Holographic interferometry was applied in situ to measure the ionic mass-transfer rates near upward-facing zinc anodes dissolving at high current densities in aqueous KOH solutions. The time-varying interference fringe patterns were converted to individual concentration profiles of Zn͑OH͒ 4 2− , K + , and OH − ions. The measured ionic concentration profiles agreed well with those predicted by a transient diffusion model for a multicomponent electrolyte. When a zinc anode was electrochemically dissolved in 3 wt % KOH electrolyte, the anode potential abruptly shifted in the noble direction, immediately followed by gas evolution. The onset time for this potential rise and accompanying gas evolution agreed well with the calculated time interval required to drive the OH − ion concentration to zero at the zinc electrode surface. The present model can be applied to not only optimize zinc cell designs but also develop a control method for trouble-free, safe operation of a zinc battery without gas evolution.The increasing international awareness of energy and environmental issues has accelerated the development of rechargeable batteries for applications such as fuel cell electric vehicles ͑FCEVs͒ and hybrid electric vehicles ͑HEVs͒. Batteries for mobile telephones, laptop computers, FCEVs, and HEVs share the common requirement of high specific energy and high volumetric energy density; however, FCEV and HEV batteries also require high power density, very low cost, fail-safe operation in series strings, wide operating and survival temperature ranges, and so on. Furthermore, FCEV and HEV batteries must undergo repeated high-rate, shortduration, shallow charge/discharge cycles near a fixed state of charge ͑SOC͒, rather than the slower, deep charge/discharge cycles characteristic of mobile-telephone or laptop-computer batteries. 1 Thus, the search for electrode materials optimized for FCEV or HEV applications is more challenging than that for mobiletelephone or laptop-computer battery materials. In addition to the obvious need to minimize all battery, cell, and component resistances in order to maximize FCEV and HEV battery power and efficiency, there is a strong need to minimize concentration overpotential. This is a particularly complex and challenging problem because during repeated shallow charge/discharge cycles, the concentration overpotential will change due to the accumulated superposition of transient ionic concentration profiles. This superposition occurs because during typical HEV battery operation there is little or no rest period between charging and discharging cycles to allow the electrodes and electrolyte to equilibrate. An important criterion for the design of a rechargeable battery for HEV or FCEV applications is that the charge/discharge cycle must not result in excessive overpotentials.Among the present and candidate batteries for FCEV and HEV are lead acid, nickel cadmium, nickel zinc, nickel metal hydride, and Li-ion. Each of these batteries has certain advantages and disadvantages, which have been discu...