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Source/Load OCVout ⊖⊕ V2+ V3+ V4+ V5+ ··· V2+ V3+ V4+ V5+ ··· V2+ V3+ V4+ V5+ Positive Tank V4+/V5+ ⊖⊕ Q−1 Q+1 Q−k Q+k Q−N Q+N ⊖⊕ OCVin Figure 1: Schematic diagram of a multi-cell stack VRB system. concentrations in the tank, denoted as ct,2, ct,3, ct,4 and ct,5, can be modelled as follows [5]: d 1k2 k4 k5 1 1 dtcc,2 =−W dcc,2+ dcc,4+2dcc,5 +ML W H (ct,2−cc,2)Q+nL W H FI, pe pe pe pe pe pe pe d 1k3 k4 k5 1 1 dtcc,3 =−W dcc,3−2dcc,4−3dcc,5 +ML W H (ct,3−cc,3)Q−nL W H FI, pe pe pe pe pe pe pe d 1k2 k3 k4 1 1 dtcc,4 =−W −3dcc,2−2dcc,3+ dcc,4 +ML W H (ct,4−cc,4)Q−nL W H FI, pe pe pe pe pe pe pe d 1k2 k3 k5 1 1 dtcc,5 =−W 2dcc,2+ dcc,3+ dcc,5 +ML W H (ct,5−cc,5)Q+nL W H FI, Negative Tank V2+/V3+ pe d ct,2 = 1 (cc,2 − ct,2)Q, pe pe pe pe pe pe dt Vt d ct,3 = 1 (cc,3 − ct,3)Q, dt Vt d ct,4 = 1 (cc,4 − ct,4)Q, dt Vt d ct,5 = 1 (cc,5 − ct,5)Q, dt Vt 4 (3)PDF Image | Electrolyte Flow Rate Control Vanadium Redox Flow Batteries
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