CN110243085B - Double-high-temperature molten salt storage tank system of solar thermal power station - Google Patents
Double-high-temperature molten salt storage tank system of solar thermal power station Download PDFInfo
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- CN110243085B CN110243085B CN201910440281.5A CN201910440281A CN110243085B CN 110243085 B CN110243085 B CN 110243085B CN 201910440281 A CN201910440281 A CN 201910440281A CN 110243085 B CN110243085 B CN 110243085B
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24S—SOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
- F24S60/00—Arrangements for storing heat collected by solar heat collectors
- F24S60/30—Arrangements for storing heat collected by solar heat collectors storing heat in liquids
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24S—SOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
- F24S50/00—Arrangements for controlling solar heat collectors
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24S—SOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
- F24S80/00—Details, accessories or component parts of solar heat collectors not provided for in groups F24S10/00-F24S70/00
- F24S80/30—Arrangements for connecting the fluid circuits of solar collectors with each other or with other components, e.g. pipe connections; Fluid distributing means, e.g. headers
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- 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
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Abstract
The invention discloses a solar thermal power station double-high-temperature molten salt storage tank system and application thereof, wherein the system comprises a first molten salt storage tank, a second molten salt storage tank, a first molten salt storage tank communicating pipeline, a second molten salt storage tank communicating pipeline and a molten salt inlet; the first molten salt storage tank communicating pipeline is led out from the first molten salt storage tank and is communicated with the molten salt inlet, and the second molten salt storage tank communicating pipeline is led out from the second molten salt storage tank and is communicated with the molten salt inlet; a first control valve is arranged on the first molten salt storage tank communicating pipeline, and a second control valve is arranged on the second molten salt storage tank communicating pipeline; the molten salt pump-out device is used for pumping out high-temperature molten salt; the molten salt pump-out device is respectively connected with the first molten salt storage tank and the second molten salt storage tank. When one of the molten salt storage tanks leaks, the molten salt storage tank can be emptied and overhauled, and the other high-temperature molten salt storage tank is started to normally generate power. Two high temperature fused salt storage tanks are each other for reserve, have guaranteed the stability and the security of light and heat power station electricity generation.
Description
Technical Field
The invention relates to the field of solar thermal power generation, in particular to a high-temperature molten salt storage tank system of a solar thermal power station.
Background
Solar high-temperature thermal power generation technology is an important direction for solar scale utilization. The working media adopted by the solar high-temperature thermal power generation include water (steam), molten salt, air, heat conduction oil, liquid metal, other heat conduction media and the like. Due to the fluctuation and discontinuity of solar illumination, a large-scale heat storage system is required in the solar photo-thermal power generation system to continuously and stably generate power. The fused salt has the characteristics of high use temperature, wide temperature range, good flow characteristic, large heat capacity and the like, can just make up the problem of unstable solar illumination when being applied to a heat storage system as a heat storage working medium, and is the most widely applied solar heat storage working medium at present.
The equipment for storing the heat storage medium molten salt is called a storage tank, the storage tank for storing the hot molten salt is called a hot salt tank, and the storage tank for storing the cold molten salt is called a cold salt tank. The storage tank is composed of a storage tank bottom plate, a storage tank edge plate, a storage tank wall plate, a storage tank vault, a storage tank foundation and the like.
Traditional storage tank adopts the individual layer jar to a storage tank for light and heat power station is often bulky, and the temperature alternation is frequent, and the load that the storage tank bore is complicated and unstable, consequently, the storage tank has very big possibility to take place to become invalid, leads to the fused salt to reveal. The existing American Crescent Dunes and the existing Gemasular photothermal power stations in Spain are caused to stop for a long time due to the leakage of storage tanks, and serious economic loss is caused. Meanwhile, the storage tank is huge in size, the adopted molten salt pump is often a high-temperature-resistant long-shaft vertical pump, and the molten salt pump is often high in cost and inconvenient to maintain.
Disclosure of Invention
Aiming at the problems in the prior art, the invention provides a solar thermal power station double-high-temperature molten salt storage tank system.
The technical scheme of the invention is as follows:
a solar photo-thermal power station double-high-temperature molten salt storage tank system comprises a first molten salt storage tank [5], a second molten salt storage tank [6], a first molten salt storage tank communicating pipeline [21], a second molten salt storage tank communicating pipeline [31], a first control valve [2], a second control valve [3] and a molten salt inlet [1 ]; wherein the content of the first and second substances,
the first molten salt storage tank communicating pipeline [21] is led out from the first molten salt storage tank [5] and is communicated with the molten salt inlet [1], and the second molten salt storage tank communicating pipeline [31] is led out from the second molten salt storage tank [6] and is communicated with the molten salt inlet [1 ];
a first control valve [2] is arranged on the first molten salt storage tank communicating pipeline [21], and a second control valve [3] is arranged on the second molten salt storage tank communicating pipeline [31 ];
the molten salt pump-out device is used for pumping out high-temperature molten salt; the molten salt pumping-out device is respectively connected with the first molten salt storage tank [5] and the second molten salt storage tank [6 ].
Preferably, the molten salt pumping-out device is a molten salt pump; a molten salt outlet is respectively arranged above the vault of the first molten salt storage tank and the vault of the second molten salt storage tank, a molten salt pump is respectively arranged above the molten salt outlet of the first molten salt storage tank and the molten salt outlet of the second molten salt storage tank, and high-temperature molten salt is pumped out through the molten salt pumps; the molten salt pump is a long-shaft vertical pump.
Preferably, the molten salt pumping-out device is a small-volume molten salt tank, a molten salt pump is arranged on the small-volume molten salt tank, and the molten salt pump is longer than the vertical pump; the small-volume molten salt tank is connected with the first molten salt storage tank and the second molten salt storage tank through a fourth communicating pipeline and a fifth communicating pipeline respectively, a fourth control valve is arranged on the communicating pipelines, and a fifth control valve is arranged on the fifth communicating pipeline; the foundation of the small-volume molten salt tank is lower than the foundation of the first molten salt storage tank and the second molten salt storage tank; and high-temperature molten salt flows into the small-volume molten salt tank through the fourth communicating pipeline and the fifth communicating pipeline and is pumped out through a molten salt pump of the small-volume molten salt tank.
Preferably, the number of the small-volume molten salt tanks is one, and the small-volume molten salt tank [13] is communicated with the first molten salt storage tank [5] through a fourth communication pipeline [15] and is communicated with the second molten salt storage tank [6] through a fifth communication pipeline [11 ].
Preferably, the first molten salt storage tank [5] and the second molten salt storage tank [6] are respectively connected with at least one small-volume molten salt tank.
Preferably, the tank foundation of the first molten salt storage tank [5] is higher than that of the second molten salt storage tank [6], and the height difference H between the two is greater than or equal to the lowest starting liquid level height of the molten salt pump of the second molten salt storage tank [6 ]; the first molten salt storage tank [5] is connected with the second molten salt storage tank [6] through a third communicating pipeline [9], and a control valve [8] is arranged on the third communicating pipeline [9 ]; the high-temperature molten salt in the first molten salt storage tank [5] can flow into the second molten salt storage tank [6] through the communicating pipeline [9 ].
Preferably, storage tank flow equalizing devices are respectively arranged in the first molten salt storage tank and the second molten salt storage tank, and each storage tank flow equalizing device is respectively connected with the communication pipeline of the first molten salt storage tank or the communication pipeline of the second molten salt storage tank. The detailed structure of the storage tank flow equalizing device can be seen in CN207894055U, a salt feeding device and a system of a molten salt storage tank.
Preferably, the storage tank flow equalizing devices are respectively arranged at positions close to the bottom plate of the first molten salt storage tank and the bottom plate of the second molten salt storage tank.
Preferably, one end of a third communicating pipeline [9] of the first molten salt storage tank [5] and the second molten salt storage tank [6] is arranged at the position, close to the bottom plate, of the first molten salt storage tank [5], and the other end of the third communicating pipeline is arranged in the second molten salt storage tank [6] and is connected with a storage tank flow equalizing device.
Preferably, the fourth communication pipeline of the first molten salt storage tank [5] and the small-volume molten salt tank, and the fifth communication pipeline of the second molten salt storage tank [6] and the small-volume molten salt tank are arranged into a horizontal pi-shaped bent structure.
Preferably, the third communicating duct [9] is arranged in a horizontal pi-shaped bent structure.
