steam and reheated steam.
The heat release flow generally needs to be provided with a fused salt-saturated water evaporator and a fused salt-superheated steam heat exchanger. In order to meet the requirements of steam-water separation, a steam-water separation device or a steam drum is generally required to be arranged. Taking a three-pot molten salt system as an example: in the heat release process, the condensed water absorbs the heat released by the medium-temperature molten salt in the molten salt-saturated water evaporator, the heat is gradually evaporated, and the generated steam-water mixture enters a steam-water separation device; the saturated steam after steam-water separation enters a fused salt-superheated steam heat exchanger, continues to absorb the heat released by high-temperature fused salt, generates high-parameter steam and transmits the high-parameter steam to a power generation or heat supply system; the medium-temperature molten salt mainly comes from a medium-temperature molten salt storage tank, and part of the medium-temperature molten salt comes from the high-temperature molten salt after heat release. In the process, the evaporation and overheating processes of water are respectively realized according to the molten salt temperatures of different areas, the energy storage system can generate steam with higher parameters, and the cascade utilization of energy is realized.
Under the special condition that the parameters of the heat storage process and the heat release process are matched, the heat storage system and the heat release system can be combined through a loop capable of realizing bidirectional operation. However, this mode may cause the flexibility of the molten salt energy storage system to decrease, so that the heat storage process and the heat release process cannot be performed simultaneously.
The beneficial effects of the utility model are that:
1) Through the arrangement of a multi-tank molten salt system, molten salt heat storage and exchange processes with different parameters are constructed, the stepped storage and utilization of energy are realized, and the molten salt energy storage system can generate steam with higher parameters;
2) The heat source of the system can be a path of superheated steam, and can also be various combinations including superheated steam and reheated steam;
3) The system usually needs to be respectively configured with a heat storage flow and a heat release flow, and when the parameters of the heat storage flow and the heat release flow are matched, a loop capable of running in two directions can be used for combination;
4) The higher parameter steam generated by the system can improve the power generation efficiency of the fused salt energy storage system, and can increase the adaptability of the system when used for supplying heat.
Drawings
Fig. 1 is a schematic view of the present invention in a heat storage mode;
FIG. 2 is a schematic diagram of the present invention in a heat release mode;
in the figure: 1. the system comprises a low-temperature molten salt tank, a medium-temperature molten salt tank, a high-temperature molten salt tank, a low-temperature molten salt pump, a medium-temperature molten salt pump, a high-temperature molten salt pump, a drain pump, a medium-temperature loop regulating valve, a saturated steam-molten salt heat exchanger, a superheated steam-molten salt heat exchanger, a molten salt-saturated water evaporator, a molten salt-superheated steam heat exchanger, a steam-water separator and a steam-water separator, wherein the low-temperature molten salt tank, the medium-temperature molten salt tank, the 3 high-temperature molten salt tank, the 4 low-temperature molten salt pump, the 5 medium-temperature molten salt pump, the 6 high-temperature molten salt pump, the 7 drain pump, the 8 medium-temperature loop regulating valve, 9 the saturated steam-molten salt heat exchanger, 10 the superheated steam-molten salt heat exchanger, 11 the molten salt-saturated water evaporator, 12 the molten salt-superheated steam heat exchanger, 13 and the steam-water separator.
Detailed Description
The technical solution of the present invention is further described in detail by the following specific embodiments in combination with the accompanying drawings:
the embodiment is as follows: as shown in fig. 1 and 2, a multi-tank molten salt energy storage system based on energy cascade utilization includes a low-temperature molten salt tank 1, a medium-temperature molten salt tank 2, a high-temperature molten salt tank 3, a low-temperature molten salt pump 4, a medium-temperature molten salt pump 5, a high-temperature molten salt pump 6, a drain pump 7, a medium-temperature loop regulating valve 8, a saturated steam-molten salt heat exchanger 9, an superheated steam-molten salt heat exchanger 10, a molten salt-saturated water evaporator 11, a molten salt-superheated steam heat exchanger 12, and a steam-water separator 13.
