CN116558341A - A thermal storage spherical tank water distributor - Google Patents
A thermal storage spherical tank water distributor Download PDFInfo
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- CN116558341A CN116558341A CN202310097685.5A CN202310097685A CN116558341A CN 116558341 A CN116558341 A CN 116558341A CN 202310097685 A CN202310097685 A CN 202310097685A CN 116558341 A CN116558341 A CN 116558341A
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D20/00—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
- F28D20/0034—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using liquid heat storage material
- F28D20/0039—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using liquid heat storage material with stratification of the heat storage material
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D20/00—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F25/00—Component parts of trickle coolers
- F28F25/02—Component parts of trickle coolers for distributing, circulating, and accumulating liquid
- F28F25/04—Distributing or accumulator troughs
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D20/00—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
- F28D2020/0065—Details, e.g. particular heat storage tanks, auxiliary members within tanks
- F28D2020/0069—Distributing arrangements; Fluid deflecting means
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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
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/14—Thermal energy storage
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Pump Type And Storage Water Heaters (AREA)
Abstract
本发明提出了一种蓄热式球罐布水器,包括球罐本体,以及分别布置在所述球罐本体内腔上部的上布水器、内腔下部的下布水器,所述上布水器包括若干个第一布水管,以及与各第一布水管相连通的第一进出水管,所述下布水器包括若干个第二布水管,以及与各第二布水管相连通的第二进出水管,各第一布水管、第二布水管上均设有若干个喷射结构。利用水介质在不同温度下的密度差异特性,高温水的密度小,低温水的密度大,可实现冷热同罐布置,使用中可减少球罐数量,减少项目投资。
The present invention proposes a thermal storage type spherical tank water distributor, which includes a spherical tank body, an upper water distributor arranged on the upper part of the inner cavity of the spherical tank body, and a lower water distributor arranged at the lower part of the inner cavity. The water distributor includes several first water distribution pipes, and the first water inlet and outlet pipes connected with each first water distribution pipe, and the lower water distributor includes several second water distribution pipes, and the first water distribution pipes connected with each second water distribution pipe The second water inlet and outlet pipes, each of the first water distribution pipe and the second water distribution pipe are provided with several spraying structures. Utilizing the density difference characteristics of the water medium at different temperatures, the density of high-temperature water is small, and the density of low-temperature water is large, so that the arrangement of cold and hot tanks can be realized, and the number of spherical tanks can be reduced during use, reducing project investment.
Description
【技术领域】【Technical field】
本发明涉及球罐蓄热的技术领域,特别是一种蓄热式球罐布水器。The invention relates to the technical field of spherical tank heat storage, in particular to a heat storage type spherical tank water distributor.
【背景技术】【Background technique】
目前大型低谷电储能项目有抽水蓄能电站、飞轮储能、压缩空气储能等等,总体来说压缩空气储能存在一定的优势。压缩空气储能系统中涉及高温热水的蓄热,利用空气压缩过程产生的热量通过换热器产生高温热水进行储存,当高压空气通过透平做功发电时释放热水中热量加热压缩空气,该系统热量的利用,可有效提高储能电站的发电效率。此外,利用低谷电进行高温蓄热,也可以应用于采暖等场合。大型高温高压蓄热系统采用球罐蓄热比较经济,占地面积也小。因此高温热水的蓄热、放热至关重要,直接影响电站的效率和经济性。At present, large-scale low-valley energy storage projects include pumped storage power stations, flywheel energy storage, compressed air energy storage, etc. Generally speaking, compressed air energy storage has certain advantages. The compressed air energy storage system involves the heat storage of high-temperature hot water. The heat generated by the air compression process is used to generate high-temperature hot water through the heat exchanger for storage. When the high-pressure air passes through the turbine to generate power, the heat in the hot water is released to heat the compressed air. The heat utilization of the system can effectively improve the power generation efficiency of the energy storage power station. In addition, the use of low-valley electricity for high-temperature heat storage can also be used in heating and other occasions. Large-scale high-temperature and high-pressure heat storage systems use spherical tanks for heat storage, which are more economical and occupy a small area. Therefore, the heat storage and heat release of high-temperature hot water are very important, which directly affects the efficiency and economy of the power station.