Preferably, a control valve on a pipeline between the small-volume molten salt tank and the first molten salt storage tank [5] and a control valve on a pipeline between the small-volume molten salt tank and the second molten salt storage tank [6] need to control the flow of molten salt entering the molten salt tank 13, so that the liquid level in the molten salt tank 13 is ensured to be stabilized in a reasonable interval.
Preferably, the first molten salt storage tank 5, the second molten salt storage tank 6 and the molten salt tank 13 are made of 347H materials.
The application of the high-low-position high-temperature molten salt storage tank system comprising the solar photo-thermal power station in solar thermal power generation.
Compared with the prior art, the invention has the beneficial effects that:
1. according to the invention, a double high-temperature molten salt storage tank system is adopted, the two storage tanks are mutually standby, once one of the two storage tanks leaks, the other high-temperature storage tank can normally work, the system operation is not influenced, the maintenance is convenient, and the stability and the safety of the power generation of the photo-thermal power station are ensured.
2. According to the scheme of the high-low level fused salt storage tank, the two storage tanks have height difference, fused salt in the high-temperature fused salt storage tank flows to the low-temperature fused salt storage tank through the bottom pipeline, the fused salt liquid level of the high-level fused salt storage tank can be lower than the lowest starting liquid level of the fused salt pump on the high-level fused salt storage tank, the weight of unusable salt in the high-level fused salt storage tank due to the lowest starting liquid level of the fused salt pump is reduced, the quality of usable high-temperature fused salt in a system is improved, and the integral power generation capacity of.
3. The invention can adopt the combination of the small-volume molten salt tank and the molten salt pump with shorter length to replace the function of the long-shaft vertical molten salt pump with higher cost on the molten salt storage tank, thereby facilitating the overhaul and maintenance of the molten salt pump, enhancing the reliability of the system and greatly reducing the cost.
4. The ground height of the high higher level fused salt storage tank or the low level fused salt storage tank of small volume fused salt groove ground is low, can further reduce because the minimum start-up liquid level of fused salt pump leads to can not utilize salt weight, improves the holistic income in power station.
Of course, it is not necessary for any product in which the invention is practiced to achieve all of the above-described advantages at the same time.
Drawings
FIG. 1 is a schematic diagram of a high and low molten salt storage tank system according to example 1 of the present invention;
FIG. 2 is a schematic diagram of a high-low molten salt storage tank system according to embodiment 2 of the invention.
Reference numerals: 1-high temperature molten salt inlet; 2-a molten salt inlet control valve of a high-level molten salt storage tank; 3-a molten salt inlet control valve of the low-level molten salt storage tank; 21-a communicating conduit; 31-a communicating conduit; 4-molten salt outlet; 5-high molten salt storage tank; 6-low-level molten salt storage tank; 7-storage tank flow equalizing device; 72-tank flow straightener; 8-control valve; 9-a third communicating pipe; 10-control valve; 11-a fifth communicating pipe; 12-a molten salt tank molten salt pump; 13-molten salt tank; 14-a control valve; 15-fourth communicating conduit.
Detailed Description
For a better understanding of the present invention, reference is made to the following detailed description taken in conjunction with the accompanying drawings. In the following embodiments, the high-level molten salt storage tank is also referred to as a high-level storage tank, the low-level molten salt storage tank is also referred to as a low-level storage tank, and the low-temperature molten salt storage tank is also referred to as a cold tank.
Example 1
As shown in figure 1, a high low level high temperature fused salt storage tank system of solar photothermal power station, including high-order fused salt storage tank 5, low level fused salt storage tank 6, high-order fused salt storage tank communicating pipe 21, low level fused salt storage tank communicating pipe 31, first control valve 2, second control valve 3 and fused salt entry 1, first control valve 2 sets up on fused salt entry 1 and the communicating pipe 21 between high-order fused salt storage tank 5, second control valve 3 sets up on fused salt entry 1 and the communicating pipe 31 between low level fused salt storage tank 6, high level fused salt storage tank 5 and 6 vault tops of low level fused salt storage tank set up fused salt export 4 respectively, fused salt export 4 tops respectively have a fused salt pump.
Wherein, the storage tank basis of the lower level fused salt storage tank 6 of the storage tank basis of high level fused salt storage tank 5 is high, and the difference in height H between them is greater than or equal to the minimum starting liquid level height of the fused salt pump of low level fused salt storage tank 6. The arrangement enables the molten salt which cannot be utilized at the bottom of the high-level storage tank to flow into the low-level storage tank through the communication pipeline, so that the weight of the molten salt which cannot be utilized in the system is reduced.
The high-level molten salt storage tank 5 and the low-level molten salt storage tank 6 are connected through a third communicating pipeline 9, and a third control valve 8 is arranged on the third communicating pipeline 9.
The communicating pipeline 21 is connected with the storage tank flow equalizing device 7 at a position close to the bottom plate in the high-level molten salt storage tank 5, and the communicating pipeline 31 is connected with the storage tank flow equalizing device 72 at a position close to the bottom plate in the low-level molten salt storage tank 6. One end of the third communicating pipeline 9 is arranged at the position of the high-level molten salt storage tank 5 close to the bottom plate, and the other end of the third communicating pipeline is arranged in the low-level molten salt storage tank 6 and is connected with the storage tank flow equalizing device 72. When the system is in operation, the third control valve 8 on the third communicating pipeline 9 is in a closed state.
Preferably, the third communication duct 9 is arranged in a horizontal pi-bend configuration to counteract the stresses caused by the thermal expansion deformations of the tank.
In this embodiment, 347H is preferably used as the material of the bodies of the high-level molten salt storage tank 5 and the low-level molten salt storage tank 6.
When the solar thermal power station high-low-level high-temperature molten salt storage tank system of the embodiment normally operates, the heat collector finishes absorbing high-temperature molten salt to enter the low-level molten salt storage tank 6 through the high-temperature molten salt inlet 1 and stores the high-temperature molten salt in the storage tank. When power generation is needed, high-temperature molten salt is pumped out by a molten salt pump above the molten salt outlet 4 of the low-level molten salt storage tank 6, and returns to the low-temperature molten salt storage tank after heat exchange of the heat exchange system. The high-level molten salt storage tank 5 is used for standby at this time.
When the low-level storage tank 6 fails and leaks, the molten salt pump of the low-level storage tank 6 is started, molten salt in the low-level storage tank 6 enters the cold tank through heat exchange of the heat exchange system, the low-level storage tank 6 is emptied and overhauled, and the high-level storage tank 5 and the cold tank normally run to generate power.
When the high-order fused salt storage tank 5 became invalid and took place to leak, the fused salt pump of low-order fused salt storage tank 6 was started, and the fused salt got to the heat transfer system heat transfer and got into cold jar in the low-order fused salt storage tank 6, opened pipeline third control valve 8 simultaneously, and the fused salt got into low-order fused salt storage tank 6 in the high-order fused salt storage tank 5, and the evacuation of high-order fused salt storage tank 5 was overhauld, closed third control valve 8 simultaneously. And the low-level molten salt storage tank 6 and the cold tank normally operate to generate power.
Or when the high-level molten salt storage tank 5 fails and leaks, the third control valve 8 of the pipeline is closed, the molten salt pump of the high-level molten salt storage tank 5 is started, the molten salt in the high-level molten salt storage tank 5 is sent to the heat exchange system for heat exchange and enters the cold tank, and the high-level molten salt storage tank 5 is emptied and overhauled. And the low-level molten salt storage tank 6 and the cold tank normally operate to generate power.
In the present embodiment, the tank foundation of the high-level tank 5 and the tank foundation of the low-level tank 6 have a height difference, but in other embodiments, the height difference may not exist, and the high-level tank 5 and the low-level tank 6 have the same tank foundation.
Example 2
In this embodiment, compared with embodiment 1, the solar photothermal power station high-low-level high-temperature molten salt storage tank system is additionally provided with a small-volume molten salt tank 13, the molten salt tank 13 is connected with the high-level molten salt storage tank 5 through a fourth communicating pipeline 15, and is connected with the low-level molten salt storage tank 6 through a fifth communicating pipeline 11, the fourth communicating pipeline 15 is provided with a fourth control valve 14, and the fifth communicating pipeline 11 is provided with a fifth control valve 10. The molten salt tank 13 is provided with a molten salt pump 12, and the molten salt pump 12 is shorter than the vertical pump. The foundation of the high-level molten salt storage tank 5 and the low-level molten salt storage tank 6 is higher than that of the molten salt tank 13.
When the system normally operates, the molten salt in the low-level molten salt storage tank 6 enters the molten salt tank 13 through the fifth communication pipeline 11, is pumped out by the molten salt pump 12 and enters the heat exchange system for heat exchange. The fifth control valve 10 needs to control the flow of the molten salt entering the molten salt tank 13, so as to ensure that the liquid level in the molten salt tank 13 is stabilized in a reasonable interval.
When the high-level molten salt storage tank 5 fails and leaks, the fourth control valve 14 of the high-level molten salt storage tank 5 and the molten salt tank is opened, the fifth control valve 10 of the molten salt tank 13 and the low-level molten salt storage tank 6 is closed, the high-temperature molten salt flows to the molten salt tank 13 through the fourth communicating pipeline 15, and the molten salt is drained and overhauled through the molten salt pump 12. The fourth control valve 14 of the pipeline needs to control the flow of the molten salt entering the molten salt tank 13, so as to ensure that the liquid level in the molten salt tank is stabilized in a reasonable interval. After evacuation, the fourth control valve 14 is closed. The low-level molten salt storage tank 6 and the molten salt tank 13 normally operate, and the power generation of the power station is not influenced.
When the low-level molten salt storage tank 6 fails and leaks, the fifth control valve 10 of the low-level molten salt storage tank 6 and the molten salt tank is opened, the fourth control valve 14 of the molten salt tank 13 and the high-level storage tank 5 is closed, high-temperature molten salt flows to the molten salt tank 13 through the fifth communication pipeline 11, and the molten salt is emptied and overhauled through the molten salt pump 12. After evacuation, the fifth control valve 10 is closed. The high-level storage tank 5 and the molten salt tank 13 normally operate, and the power generation of the power station is not influenced.
Because the volume ratio of light and heat power station storage tank is bigger, therefore the molten salt pump that adopts on the storage tank is the major axis vertical pump, and this pump is higher to the technology and the precision requirement of processing, therefore its cost is also higher. Meanwhile, the pump body is longer and goes deep into the storage tank, so that the maintenance and overhaul of the pump are difficult. In this embodiment, the system has cancelled the molten salt pump on high-order molten salt storage tank 5 and the low level molten salt storage tank 6, adopts small volume molten salt groove and the shorter molten salt pump of length to combine to replace, has greatly reduced the holistic cost of system, is convenient for simultaneously the maintenance and the maintenance of molten salt pump. When the molten salt pump 12 on the molten salt tank 13 needs to be overhauled or maintained, the fifth control valve 10 and the fourth control valve 14 are closed at the same time, molten salt in the molten salt tank 13 is emptied, the overhaul and maintenance of the molten salt pump can be carried out, and the reliability and stability of the system are enhanced. In order to further ensure the stability of the system operation, a molten salt pump can be respectively arranged above the molten salt outlets of the high-level storage tank and the low-level storage tank; a communicating pipeline can be arranged between the high-level storage tank and the low-level storage tank, and a control valve is arranged on the communicating pipeline.
In the present embodiment, the number of the small-volume molten salt bath 13 is set to one, but the present invention is not limited to the number of the small-volume molten salt bath 13, and those skilled in the art can select other numbers of the small-volume molten salt bath 13 to set them according to simple modifications.
The preferred embodiments of the invention disclosed above are intended to be illustrative only. The preferred embodiments are not intended to be exhaustive or to limit the invention to the precise embodiments disclosed. Obviously, many modifications and variations are possible in light of the above teaching. The embodiments were chosen and described in order to best explain the principles of the invention and the practical application, to thereby enable others skilled in the art to best utilize the invention. The invention is limited only by the claims and their full scope and equivalents.
Claims (6)
1. A solar photo-thermal power station double-high-temperature molten salt storage tank system is characterized by comprising a first molten salt storage tank [5], a second molten salt storage tank [6], a first molten salt storage tank communicating pipeline [21], a second molten salt storage tank communicating pipeline [31], a first control valve [2], a second control valve [3] and a molten salt inlet [1 ]; wherein the content of the first and second substances,
the first molten salt storage tank communicating pipeline [21] is led out from the first molten salt storage tank [5] and is communicated with the molten salt inlet [1], and the second molten salt storage tank communicating pipeline [31] is led out from the second molten salt storage tank [6] and is communicated with the molten salt inlet [1 ];
a first control valve [2] is arranged on the first molten salt storage tank communicating pipeline [21], and a second control valve [3] is arranged on the second molten salt storage tank communicating pipeline [31 ];
the molten salt pump-out device is used for pumping out high-temperature molten salt; the molten salt pumping-out device is respectively connected with the first molten salt storage tank [5] and the second molten salt storage tank [6 ];
the tank foundation of the first molten salt storage tank [5] is higher than that of the second molten salt storage tank [6], and the height difference H between the two is larger than or equal to the lowest starting liquid level height of the molten salt pump of the second molten salt storage tank [6 ]; the first molten salt storage tank [5] is connected with the second molten salt storage tank [6] through a third communicating pipeline [9], and a third control valve [8] is arranged on the third communicating pipeline [9 ]; the high-temperature molten salt in the first molten salt storage tank [5] can flow into the second molten salt storage tank [6] through the third communicating pipeline [9], so that the weight of the unavailable molten salt in the system is reduced.
2. The solar photothermal power station dual high temperature molten salt storage tank system of claim 1 wherein said molten salt pumping out device is a molten salt pump; a molten salt outlet is respectively arranged above the vault of the first molten salt storage tank and the vault of the second molten salt storage tank, a molten salt pump is respectively arranged above the molten salt outlet of the first molten salt storage tank and the molten salt outlet of the second molten salt storage tank, and high-temperature molten salt is pumped out through the molten salt pumps; the molten salt pump is a long-shaft vertical pump.
3. The dual-high-temperature molten salt storage tank system of the solar photothermal power station of claim 1 or 2, wherein storage tank flow equalizing devices are respectively arranged in the first molten salt storage tank and the second molten salt storage tank, and each storage tank flow equalizing device is respectively connected with the first molten salt storage tank communicating pipeline or the second molten salt storage tank communicating pipeline; the storage tank flow equalizing device is respectively arranged at the position close to the bottom plate of the first molten salt storage tank and the position close to the bottom plate of the second molten salt storage tank.
4. The solar thermal power station double-high-temperature molten salt storage tank system according to claim 3, wherein one end of a third communication pipeline [9] between the first molten salt storage tank and the second molten salt storage tank is arranged at a position, close to the bottom plate, of the first molten salt storage tank [5], and the other end of the third communication pipeline is arranged in the second molten salt storage tank [6] and is connected with a storage tank flow equalizing device.
5. The solar photothermal power station double high temperature molten salt storage tank system according to claim 1, wherein said third communicating pipe [9] is arranged in a horizontal pi-shaped bent structure.
6. Use of a dual high temperature molten salt storage tank system comprising a solar photothermal power station according to any of claims 1-5 in solar thermal power generation.
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| CN202011347399.2A CN113218093B (en) | 2019-05-24 | 2019-05-24 | Double-high-temperature molten salt storage tank system of solar thermal power station and application thereof |
| CN201910440281.5A CN110243085B (en) | 2019-05-24 | 2019-05-24 | Double-high-temperature molten salt storage tank system of solar thermal power station |
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| CN110701801A (en) * | 2019-09-27 | 2020-01-17 | 浙江中控太阳能技术有限公司 | Fused salt conveying system for solar photo-thermal power station |
| CN111879019B (en) * | 2020-06-12 | 2022-03-18 | 浙江大学 | System for detecting fused salt leakage of photo-thermal power generation heat storage device by utilizing electrode plate |
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| CN207894055U (en) * | 2017-12-06 | 2018-09-21 | 浙江中控太阳能技术有限公司 | A kind of fused salt storage tank into salt apparatus and system |
| CN207865731U (en) * | 2017-12-29 | 2018-09-14 | 中国电力工程顾问集团西北电力设计院有限公司 | A kind of solar energy thermo-power station fused salt storage tank system |
| CN207975662U (en) * | 2018-02-06 | 2018-10-16 | 湛江电力有限公司 | A kind of boiler reheated steam soot blowing vapour source draws vapour device |
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2019
- 2019-05-24 CN CN201910440281.5A patent/CN110243085B/en active Active
- 2019-05-24 CN CN202011347399.2A patent/CN113218093B/en active Active
Also Published As
| Publication number | Publication date |
|---|---|
| CN113218093A (en) | 2021-08-06 |
| CN110243085A (en) | 2019-09-17 |
| CN113218093B (en) | 2023-03-31 |
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