The heat storage working mode of the system is shown in figure 1:
the molten salt in the low-temperature molten salt tank 1 is pumped out by a low-temperature molten salt pump 4, enters a saturated steam-molten salt heat exchanger 9, absorbs heat released by saturated steam, and is heated to become medium-temperature molten salt. Most of the medium-temperature molten salt enters the medium-temperature molten salt tank 2 for storage, and the rest of the medium-temperature molten salt enters the superheated steam-molten salt heat exchanger 10 to absorb heat released by the superheated steam to become high-temperature molten salt, and the high-temperature molten salt enters the high-temperature molten salt tank 3 for storage. The proportion of the molten salt entering the medium-temperature molten salt tank 2 and the high-temperature molten salt tank 3 is mainly completed by a medium-temperature loop regulating valve 8.
The steam source of the superheated steam-molten salt heat exchanger 10 is usually a single-path superheated steam, and may also be a multi-path steam source including superheated steam and reheated steam.
Through the flow, the heat released by the steam superheating section and the condensing section is respectively stored in the high-temperature molten salt tank 3 and the medium-temperature molten salt tank 2, the molten salt temperature in the high-temperature molten salt tank 3 is improved through the optimized configuration of the molten salt flow in the high-temperature molten salt loop and the medium-temperature molten salt loop, and the steam heat is stored in a stepped manner according to the quality.
Exothermic mode of operation of the system, see fig. 2:
feed water from the system enters a molten salt-saturated water evaporator 11, heat released by medium-temperature molten salt is absorbed in the evaporator to gradually realize evaporation, and a generated steam-water mixture enters a steam-water separator 13; saturated water from the steam-water separator 13 returns to the water supply system after being pressurized by the drain pump 7; saturated steam from the steam-water separator 13 enters the molten salt-superheated steam heat exchanger 12 to absorb heat released by high-temperature molten salt and change the heat into superheated steam.
In the process, the high-temperature molten salt pump 6 pumps the high-temperature molten salt from the high-temperature molten salt tank 3, and the high-temperature molten salt releases heat in the molten salt-superheated steam heat exchanger 12 to become medium-temperature molten salt; mixed with the medium-temperature molten salt pumped by the medium-temperature molten salt pump 5 from the medium-temperature molten salt tank 2, enters the molten salt-saturated water evaporator 11, is changed into low-temperature molten salt after releasing heat, and returns to the low-temperature molten salt tank 1.
Through the process, in the heat release process of the molten salt energy storage system, the superheat section corresponds to high-temperature molten salt, the evaporation section corresponds to medium-temperature molten salt, and gradient utilization of energy is realized, so that steam with higher parameters can be generated, and the heat supply or power generation requirements of the subsequent flow are met.
A multi-tank molten salt energy storage system based on energy gradient utilization organically separates a steam condensation heat exchange process and an superheated steam cooling process in a heat storage process, and respectively stores heat in a medium-temperature molten salt tank and a high-temperature molten salt tank through distribution of molten salt flow to realize gradient storage of energy; in the heat release process, the evaporation and overheating processes of water respectively correspond to the heat release processes of medium-temperature molten salt and high-temperature molten salt, and the gradient utilization of energy is realized.
By the above energy storage scheme, the system can generate steam with higher parameters. When the power generation device is used for doing work and generating power, the output power and the power generation efficiency of the system can be improved; when the steam heating device is used for heating, higher steam parameters can adapt to more heat utilization scenes. The energy storage scheme eliminates the defects of a double-tank molten salt system, and has wide application prospects in the fields of thermal power unit deep peak regulation, industrial heat supply, steam power generation, waste heat utilization and the like.
The above-described embodiment is only a preferred embodiment of the present invention, and is not intended to limit the present invention in any way, and other variations and modifications may be made without departing from the scope of the invention as set forth in the claims.