目前压缩空气能蓄热系统中一般采高温高压球形热水储罐。蓄热式球罐布水器的结构直接影响蓄热放热效率,没有布水器或者布水器效果不好,可能会导致球罐内部“短路”,球罐蓄热量、放热量达不到设计参数的60%。At present, high-temperature and high-pressure spherical hot water storage tanks are generally used in compressed air energy storage systems. The structure of the heat storage spherical tank water distributor directly affects the heat storage and heat release efficiency. If there is no water distributor or the water distributor is not effective, it may cause a "short circuit" inside the spherical tank, and the heat storage and heat release of the spherical tank cannot reach the design. 60% of the parameters.
【发明内容】【Content of invention】
本发明的目的就是解决现有技术中的问题,提出一种蓄热式球罐布水器,可保证球罐内蓄热介质温度均匀,确保蓄热充分;同时放热时也能保证球罐内介质充分放热。The purpose of the present invention is to solve the problems in the prior art, and propose a heat storage type spherical tank water distributor, which can ensure the uniform temperature of the heat storage medium in the spherical tank and ensure sufficient heat storage; at the same time, it can also ensure that the spherical tank The inner medium is fully exothermic.
为实现上述目的,本发明提出了一种蓄热式球罐布水器,包括球罐本体,以及分别布置在所述球罐本体内腔上部的上布水器、内腔下部的下布水器,所述上布水器包括若干个第一布水管,以及与各第一布水管相连通的第一进出水管,所述下布水器包括若干个第二布水管,以及与各第二布水管相连通的第二进出水管,各第一布水管、第二布水管上均设有若干个喷射结构。In order to achieve the above object, the present invention proposes a thermal storage type spherical tank water distributor, which includes a spherical tank body, an upper water distributor arranged on the upper part of the inner cavity of the spherical tank body, and a lower water distributor at the lower part of the inner cavity. The upper water distributor includes several first water distribution pipes, and the first water inlet and outlet pipes connected with each first water distribution pipe, and the lower water distributor includes several second water distribution pipes, and the first water distribution pipes connected with each second water distribution pipe. The second water inlet and outlet pipes connected by the water distribution pipes, and the first water distribution pipes and the second water distribution pipes are provided with several spraying structures.
作为优选,所述上布水器包括若干层沿高度方向间隔布置的第一布水管层,所述第一布水管层包括自内至外依次设置的若干个第一布水管,相邻的两个第一布水管之间通过第一连接管连通。Preferably, the upper water distributor includes several layers of first water distribution pipe layers arranged at intervals along the height direction, and the first water distribution pipe layer includes several first water distribution pipes arranged in sequence from the inside to the outside. The two first water distribution pipes are connected through the first connecting pipe.
作为优选,所述下布水器包括若干层沿高度方向间隔布置的第二布水管层,所述第二布水管层包括自内至外依次设置的若干个第二布水管,相邻的两个第二布水管之间通过第二连接管连通。As a preference, the lower water distributor includes several layers of second water distribution pipe layers arranged at intervals along the height direction, and the second water distribution pipe layer includes several second water distribution pipes arranged sequentially from the inside to the outside. The two second water distribution pipes are communicated through the second connecting pipe.
作为优选,所述第一布水管、第二布水管均采用环形圈管。As a preference, both the first water distribution pipe and the second water distribution pipe adopt annular ring pipes.
作为优选,所述第一布水管、第二布水管上分别设有若干排喷射结构。Preferably, the first water distribution pipe and the second water distribution pipe are respectively provided with several rows of spraying structures.
作为优选,所述第一布水管上的喷射结构向上倾斜设置,所述第二布水管的喷射结构向下倾斜设置,所述喷射结构与水平面成一定的角度b。Preferably, the spraying structure on the first water distribution pipe is arranged inclined upwards, the spraying structure of the second water distribution pipe is arranged inclined downward, and the spraying structure forms a certain angle b with the horizontal plane.
作为优选,所述第一布水管、第二布水管上分别设有两排喷射结构,且两排喷射结构之间成一定的角度a。Preferably, the first water distribution pipe and the second water distribution pipe are respectively provided with two rows of spraying structures, and the two rows of spraying structures form a certain angle a.
作为优选,所述喷射结构为喷射孔或喷嘴。Preferably, the injection structure is an injection hole or a nozzle.
本发明的有益效果:Beneficial effects of the present invention:
1、利用水介质在不同温度下的密度差异特性,高温水的密度小,低温水的密度大,可实现冷热同罐布置,使用中可减少球罐数量,减少项目投资。1. Using the density difference characteristics of water medium at different temperatures, the density of high-temperature water is small, and the density of low-temperature water is large, which can realize the arrangement of cold and hot tanks in the same tank, reduce the number of spherical tanks and reduce project investment during use.
2、蓄热过程,高温水从球罐顶部通过上布水器进入球罐中,逐渐把低温水从球罐底部通过下布水器排出球罐,直至球罐内全部为高温水,蓄热才结束。放热过程,低温水从球罐底部通过下布水器进入球罐中,逐渐把高温水从球罐顶部通过上布水器排出球罐,直至球罐内高温水全部输出,罐体内全部换成低温水,放热才结束。蓄热过程、放热过程,球罐内斜温层水量所占球罐总水量的3%以内。2. During the heat storage process, high-temperature water enters the spherical tank from the top of the spherical tank through the upper water distributor, and gradually discharges low-temperature water from the bottom of the spherical tank through the lower water distributor until all the high-temperature water in the spherical tank is stored. before the end. During the exothermic process, the low-temperature water enters the spherical tank from the bottom of the spherical tank through the lower water distributor, and gradually discharges the high-temperature water from the top of the spherical tank through the upper water distributor until all the high-temperature water in the spherical tank is output, and all the inside of the tank is replaced. When it becomes low-temperature water, the heat release ends. During the heat storage process and the heat release process, the thermocline water in the spherical tank accounts for less than 3% of the total water in the spherical tank.
本发明的特征及优点将通过实施例结合附图进行详细说明。The features and advantages of the present invention will be described in detail with reference to the accompanying drawings.
【附图说明】【Description of drawings】
图1是本发明一种蓄热式球罐布水器的内部结构示意图;Fig. 1 is a schematic diagram of the internal structure of a heat storage type spherical tank water distributor of the present invention;
图2是本发明一种蓄热式球罐布水器的下布水器的结构示意图;Fig. 2 is a schematic structural view of the lower water distributor of a thermal storage type spherical tank water distributor of the present invention;
图3是本发明一种蓄热式球罐布水器的下布水器的俯视图;Fig. 3 is a top view of the lower water distributor of a thermal storage type spherical tank water distributor of the present invention;
图4是本发明一种蓄热式球罐布水器的第二布水管的截面结构示意图。Fig. 4 is a schematic cross-sectional structure diagram of the second water distribution pipe of a heat storage type spherical tank water distributor according to the present invention.
【具体实施方式】【Detailed ways】
参阅图1至图4,本发明一种蓄热式球罐布水器,包括球罐本体10,以及分别布置在所述球罐本体10内腔上部的上布水器1、内腔下部的下布水器2,所述上布水器1包括若干个第一布水管11,以及与各第一布水管11相连通的第一进出水管12,所述下布水器2包括若干个第二布水管21,以及与各第二布水管21相连通的第二进出水管22,各第一布水管11、第二布水管21上均设有若干个喷射结构。通过在球罐顶部设置用于热水进出的上布水器,底部设置用于冷水进出的下布水器,蓄热过程可使球罐内介质温度均匀一致,达到额定的温度值,放热过程可使高温介质全部释放,放热结束时罐体内均为低温的水介质。Referring to Fig. 1 to Fig. 4, a thermal storage type spherical tank water distributor of the present invention includes a spherical tank body 10, an upper water distributor 1 arranged on the upper part of the inner cavity of the spherical tank body 10, and a water distributor at the lower part of the inner cavity. The lower water distributor 2, the upper water distributor 1 includes several first water distribution pipes 11, and the first water inlet and outlet pipes 12 communicated with each first water distribution pipe 11, the lower water distributor 2 includes several first water distributors Two water distribution pipes 21, and the second water inlet and outlet pipes 22 connected with each second water distribution pipe 21, each of the first water distribution pipe 11 and the second water distribution pipe 21 are provided with several spraying structures. By setting the upper water distributor on the top of the spherical tank for hot water in and out, and the lower water distributor for cold water in and out at the bottom, the heat storage process can make the temperature of the medium in the spherical tank uniform, reach the rated temperature value, and release heat The process can release all the high-temperature medium, and at the end of the heat release, the tank is filled with low-temperature water medium.
进一步地,参阅图1至图3,所述上布水器1包括若干层沿高度方向间隔布置的第一布水管层,所述第一布水管层包括自内至外依次设置的若干个第一布水管11,相邻的两个第一布水管11之间通过第一连接管连通。所述下布水器2包括若干层沿高度方向间隔布置的第二布水管层,所述第二布水管层包括自内至外依次设置的若干个第二布水管21,相邻的两个第二布水管21之间通过第二连接管连通。在本实施例中,第一布水管11、第二布水管21在高度方向只表示了2层,直径方向只表示了3圈,而实际应用中对于大直径球罐本体,高度方向可设置2层及2层以上,直径方向可设置3圈及3圈以上。Further, referring to Fig. 1 to Fig. 3, the upper water distributor 1 includes several layers of the first water distribution pipe layer arranged at intervals along the height direction, and the first water distribution pipe layer includes several first water distribution pipe layers arranged sequentially from the inside to the outside. A water distribution pipe 11, and two adjacent first water distribution pipes 11 communicate through a first connecting pipe. The lower water distributor 2 includes several layers of second water distribution pipe layers arranged at intervals along the height direction. The second water distribution pipe layer includes several second water distribution pipes 21 arranged sequentially from the inside to the outside. The second water distribution pipes 21 communicate with each other through a second connecting pipe. In this embodiment, the first water distribution pipe 11 and the second water distribution pipe 21 only show 2 layers in the height direction, and only 3 circles in the diameter direction, but in practical applications, for the large-diameter spherical tank body, 2 layers can be set in the height direction 3 or more layers can be set in the diameter direction.
进一步地,参阅图3,所述第一布水管11、第二布水管21均采用环形圈管,所述第一布水管11、第二布水管21上分别设有若干排喷射结构,在本实施例中,每根布水管上设置了2排喷射结构,流量或流速可满足系统蓄热、放热要求。Further, referring to Fig. 3, both the first water distribution pipe 11 and the second water distribution pipe 21 are annular pipes, and the first water distribution pipe 11 and the second water distribution pipe 21 are respectively provided with several rows of spraying structures. In the embodiment, two rows of injection structures are installed on each water distribution pipe, and the flow rate or flow rate can meet the heat storage and heat release requirements of the system.
进一步地,参阅图4,所述第一布水管11上的喷射结构向上倾斜设置,所述第二布水管21的喷射结构向下倾斜设置,所述喷射结构与水平面成一定的角度b,在本实施例中,角度b的取值范围为10~60度,能够保证球罐同一平面下的水流速基本均匀。通过水流仿真模拟,确保在球罐本体高度方向上水流能均匀流动,可确保罐体内斜温层尽量小,斜温层的水量控制在总水量的3%以内。Further, referring to Fig. 4, the spraying structure on the first water distribution pipe 11 is arranged inclined upwards, and the spraying structure of the second water distribution pipe 21 is arranged inclined downwards, and the spraying structure forms a certain angle b with the horizontal plane. In this embodiment, the value range of the angle b is 10-60 degrees, which can ensure that the water flow rate under the same plane of the spherical tank is basically uniform. Through the water flow simulation, it is ensured that the water flow can flow evenly in the height direction of the spherical tank body, and the thermocline layer in the tank body can be ensured as small as possible, and the water volume in the thermocline layer is controlled within 3% of the total water volume.
进一步地,所述第一布水管11、第二布水管21上分别设有两排喷射结构,且两排喷射结构之间成一定的角度a。由于球罐在高度方向上的直径是变化的,所以流量恒定下高度方向的水流速也是变化的,在本实施例中,角度a的取值范围为60~120度,能够保证球罐同一平面下的水流速基本均匀。Further, the first water distribution pipe 11 and the second water distribution pipe 21 are respectively provided with two rows of spraying structures, and the two rows of spraying structures form a certain angle a. Since the diameter of the spherical tank in the height direction changes, the water flow rate in the height direction also changes when the flow rate is constant. In this embodiment, the value range of the angle a is 60-120 degrees, which can ensure that the spherical tank is on the same plane The water flow rate is basically uniform.
进一步地,所述喷射结构为喷射孔或喷嘴。Further, the injection structure is an injection hole or a nozzle.
