• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    The invention relates to a pressure compensation system with safety function for an electrolyte tank of flow batteries, in particular vanadium redox flow batteries, wherein a head portion (5) of the electrolyte tank (3, 4) with the environment (2) of the flow battery via a pipe (6) in the a primary bidirectional pressure compensating valve (7) is arranged, connected and branches off from the pipeline (6) with the primary bidirectional pressure compensating valve (7) with a first set pressure, a bypass line (9, 20) in which a secondary bidirectional pressure compensating valve (10) is arranged with a second response pressure which is greater than the first response pressure, and whose outlet (11) is located within a, the electrolyte tank (3, 4) surrounding the housing (13).
    公开号:AT514421A4
    申请号:T50374/2013
    申请日:2013-06-06
    公开日:2015-01-15
    发明作者:Martin Harrer；Paul Dipl Ing Binder；Michael Dipl Ing Fh Pinzl；Adam Dr Whitehead
    申请人:Cellstrom Gmbh；
    IPC主号:
    专利说明:

    Gas bubbler
    The invention relates to a pressure compensation system with safety function for an electrolyte tank of redox flow batteries, wherein a head portion of an electrolyte tank with the environment of the flow battery via a pipe in which a primary bidirectional pressure compensating valve is arranged with a first set pressure.
    Redox flow batteries are known to consist of cells which are flowed through by electrically differently charged electrolytes. When using vanadium redox flow batteries, during discharge, V2 + in the negative electrolyte reacts to V3 +. To the same extent V5 + in the positive electrolyte reacts to V4 +. This process is the normal electrochemical process as a result of the discharge, with the concentrations of V3 + in the negative electrolyte and V4 + in the positive electrolyte being about the same under normal circumstances.
    Upon contact of the negative electrolyte liquid of such vanadium redox flow batteries with oxygen, V2 + in the negative electrolyte also reacts to V3 +. This results in an imbalance between the negative electrolyte and the positive electrolyte, which in practice leads to a reduction of the available capacity.
    A reprocessing of the electrolytes is possible, but expensive and associated with corresponding costs. For this reason, the electrolyte is in a closed tank, whereby the closed design of the electrolyte tank ensures that there is no chemical reaction with the oxygen from the surrounding air.
    Due to temperature changes and gas formation during the charging process within the flow battery, there is also a tendency for a high pressure variation within the closed electrolyte tank. Since, for comprehensible reasons, the electrolyte tank can only be safely operated in a certain pressure range, a corresponding compensation system is to be provided which ensures the reliable function.
    In this connection, JP2001093560A, for example, provides a system in which that portion of the tank in which there is no electrolyte fluid is filled with an inert gas. The inert gas filling is maintained at a constant pressure by means of a pressure regulating valve. The disadvantage here is to see that the inert gas at regular intervals to check and if necessary to replace, which is naturally associated with additional effort and expense.
    Another way to compensate for pressure fluctuations within the electrolyte tank while preventing the electrolyte from coming in contact with atmospheric oxygen is to place elastic containers within the tank structure. Such a construction is shown for example in US 7,220,515 BB or US 6,681,789 BA. The elastic containers are arranged above the liquid stored in the tank and are directly in contact with the ambient air via corresponding openings. Depending on the pressure level within the electrolyte tank, the elastic containers are more or less filled with ambient air. For example, as the pressure level increases, the volume of the elastic containers is reduced, thus allowing the pressure within the electrolyte tank to be maintained at a constant level by volume liberated. A disadvantage is that, depending on the possible volume of the elastic container, only a certain pressure difference can be compensated. A safety device for the case in which the opening, via which the elastic container in communication with the environment, is misplaced or clogged, is not provided. Such blockage of the main outlet would therefore lead to failure of the pressure compensation system.
    CN 102244281A shows an indirect sealing arrangement in which the tank of a flow battery is sealed off from the environment using a sealing liquid or a sealing gas, so that no atmospheric oxygen gets inside the electrolyte tank. The sealing liquid is located in the sink of a pipeline whose shape corresponds to a horizontal "S". This pipeline opens on the one hand in the head region of the electrolyte tank, on the other hand directly into the environment. The disadvantage of the embodiment shown is that no safety devices are provided in the event of a malfunction, for example, an already mentioned blockage of the pipeline.