Claims (5)
1. A multi-tank molten salt energy storage system based on energy gradient utilization is characterized by comprising not less than three molten salt storage tanks with different temperatures, a steam-molten salt heat exchange system for storing heat and a molten salt-steam heat exchange system for releasing heat, wherein the molten salt storage tanks with different temperatures are arranged according to the quality of steam in the heat storage process, the steam-molten salt heat exchange system for storing heat is provided with a saturated steam-molten salt heat exchanger and an overheated steam-molten salt heat exchanger, the saturated steam-molten salt heat exchanger or the overheated steam-molten salt heat exchanger is respectively arranged between pipelines communicated with the molten salt storage tanks with different temperatures, the heat released by a steam condensation section and an overheating section in a steam pipeline is absorbed through heat exchange and stored in molten salt storage tanks with different temperatures, the heat is stored in a grading manner according to the quality, in the heat release process, a molten salt-steam heat exchange system for releasing heat is provided with a molten salt-saturated water evaporator and a molten salt-overheated steam heat exchanger, a molten salt-saturated water evaporator or a molten salt-overheated steam heat exchanger is arranged between pipelines communicated with the molten salt storage tanks with different temperatures, the condensed water in a water supply pipeline absorbs the heat through the heat exchange of the molten salt-saturated water evaporator and is gradually evaporated, the evaporated saturated steam enters the molten salt-overheated steam heat exchanger and is continuously subjected to heat exchange absorption to generate high-parameter steam and then is conveyed to a power generation or heat supply system.
2. The multi-tank molten salt energy storage system based on energy cascade utilization is characterized in that the molten salt storage tanks with different temperatures not less than three comprise a low-temperature molten salt tank, a middle-temperature molten salt tank and a high-temperature molten salt tank, molten salt is extracted from the low-temperature molten salt tank in the heat storage process to absorb heat released by saturated steam, most of the generated middle-temperature molten salt returns to the middle-temperature molten salt tank, a part of the molten salt is further subjected to heat absorption and temperature rise in an overheat steam-molten salt heat exchanger to form high-temperature molten salt, the high-temperature molten salt tank returns the high-temperature molten salt tank to store the heat in a grading manner according to quality, during the heat release process, condensed water absorbs the heat released by the middle-temperature molten salt in a molten salt-saturated water evaporator and is gradually evaporated, the generated saturated steam enters the molten salt-overheat steam heat exchanger to continuously absorb the heat released by the high-temperature molten salt to generate high-parameter steam, and the high-parameter steam is conveyed to a power generation or heat supply system, a part of the middle-temperature molten salt comes from the middle-temperature molten salt storage tank, and a part of the high-temperature molten salt after heat release.
3. The multi-tank molten salt energy storage system based on energy cascade utilization is characterized in that the molten salt-steam heat exchange system for releasing heat is further provided with a steam-water separation device or a steam drum, condensed water absorbs heat in a molten salt-saturated water evaporator and is gradually evaporated, and a generated steam-water mixture enters the steam-water separation device; and the saturated steam after steam-water separation enters a fused salt-superheated steam heat exchanger, and the condensed water after steam-water separation enters a fused salt-saturated water evaporator again to absorb heat.
4. The multi-tank molten salt energy storage system based on energy cascade utilization is characterized in that the steam-molten salt heat exchange system for heat storage further comprises a reheat steam pipeline, and the reheat steam pipeline releases heat for molten salt absorption through heat exchange of a molten salt-superheated steam heat exchanger.
5. The multi-tank molten salt energy storage system based on energy cascade utilization as claimed in claim 1, wherein in the special case that parameters of a heat storage process and parameters of a heat release process are matched, the heat storage system and the heat release system can be combined through a loop capable of achieving bidirectional operation.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202210213720.0A CN114322619A (en) | 2022-03-07 | 2022-03-07 | Multi-tank molten salt energy storage system based on energy gradient utilization |
| CN2022102137200 | 2022-03-07 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN217844870U true CN217844870U (en) | 2022-11-18 |
Family
ID=81030619
