The present invention relates to a redox flow battery including a measuring device for determining an electrolyte property. However, this does not involve, in particular, merely the determination of an electrode potential. The battery in this case may be operated alone or as part of a battery system. Such a battery system is made up, for example, of a series connection of multiple redox flow batteries (battery string).
A redox flow battery includes a cell assembly, i.e., an arrangement of a plurality of redox flow cells, and a tank device for storing electrolyte including at least two tanks, a first tank storing negative electrolyte and a second tank storing positive electrolyte. During operation of the battery, negative and positive electrolyte is pumped in two separate circuits through the cells. Pump impellers, means for driving the pump impellers, and corresponding piping are provided for this purpose. To determine the state of charge (SoC), a redox flow battery includes a measuring device for determining the open circuit voltage (OCV). This is an electrochemical cell including chambers for positive and negative electrolytes, which are separated by a membrane. Electrodes, at which a voltage may be tapped as a measuring variable, are situated in the chambers. In addition, such a redox flow battery may also include further electrochemical cells, which are constructed similarly to the cells for determining the open circuit voltage. In the case of the further cells, however, one of the chambers is filled with a reference electrolyte, and the other chamber is filled with negative or positive electrolyte. Such cells are also referred to as reference cells and are used to detect a shift in the electrolyte of the battery. WO 2018/237181 A1 describes a redox flow battery including OCV cells and reference cells. WO 2012/020277 A1 describes a redox flow battery including an OCV cell, WO 2012/020277 A1 describing details for integrating the OCV cell into the battery.
It is an object of the present invention to provide a redox flow battery that is more simply constructed or may be more flexibly designed than conventional redox flow batteries.
The present invention provides a redox-flow battery (1) including a cell assembly (2) and a tank device (3) for receiving electrolyte, the cell assembly (2) including a plurality of redox flow cells, and the tank device (3) including at least a first tank for receiving negative electrolytes, at least a second tank for receiving positive electrolytes, a pipe system for connecting the tanks to the cell assembly (2) and pump impellers (7) for conveying the electrolytes, in order to form in each case an electrolyte circuit, and the redox flow battery (1) including at least one measuring device (4) for determining an electrolyte property, including at least one measuring cell (4.1, 4.2, 4.3), the at least one measuring cell (4.1, 4.2, 4.3) including at least one connection for supplying electrolyte, at least one connection for discharging electrolyte and a connection element (5) including a channel (5.1), which is connected to one of the electrolyte circuits in such a way that during a circulation of the electrolyte in the electrolyte. The channel (5.1) includes a first section (5.1.1) and a second section (5.1.2), the cross section of the first section (5.1.1) being smaller than the cross section of the second section (5.1.2), and the connection for discharging electrolyte being connected to the first section (5.1.1) by a connection line and the connection for supplying electrolyte to the second section (5.1.2) being connected by a connection line.
The approaches according to the present invention are explained below with reference to figures. In particular:
The specific embodiment shown in the lower part of
“Crossover” may also occur in a reference cell itself. In order to reduce this undesirable effect, it is advantageous if the reference liquid has a preferably high viscosity. The reference liquid used may therefore advantageously be a so-called “gelled electrolyte,” which is described in WO 02/11227 A1. In general, V3+/V4+ electrolyte is used in vanadium-based redox flow batteries.
Instead of a conventional electrode and a reference liquid, one further specific embodiment of a reference cell involves using a platinum wire situated in the corresponding chamber, which is situated close to the membrane or to the separator and through which a current passes during the measurement. In addition to platinum, it is also possible to use silver-silver chloride as a material for such a wire.
One further specific embodiment of a reference cell is based on a completely different measuring principle. The reference cell in this case is made up of one single narrow chamber or one narrow space, through which electrolyte flows. The measurement of the electrolyte property then takes place not electrically with the aid of an electrode, but optically, by spectroscopic examination of the electrolyte film. Further details in this regard are found, for example, in “A review on the electrolyte imbalance in vanadium redox flow batteries” by Tossaporn Jirabovornwisut, Amornchai Arpornwichanop, published in the International Journal of Hydrogen Energy 44 (2019), pages 24485 through 24509 starting from the paragraph “U-vis spectroscopic measurement” on page 24497.
All specific embodiments have in common the fact that measuring device 4 for determining an electrolyte property includes at least one measuring cell and at least two connections, one connection for supplying electrolyte and one connection for discharging electrolyte being provided. In this case, it is clear that the connections are designed to supply the at least one measuring cell or the at least one chamber of the measuring cell with an electrolyte through-flow.
