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Model-based Design Vanadium Redox Flow Batteries

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Model-based Design Vanadium Redox Flow Batteries ( model-based-design-vanadium-redox-flow-batteries )

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Section 2.3  Concentrations of the ionic species Because of the vanadium crossover, described in Section 2.4 on page 18, the SoCs of both electrolytes might deviate from each other during the battery operation. They are calculated as shown in the Eqs. (2-3) and (2-4) [18]. To facilitate the reading, from now on, the time variable is omitted. SoCT􏱆 􏰵 c2T􏱆 (2-3) c2T􏱆 􏰷 c3T􏱆 SoCT􏱇 􏰵 c5T􏱇 (2-4) c4T􏱇 􏰷 c5T􏱇 The combined SoC of both tanks, SoCT, can be expressed in two ways. Eq. (2-5) shows one way of a combined SoC. Herein, we just divide the concentration of the ‘charged’ species by the total concentration of vanadium ions in the two electrolytes. However, this SoC definition is not practical. If the V2+ ions are depleted in the negative tank, we can no longer operate the battery. Nevertheless, if the positive tank still stores VO2+ ions, the tank SoC according to Eq. (2-5) is not zero. Effectively, the positive tank still stores energy, but this energy is no longer accessible in this battery configuration. SoCT 􏰵 c2T􏱆 􏰷 c5T􏱇 (2-5) c2T􏱆 􏰷 c3T􏱆 􏰷 c4T􏱇 􏰷 c5T􏱇 The second way for deriving a combined SoC originates from the SoC measurement in practice. Using a bypass-cell which operates under open circuit conditions, we can constantly measure the open circuit voltage (OCV) of the two electrolytes [17]. VRFB manufacturers usually measure the OCV(SoC) correlation for their particular electrolyte/membrane combination. Using this data, it is possible to convert the measured OCV into the electrolyte SoC. Unfortunately, the OCV(SoC) relations supplied by the manufacturers are confidential. Hence, the Nernst equation, introduced in Section 2.6 on page 35, is used to describe the relationship between the OCV and the SoC. Under the assumption of an equal total vanadium concentration in both electrolytes, Eq. (2-6) can be derived. In the model, this relation is used to determine the combined tank SoC. For an extensive derivation of this correlation, the reader is referred to the Appendix, namely Section B.1 on page 151. 􏱣c2T􏱆 ⋅c5T􏱇 .SoCT 􏰵 c3T􏱆⋅c4T􏱇 (2-6) 1 􏰷 􏱣c2T􏱆⋅c5T􏱇 c3T􏱆 ⋅c4T􏱇 2.3 Concentrations of the ionic species The SoC calculation shows that the concentrations of the ionic species are the basic quantities in the VRFB. The species’ concentration is affected by various processes. While the impact of the applied charging or discharging current on the concentration is intended, several undesired processes, so-called side reactions, also affect the 15

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