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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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Appendix B  Additional data and calculations Appendix B Additional data and calculations Additional data and calculations B.1 CalculationofthetankSoCfromtheelectrolyteOCV In the model, the OCV is derived using the Nernst equation. With the assumption of a constant hydrogen proton concentration, Eq. (A-1) is derived. 􏱸0 GT c2T􏱆 ⋅ c5T+ EOCV 􏰵E 􏰷 F ln􏱳c ⋅c 􏱴 (A-1) Assuming an ideally balanced electrolyte, we can calculate the identical SoCs of both electrolytes as shown in Eq. (A-2). SoCT 􏰵 c2T􏱆 􏰵 c5T􏱇 (A-2) 3T􏱆 4T+ c2T􏱆 􏰷 c3T􏱆 c4T􏱇 􏰷 c5T􏱇 The sum of the concentrations of V2+ and V3+ ions in the negative electrolyte and the sum of the concentrations of VO2+ and VO2+ ions in the positive electrolyte both equal the total vanadium concentration, cV, as shown in Eq. (A-3). c2T􏱆 􏰷 c3T􏱆 􏰵 c4T􏱇 􏰷 c5T􏱇 􏰵 cV (A-3) Now we can express the concentrations exclusively by SoC and total vanadium concentration, as shown in Eq. (A-4). c2T􏱆 SoCT 􏲊c3T􏱆􏲍 􏰵 􏱫1 􏱡 SoCT􏱬 c (A-4) c4T􏱇 1 􏱡 SoCT V c5T􏱇 SoCT If we replace all concentrations in Eq. (A-1) by the expressions using the SoC, we can derive Eq. (A-5), which represents a common simplification for the OCV(SoC) relation. 􏱸0 GT SoCTcVSoCTcV EOCV 􏰵 E + F ln􏱳(1􏱡SoC )c (1􏱡SoC )c 􏱴 TV TV 􏱸0 GT SoCT2 (A-5) 􏰵E+ F ln􏱲􏰻1􏱡SoCT􏱋2􏱵 The comparison of the argument of the logarithmic term in Eq. (A-1) with the one in Eq. (A-5) yields Eq. (A-6). SoCT2 c2T􏱆 ⋅ c5T+ 􏰻1 􏱡 SoCT􏱋2 􏰵 c3T􏱆 ⋅ c4T+ (A-6) Finally, a SoC dependence on all four different vanadium ions can be derived, as shown in Eq. (A-7). 151

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