    The object of the present invention is to form a simple as possible bi-directional pressure equalization system for electrolyte tanks of flow batteries, which should ensure safe operation under all circumstances and which further ensures that the electrolyte fluids are separated from the oxygen of the surrounding air.
    The object is achieved according to the present invention in a pressure equalization system of the type mentioned in that a bypass line branches off from the pipeline, in which a secondary bidirectional pressure compensating valve with a second set pressure is greater than the first set pressure, is arranged, and a valve outlet of secondary bidirectional pressure compensating valve located within a housing surrounding the electrolyte tank. It is insignificant at which point of the pipeline branches off the bypass line. If, for example, the ambient side main outlet of the primary bidirectional pressure compensation valve due to snow, leaves, pollution, etc. or other factors such as vandalism laid or blocked, granted the secondary bidirectional pressure compensation valve, protected by the surrounding housing, with appropriate pressure difference yet the escape of the pent-up gas.
    The response pressure, ie the value for the mentioned pressure difference between the head of the Elektolyt tank and the environment in which the withdrawal of the gas formed via the secondary bidirectional pressure compensation valve, according to the invention is above the set pressure at which the primary bidirectional pressure compensating valve is activated and is usually in Dependence of the structural properties of the electrolyte tank chosen to avoid their damage.
    Since the gas formed inside the electrolyte tank during charging is flammable due to the high proportion of hydrogen, a flame check valve is advantageously arranged at the main outlet. This makes it possible to prevent the flames from being repelled into the inner region of the housing in the event of ignition of the escaping gas.
    Advantageously, a sensor for detecting escaping gas is arranged in the region of the valve outlet of the secondary bidirectional pressure compensation valve. This allows a pressure difference to be detected that is large enough for the gas to travel the bypass tubing and not the primary bi-directional pressure balance valve. As a result, a possible malfunction of the primary bidirectional pressure compensation valve can be deduced. For example, the flow battery can subsequently be disconnected from the electrical network, the photovoltaic system or wind power plant in order to stop further gas formation in the course of the charging process. This could also avoid the formation of a critical concentration of gas within the housing surrounding the electrolyte tank. Furthermore, a corresponding output is conceivable that informs the operator of the flow battery about the malfunction and thus causes appropriate action.
    An advantageous embodiment of the invention provides that the secondary bidirectional pressure compensation valve is designed by a U-shaped bypass pipe, which is filled with a certain amount of sealing liquid, and the sealing liquid is in the pressure-balanced state in the sink of the U-shaped bypass pipe. This makes it possible to realize a simply constructed valve, without the use of maintenance-prone, movable mechanism, which on the amount of sealing liquid simply to different
    Tightening pressures is to adapt, again is insignificant at which point of the pipeline branches off the U-shaped bypass pipe.
    Advantageously, it can further be provided that the primary bidirectional pressure compensation valve is designed by a U-shaped pipe section of the pipeline connecting the head of the electrolyte tank with the environment of the tank area and in the pressure-balanced state, a sealing liquid in the sink of the U-shaped pipe section , wherein the advantageous effect is analogous to that of the above-described secondary bidirectional pressure compensating valve.
    In this context, it is advantageously provided that a liquid with a low degree of evaporation, such as mineral oil or paraffin oil, is provided as the sealing liquid. As a result, set pressure, or the mentioned pressure difference from which it comes to equalize the pressure, be kept approximately constant, since there is no significant shrinkage of the sealing liquid due to evaporation.
    In a further advantageous embodiment, it is provided that an antistatic liquid is used as the sealing liquid, or the sealing liquid is mixed with an antistatic additive.
    In a further advantageous manner, an acoustic sensor is arranged on the U-shaped bypass pipe. If gas bubbles pass through the sealing liquid contained in the U-shaped bypass pipe, a characteristic acoustic signal is generated, which is detected by the acoustic sensor. As a result, a possible blockage or malfunction of the primary bidirectional pressure compensating valve can again be inferred.
    In order to facilitate filling and maintenance, the U-shaped pipe section and / or the U-shaped bypass pipe are advantageously made transparent or translucent.
    In a very similar advantageous embodiment, instead of or in addition to the acoustic sensor, an optical sensor is arranged on the U-shaped bypass pipe, wherein this is made transparent or translucent. As soon as gas bubbles pass through the sealing liquid in the U-shaped bypass pipe, a momentary change in the optical signal occurs. This change is an indication that the primary bi-directional pressure balance valve is not functioning properly.
    A further advantageous embodiment provides that between the inlet and outlet side of the primary bidirectional pressure compensating valve, a purge valve is provided. This allows, for example when flushing with a purge gas for service purposes, a higher gas flow rate than would be possible through the primary bidirectional pressure equalization valve.
    In order to increase the service life of the pressure equalization system, it is advantageously provided that the U-shaped pipe section and the bypass line are made of chemically resistant material relative to the electrolyte fluids, since electrolyte fluid may well be in the form of droplets within the gas formed.
    An advantageous embodiment of the invention includes that a means for grounding is provided, which is in electrical contact with the sealing fluids. This allows to minimize the risk of static electricity.
    The subject invention will be explained in more detail below with reference to Figures 1 to 3, which show by way of example, schematically and not by way of limitation advantageous embodiments of the invention. It shows
    1 shows the schematic structure of the tank region of a flow battery with a pressure compensation system according to the invention with safety function,
    Fig. 2 shows the schematic structure of the tank area of a flow battery with a pressure compensation system according to the invention with safety function in a particularly advantageous embodiment and
    Fig. 3 shows the schematic structure of the pressure compensation system in a further arrangement variant.
    FIG. 1 shows the schematic structure of the tank region 1 of a flow battery according to the invention, in which the two electrolyte tanks 3 and 4 have a common head region 5, but a design in which each of the two electrolyte tanks 3 and 4 has its own head region 5 lying over it is shown. conceivable, in which case each head area is connected to the pressure equalization system according to the invention.
    As a consequence, only one common head region 5 will be mentioned without any restricting effect.
    In the common head area 5 of the two electrolyte tanks 3 and 4 collects, for example, caused by heating, gas. Via a pipe 6 and the primary bidirectional pressure compensation valve 7, the resulting gas can escape at a corresponding pressure difference across the main outlet 8 in the housing 13 into the environment. Furthermore, a bypass pipeline 9 with a secondary bidirectional pressure compensation valve 10 branches off from the pipeline 6.
    As the pressure in the head region 5 increases due to increased gas evolution, for example as a result of operational heating, the accumulated gas can escape into the environment 2 via the main outlet 8 on the ambient side of the primary bidirectional pressure compensation valve 7. The response pressure of the primary bidirectional pressure compensation valve, ie the necessary pressure difference between the head region 5 and the environment 2, is dependent on the setting or the dimensioning of the primary bidirectional pressure compensation valve 7.
    If the primary bidirectional pressure compensating valve 7, for example, due to a blockage of the ambient side main outlet 8 is not functional, the pressure difference between the head area 5 and primary bidirectional pressure compensating valve 7, due to the continued evolution of gas continues to increase. If the pressure difference reaches a corresponding level, namely the response pressure of the secondary bidirectional pressure compensation valve 10, the gas is withdrawn via the secondary bidirectional pressure compensation valve 10, the gas via the valve outlet 11, which according to the invention within the housing 13 surrounding the electrolyte tanks 3 and 4 is located, escapes. The magnitude of the set pressure at which the withdrawal of the gas via the secondary bidirectional pressure compensation valve 10 is above that pressure difference at which the primary bidirectional pressure compensation valve 7 in normal operation allows the gas to escape via the main outlet 8 on the side of the environment and is usually due to the structural properties of the electrolyte tanks 3 and 4 dependent. Characterized in that the response pressure of the secondary bidirectional pressure compensating valve 10 is above that of the primary bidirectional pressure compensating valve 7, thus ensuring that the pressure equalization takes place in normal operation exclusively via the primary bidirectional pressure compensating valve 7.
    Since the described mode of action is bidirectional, it is also possible in this way to compensate for a suppression in the head region 5, which could occur as a result of atmospheric changes.
    2 shows the just described tank region 1 according to the invention of a flow battery in a particularly advantageous embodiment.
    In this case, the primary bidirectional pressure compensation valve 7 by a U-shaped pipe section 12 of the pipe 6 which connects the head portion 5 of the electrolyte tanks 3 and 4 with the environment 2 of the tank portion 1 is executed. In the pressure-balanced state, there is a sealing liquid 14 in the depression 16 of this U-shaped pipe section 12.
    Due to the increase in pressure in the head region 5 of the two electrolyte tanks 3 and 4 due to increased gas evolution, for example, by operational heating, the
    Seal fluid 14 is displaced within the U-shaped tube section 12 in the direction of the outlet side 17. Once the set pressure of the primary bidirectional pressure compensating valve 7 is reached, so the pressure difference is sufficient to push the sealing liquid 14 completely above the bottom dead center 15 of the U-shaped tube section 12, the pent-up gas in the form of individual ascending gas bubbles through the U-shaped pipe section 12, the sealing liquid contained therein 14 and ultimately through the outlet side 17 escape through the ambient side main outlet 8 and the flame check valve 18, whereby the resulting pressure difference is successively reduced. The process of escape lasts just as long until, due to the reducing pressure difference, the sealing liquid 14 moves back into the area of the bottom dead center 15 of the U-shaped pipe section 12.
    Since the described mode of action is bidirectional, it is also possible in this way to compensate for a suppression in the head region 5, which could occur in rare cases. In this case, the sealing liquid 14 shifts within the U-shaped pipe section 12 but in the direction of the tank-side inlet 19 of the U-shaped pipe section 12. In the same way as already described, therefore, as soon as the sealing liquid 14 completely above the bottom dead center 15 of the U-shaped pipe section 12, ambient air in the form of individual gas bubbles are sucked through the U-shaped pipe section 12 and the sealing liquid 14 contained therein, which in turn reduces the resulting pressure difference. As with the reduction of overpressure, the process of suction at negative pressure continues exactly until, due to the reducing pressure difference, the sealing liquid 14 again moves into the area of bottom dead center 15 of the U-shaped tube section 12.
    The set pressure, so the mentioned pressure difference between the head area 5 and the surrounding area 2, which is necessary to push the sealing liquid 14 completely above the bottom dead center 15 of the U-shaped tube section 12, is of the dimensioning of the U-shaped tube section 12, the Art the sealing liquid 14 and the amount depends on and can be easily adjusted.
    Similarly, the secondary bidirectional pressure compensating valve 10 in the form of a U-shaped bypass pipe 20 with sealing liquid 21 which is in the pressure-balanced state in the well 22 of the U-shaped bypass pipe 20 is executed. By way of example, the U-shaped bypass pipe 20 is shown on the tank side by the U-shaped pipe section 12.
    If the primary bidirectional pressure compensating valve 7, for example, due to a blockage of the environment-side main outlet 8 is not functional, the pressure difference between the head area 5 of the two electrolyte tanks 3 and 4 and primary bidirectional pressure compensation valve 7, due to the continued evolution of gas, continues to rise to the set pressure of the secondary bidirectional pressure compensating valve 10 is reached. As just described for the primary bidirectional pressure compensation valve 7, the sealing liquid 21 is thereby displaced within the U-shaped bypass pipe 21 in the same way. Once the sealing liquid 21 is completely above the bottom dead center 23 of the U-shaped bypass pipe 20, the accumulated gas in the form of individual gas bubbles through the U-shaped bypass pipe 20 and the sealing liquid contained therein 21 and consequently via the valve outlet 11, which according to the invention is within the housing 13 surrounding the electrolyte tank 3 and 4, escape. As also described for the primary bidirectional pressure compensating valve 7, the process of escape continues until the sealing liquid 21 again moves into the area of the bottom dead center 23 of the U-shaped bypass pipe 20 due to the reducing pressure difference.
    The arranged in the region of the Ventilauslasses 11 sensor 24 detects any leakage of gas through the U-shaped bypass pipe 20. Since this can be deduced a possible malfunction of the primary bidirectional pressure compensating valve 7, for example, the flow battery from the electrical network, the photovoltaic or Wind turbine to be disconnected in order to stop further gas formation in the course of the charging process and / or the operator of the flow battery to be informed by a corresponding issue about the malfunction.
    Furthermore, acoustic sensors 25 and / or optical sensors 26 can be arranged on the U-shaped bypass pipeline 20, which detect the displacement of the sealing liquid 21 or the passage of gas bubbles.
    As for the primary bidirectional pressure compensation valve 7, the amount of the necessary pressure difference or the amount of response pressure of the dimensioning of the U-shaped bypass pipe 20, the type of sealing liquid 21 and the amount depends, the necessary pressure difference to activate the secondary bidirectional pressure compensation valve 10th As already described, the level of the necessary pressure difference for activating the secondary bidirectional pressure compensation valve 10 can, as also already described, be made dependent on the structural properties of the electrolyte tanks 3 and 4.
    The bidirectional effect and the associated operation is analogous to that of the primary bidirectional pressure compensation valve. 7
    Between inlet side 19 and outlet side 17 of the primary bidirectional pressure compensation valve 7, a purge valve 27 may be provided. In normal operation, the purge valve 27 is closed and the resulting gas takes, as described, with sufficient pressure difference the way through the primary bidirectional pressure compensating valve 7 and the sealing liquid contained therein 14. The purge valve 27 allows in the open state, the flushing with a purge gas for service purposes with a higher gas flow rate than would be possible through the primary bidirectional pressure compensation valve 7.
    By grounding the sealing fluids 14 and 21 by means of the device 28, it can be ensured that the risk of static charge is minimized. Of course, this risk can also be minimized by the use of antistatic sealing liquids, or the addition of an antistatic additive to the sealing liquids 14 and 21.
    Fig. 3 shows the schematic structure of the pressure equalization system in a further arrangement variant in which only one electrolyte tank 3 is arranged and the U-shaped bypass pipe 20 branches off from bottom dead center 15 of the U-shaped pipe section 12 of the pipe 6.
    The ratio between the first response pressure of the primary bidirectional pressure compensating valve 7 and the second response pressure of the secondary bidirectional pressure compensating valve 10 depends on their arrangement or their position relative to one another. Otherwise, the function is identical to the embodiment in FIG. 2.
    权利要求:
    Claims (13)
    [1]
    1. Pressure compensation system with safety function for an electrolyte tank of redox flow batteries, wherein a head region (5) of an electrolyte tank (3, 4) with the environment (2) of the flow battery via a pipe (6) in a a primary bidirectional pressure compensation valve (7) is arranged with a first set pressure, is connected, characterized in that from the pipe (6) branches off a bypass line (9, 20) in which a secondary bidirectional pressure compensating valve (10) having a second set pressure, which is greater than the first set pressure , and a valve outlet (11) of the secondary bidirectional pressure compensating valve (10) is located within a housing (13) surrounding the electrolyte tank (3, 4).
    [2]
    2. Pressure equalization system according to claim 1, characterized in that at the main outlet (8) a flame check valve (18) is arranged.
    [3]
    3. Pressure equalization system according to claim 1 or 2, characterized in that in the region of the valve outlet (11) of the secondary bidirectional pressure compensation valve (10), a sensor (24) is arranged for the detection of escaping gas.
    [4]
    4. Pressure equalization system according to one of claims 1 to 3, characterized in that the secondary bidirectional pressure compensation valve (10) by a U-shaped bypass pipe (20) which is filled with a certain amount of sealing liquid (21) is executed, and the sealing liquid ( 21) in the pressure-balanced state in the recess (22) of the U-shaped bypass pipe (20).
    [5]
    5. Pressure equalization system according to one of claims 1 to 4, characterized in that the primary bidirectional pressure compensating valve (7) by a U-shaped pipe section (12) of the pipe (6) with the head region (5) of the electrolyte tank (3, 4) the environment (2) of a tank region (1) is designed to run and in the pressure-balanced state, a sealing liquid (14) in the depression (16) of the U-shaped pipe section (12).
    [6]
    6. pressure equalization system according to claims 4 and 5, characterized in that as the sealing liquid (14, 21) a liquid is provided with a low degree of evaporation.
    [7]
    7. Pressure equalization system according to one of claims 4 to 6, characterized in that as the sealing liquid (14, 21) an antistatic liquid is used, or the sealing liquid (14, 21) is mixed with an antistatic additive.
    [8]
    8. Pressure equalization system according to one of claims 4 to 7, characterized in that an acoustic sensor (25) on the U-shaped bypass pipe (20) is arranged.