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202210213720.0A Pending CN114322619A (en) | 2022-03-07 | 2022-03-07 | Multi-tank molten salt energy storage system based on energy gradient utilization |
| CN202221457393.5U Active CN217844870U (en) | 2022-03-07 | 2022-06-13 | Multi-tank molten salt energy storage system based on energy gradient utilization |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202210213720.0A Pending CN114322619A (en) | 2022-03-07 | 2022-03-07 | Multi-tank molten salt energy storage system based on energy gradient utilization |
Country Status (1)
| Country | Link |
|---|---|
| CN (2) | CN114322619A (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114718676B (en) * | 2022-04-15 | 2023-07-25 | 西安热工研究院有限公司 | Heat storage and release system for fused salt heated by coal-fired unit steam |
| CN115076678A (en) * | 2022-05-13 | 2022-09-20 | 华电电力科学研究院有限公司 | Combined cycle coupling fused salt energy storage deep peak regulation system and method thereof |
| CN114857567A (en) * | 2022-05-18 | 2022-08-05 | 西安热工研究院有限公司 | Multi-tank heat storage and release system based on generator set |
| CN115711495B (en) * | 2022-11-16 | 2023-09-12 | 中国核动力研究设计院 | Energy storage power station and system special for power grid peak shaving |
| CN116379831B (en) * | 2023-04-04 | 2024-08-02 | 华北电力大学 | Control method, device, equipment and storage medium of heat storage system |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1286050B (en) * | 1959-07-03 | 1969-01-02 | Siemens Ag | Control device for steam power plants with forced flow boiler |
| CN107100684A (en) * | 2017-04-19 | 2017-08-29 | 百吉瑞（天津）新能源有限公司 | A kind of steam power plant utilizes boiler bypass depth of round peak regulation modernization system |
| CN207004745U (en) * | 2017-07-28 | 2018-02-13 | 中国电力工程顾问集团西北电力设计院有限公司 | A kind of full load fused salt steam generating system |
| CN207795526U (en) * | 2017-12-08 | 2018-08-31 | 泉州装备制造研究所 | A kind of compressed-air energy-storage system forcing precooling suitable for peak load regulation network band |
-
2022
- 2022-03-07 CN CN202210213720.0A patent/CN114322619A/en active Pending
- 2022-06-13 CN CN202221457393.5U patent/CN217844870U/en active Active
Also Published As
| Publication number | Publication date |
|---|---|
| CN114322619A (en) | 2022-04-12 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN217844870U (en) | Multi-tank molten salt energy storage system based on energy gradient utilization | |
| CN108561282B (en) | Trough type direct steam and molten salt combined thermal power generation system | |
| CN103953402A (en) | Solar energy and biomass energy combined power generation optimizing integrated system | |
| CN103912464A (en) | Combined solar heat and BIGCC power generation system | |
| CN113669715B (en) | Energy storage peak shaving system suitable for reheating unit steam heating fused salt | |
| CN108518324A (en) | A kind of tower type solar photo-thermal coupling coal generating system with accumulation of energy | |
| CN110273722A (en) | A kind of thermal power plant's concrete heat accumulation peak regulation system and method | |
| CN101846044A (en) | Solar heat collection, energy storage and back heating system applied to thermal generator set | |
| CN113503531A (en) | Multi-power-supply heat storage peak regulation power station for coal-fired power plant transformation and peak regulation method | |
| CN102878036A (en) | Solar energy-gas turbine combined cycle cogeneration system | |
| CN201637131U (en) | Solar heat collection and energy storage regenerative heating device for thermal generator set | |
| CN111456818A (en) | Double-source heating fused salt energy storage system of thermal power plant | |
| CN204003297U (en) | The combined generating system that solar energy optical-thermal and BIGCC are integrated | |
| CN109026240B (en) | Power generation system and method based on nuclear energy and solar energy coupling | |
| CN203867640U (en) | Optimized integrated system for combined power generation of solar energy and biomass energy | |
| CN108980616B (en) | Long-distance industrial steam supply system for intermittent steam use users | |
| CN208349609U (en) | A kind of photo-thermal fused salt accumulation of heat light coal coupled system | |
| CN203081667U (en) | Solar and fossil fueled plant complemental circulating device | |
| CN215174935U (en) | High-low temperature heat storage peak shaving system of thermal power plant | |
| CN215808405U (en) | Multi-power-supply heat-storage peak-regulation power station reconstructed from coal-fired power plant | |
| CN115405390A (en) | Pressurized water reactor power generation, energy storage, seawater desalination and refrigeration coupled operation system and method | |
| CN214664318U (en) | Fused salt energy storage power station system | |
| CN212318103U (en) | Double-source heating fused salt energy storage system of thermal power plant | |
| CN108870503B (en) | Waste heat comprehensive utilization system for long-distance industrial steam supply of intermittent steam utilization users | |
| CN208703575U (en) | A kind of long range industry steam-supplying system for using vapour user for intermittence |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |