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Section 8.9 Summary Concentration overpotential Energy required for running the pumps 3.5 3 2.5 2 1.5 1 0.5 0 Figure 8-16: Losses due to concentration overpotential and pump power demand over applied current for the two variable FRCS strategies for cell design 2.5, optimized for capacity Conve ntional variable FRCS Innovative variable FRCS 40 60 80 100 120 140 160 180 200 Charging/discharging current in A 141PDF Image | Model-based Design Vanadium Redox Flow Batteries
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