    [9]
    9. Pressure equalization system according to one of claims 4 to 8, characterized in that the U-shaped pipe section (12) and / or the U-shaped bypass pipe (20) is made transparent or translucent.
    [10]
    10. Pressure equalization system according to one of claims 4 to 8, characterized in that an optical sensor (26) on the U-shaped bypass pipe (20) is arranged and the U-shaped bypass pipe (20) is made transparent or translucent.
    [11]
    11. Pressure equalization system according to one of claims 1 to 10, characterized in that between the inlet side (19) and outlet side (17) of the primary bidirectional pressure compensation valve (7), a flush valve (27) is provided.
    [12]
    12. Pressure equalization system according to one of claims 4 to 11, characterized in that the U-shaped pipe section (12) and the bypass line (9, 20) from, compared to the electrolyte liquid in the electrolyte tank (3, 4), chemically resistant material are executed.
    [13]
    13. Pressure equalization system according to one of claims 4 to 9, characterized in that a device (28) is provided for grounding, which is in electrical contact with the sealing liquid (14, 21).
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    CA2915294A1|2014-12-11|
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    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    DE2218945A1|1972-04-19|1973-10-31|Varta Batterie|GALVANIC ELEMENTS WITH A PRESSURE COMPENSATION DEVICE|
    DE4113006C1|1991-04-20|1992-04-02|Mercedes-Benz Aktiengesellschaft, 7000 Stuttgart, De|
    US6199577B1|1999-03-12|2001-03-13|Seh America, Inc.|Pressure relief system for chemical storage tanks|
    US6446681B1|1999-08-24|2002-09-10|Johan Christiaan Fitter|Filler unit for topping up a container with liquid|
    US20040134535A1|2003-01-14|2004-07-15|Mitchell Thomas O.|Liquid column pressure and vacuum vent|
    JP2001093560A|1999-09-27|2001-04-06|Kashimakita Kyodo Hatsuden Kk|Redox flow battery|
    JP3642732B2|2000-12-06|2005-04-27|住友電気工業株式会社|Pressure fluctuation prevention tank structure, electrolyte circulation type secondary battery and redox flow type secondary battery|
    CN102244281B|2011-05-27|2015-07-15|国网电力科学研究院武汉南瑞有限责任公司|Method for sealing liquid reservoir for liquid flow battery|
    CN102386427A|2011-11-22|2012-03-21|深圳市金钒能源科技有限公司|Sealing method of vanadium liquid cavity and vanadium pile system using same|GB2578611A|2018-10-31|2020-05-20|Redt Ltd Dublin Ireland|Pressure regulator|
    IT201900002301A1|2019-02-18|2020-08-18|Univ Degli Studi Padova|SAFETY EQUIPMENT FOR MILLIBARIAL PRESSURE CONTROL IN INERT ATMOSPHERE FOR HIGH REACTIVITY LIQUID SOLUTIONS, AND FLOW TANK AND BATTERY INCLUDING THIS SAFETY EQUIPMENT|
    法律状态:
    2016-11-15| PC| Change of the owner|Owner name: GILDEMEISTER ENERGY STORAGE GMBH, AT Effective date: 20161005 |
    2018-12-15| PC| Change of the owner|Owner name: ENEROX GMBH, AT Effective date: 20181018 |
    优先权:
    申请号 | 申请日 | 专利标题
    ATA50374/2013A|AT514421B1|2013-06-06|2013-06-06|Pressure compensation system with safety function for an electrolyte tank|ATA50374/2013A| AT514421B1|2013-06-06|2013-06-06|Pressure compensation system with safety function for an electrolyte tank|
    KR1020167000261A| KR20160017065A|2013-06-06|2014-05-27|Pressure-equalising system with safety function for an electrolyte tank|
    EP14726976.5A| EP3005444B1|2013-06-06|2014-05-27|Pressure-equalising system with safety function for an electrolyte tank|
    CA2915294A| CA2915294A1|2013-06-06|2014-05-27|Pressure compensation system having a safety function for an electrolytic tank|
    PCT/EP2014/060984| WO2014195191A1|2013-06-06|2014-05-27|Pressure-equalising system with safety function for an electrolyte tank|
    US14/890,017| US20160141669A1|2013-06-06|2014-05-27|Pressure Compensation System Having a Safety Function for an Electrolytic Tank|
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