本发明工作过程:Working process of the present invention:
蓄热过程中,高温水从球罐本体10顶部通过上布水器1进入球罐本体10中,逐渐把低温水从球罐本体10底部通过下布水器2排出,直至球罐本体10内全部为高温水,蓄热才结束。利用布水器,可使高温水从球罐本体上部均匀往下流动,避免形成紊流,低温水也均匀流出,确保有效减小斜温层。During the heat storage process, high-temperature water enters the spherical tank body 10 from the top of the spherical tank body 10 through the upper water distributor 1, and gradually discharges low-temperature water from the bottom of the spherical tank body 10 through the lower water distributor 2 until it reaches the inside of the spherical tank body 10. It is all high temperature water, and the heat storage is completed. The water distributor can make the high-temperature water flow down evenly from the upper part of the spherical tank body to avoid turbulent flow, and the low-temperature water can also flow out evenly, so as to effectively reduce the temperature slope.
放热过程中,低温水从球罐本体10底部通过下布水器2进入球罐本体10中,逐渐把高温水从球罐本体10顶部通过上布水器1排出球罐,直至球罐本体10内高温水全部输出,罐体内全部换成低温水,放热才结束。利用布水器,可使低温水从球罐本体底部均匀往上流动,避免形成紊流,高温水从罐体顶部均匀流出,确保有效减小斜温层。During the exothermic process, low-temperature water enters the spherical tank body 10 from the bottom of the spherical tank body 10 through the lower water distributor 2, and gradually discharges high-temperature water from the top of the spherical tank body 10 through the upper water distributor 1 until the spherical tank body All the high temperature water is output within 10, and all the water in the tank is replaced with low temperature water, so that the heat release is over. The water distributor can make the low-temperature water flow upward evenly from the bottom of the spherical tank body, avoiding the formation of turbulent flow, and the high-temperature water flows out evenly from the top of the tank body, ensuring the effective reduction of the temperature slope.
上述实施例是对本发明的说明,不是对本发明的限定,任何对本发明简单变换后的方案均属于本发明的保护范围。The above-mentioned embodiment is an illustration of the present invention, not a limitation of the present invention, and any solution after a simple transformation of the present invention belongs to the protection scope of the present invention.
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN116498901A (en) * | 2023-02-10 | 2023-07-28 | 中国能源建设股份有限公司 | A Spherical Tank Thermal Storage System with Temperature Compensation |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201964554U (en) * | 2010-12-23 | 2011-09-07 | 深圳市中科拓工程技术有限公司 | Cold storage device |
| CN202902956U (en) * | 2012-11-06 | 2013-04-24 | 北京英沣特能源技术有限公司 | Efficient closed-type pressurized water energy storage device |
| CN107179014A (en) * | 2017-06-23 | 2017-09-19 | 中能服能源科技股份有限公司 | A kind of multi-level water-distributing device of high uniformity |
| CN109059593A (en) * | 2018-08-08 | 2018-12-21 | 北京京诚科林环保科技有限公司 | High-efficiency energy-storage water tank that can distribute water evenly |
| CN114518048A (en) * | 2022-02-24 | 2022-05-20 | 中冶南方工程技术有限公司 | A spherical tank heat accumulator |
-
2023
- 2023-02-10 CN CN202310097685.5A patent/CN116558341A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201964554U (en) * | 2010-12-23 | 2011-09-07 | 深圳市中科拓工程技术有限公司 | Cold storage device |
| CN202902956U (en) * | 2012-11-06 | 2013-04-24 | 北京英沣特能源技术有限公司 | Efficient closed-type pressurized water energy storage device |
| CN107179014A (en) * | 2017-06-23 | 2017-09-19 | 中能服能源科技股份有限公司 | A kind of multi-level water-distributing device of high uniformity |
| CN109059593A (en) * | 2018-08-08 | 2018-12-21 | 北京京诚科林环保科技有限公司 | High-efficiency energy-storage water tank that can distribute water evenly |
| CN114518048A (en) * | 2022-02-24 | 2022-05-20 | 中冶南方工程技术有限公司 | A spherical tank heat accumulator |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116498901A (en) * | 2023-02-10 | 2023-07-28 | 中国能源建设股份有限公司 | A Spherical Tank Thermal Storage System with Temperature Compensation |
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