If measuring cell 4 includes only one measuring cell for determining the open circuit voltage, as represented in the upper part of
In the specific embodiments represented in
In order for a measuring device 4 to be able to reliably determine the instantaneous electrolyte property, the chamber must or the chambers must be supplied with fresh electrolyte. This occurs by integrating the measuring device into the electrolyte circuit. In conventional batteries, the connections for supplying and discharging electrolyte are connected to points of the electrolyte circuit, which have such a pressure difference that electrolyte is able to flow through the chambers of measuring device 4. Suitable branch points with high pressure are found in the lines that extend from the pressure side of the pump impellers up to the cell assembly. Suitable branch points with low pressure are found in the lines that extend from the tanks up to the intake side of the pump impellers or from the cell assembly up to the tanks. Low pressure further prevails in the upper part of the tank itself so that the connection for discharging electrolyte of measuring device 4 may also be connected to this part of the tank. In conventional batteries, the latter option is generally used. It is clear from the aforementioned that in conventional batteries, several lines and branching parts are required for supplying the measuring cells with electrolyte, which makes the battery complex and which therefore increases the risk of an electrolyte leakage.
An object of the inventors is therefore to design the connection of the measuring device to the electrolyte circuit in such a way that the aforementioned disadvantages are avoided.
One or multiple or all connection lines between the chambers and the first and second sections 5.1.1 and 5.1.2 of channel 5.1 may optionally include cutoff valves.
A battery according to the present invention may include the following combination of measuring cells:
Further measuring cells may be added, which are redundantly designed. In each case, the advantage according to the present invention occurs already when only one of the reference cells according to
The contour of the constriction in channel 5.1 is represented in
It is particularly advantageous if the respective measuring cells constructed according to the present invention together with connection element or connection elements form a structural unit, so that the chambers, the membrane or the membranes, the channel or the channels and the connection lines between the chambers and the channels are embedded into this one structural unit. This structural unit may, for example, be manufactured by injection molding, the structural unit preferably being made of a plastic. As a further manufacturing option, the aforementioned structural unit includes two or multiple components made of plastic, in which the chambers, channels and connection lines are embedded with the aid of corresponding recesses. The chambers, channels and connection lines are then formed by joining the components. The recesses may be formed, for example, by milling. The joining in this case may also take place by screwing together, gluing or welding. When screwing together, seals are to be provided if necessary. The multipart arrangement may be particularly advantageously designed if the one chamber of the measuring cell is provided in one of the components, and the other chamber of the measuring cell is provided in another component in such a way that the membrane is clamped between these two components. If necessary, seals are to be provided at the clamping point. Alternatively, the structural unit may also be manufactured via an additive manufacturing method. The aforementioned manufacturing methods may of course also be combined, for example, by manufacturing a portion of the components using casting techniques, and by producing another portion of the components by milling.
Sensors may be advantageously integrated into the structural unit. These may involve, for example, pressure sensors or temperature sensors. Temperature sensors are of particular importance, since the temperature has a significant influence on the potential ascertained from the Nernst equation.
To connect the connection element or the connection elements at the electrolyte circuit, flanges or connection pieces may be provided. These may be advantageously integrated into the structural unit.
One further advantageous specific embodiment results when the arrangement made up of connection lines together with OCV cell is designed to be self-venting. For example, the connection lines may be designed to be monotonically ascending in the flow direction of the electrolyte and/or using suitable geometries of the OCV cell. This facilitates the automatic venting of the measuring cells.
One particularly advantageous specific embodiment results when, in addition to the channel, the chambers and the supply lines, one or both of the pump impellers of the battery are also integrated into the structural unit. Further connection pieces in the electrolyte circuit are eliminated as a result, so that the complexity and the susceptibility to leakage may be further reduced. In this case, the channel may be provided with a narrowing either on the pressure side or on the intake side of the pump impeller. In this specific embodiment, the structural unit represents essentially an enlarged pump head, in which the measuring cell, the connection element or the connection elements and the connection lines are integrated. With respect to the manufacture of this specific embodiment, the above applies.
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Number | Date | Country | Kind |
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10 2020 120 428.0 | Aug 2020 | DE | national |
Filing Document | Filing Date | Country | Kind |
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PCT/EP2021/058989 | 4/7/2021 | WO |