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Figure Captions Figure 1. The normalised performance of two cell designs under full mass transfer reaction control having different porous electrodes and electrolytes. The product kmAe is plotted as a function of pressure drop due to electrolyte flow rate. Pt/Ti electrodes correspond to a laboratory cerium-based RFB and others to a FM01-LC electrolyser [12]. Reprinted with permission from Arenas et al. [14], Pressure drop through platinised titanium porous electrodes for cerium‐based redox flow batteries, AIChE Journal 64(3):1135–46. Copyright (2017) John Wiley and Sons. 26PDF Image | Redox flow batteries for energy storage challenges
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