The electrochemical characteristics of lab prepared Pt vertical bar Nafion and commercial Pt-C vertical bar Nafion air fuel cell electrodes in sulfuric and chromic acid electrolytes were examined to help in the design of an electrochemical system that might potentially be used in the regeneration of spent chromium plating solutions to save energy. In both solutions, the Pt-C vertical bar Nafion electrode obtained higher cathodic currents from oxygen reduction than the PtINafion electrode, mainly due to an order of magnitude greater active area in the Pt-C vertical bar Nafion than in the Pt vertical bar Nafion electrode. The currents significantly increased after the cathodic sweeps passed similar to 0.7-0.8 V versus a standard hydrogen electrode (SHE) in both systems. The currents for the oxygen reduction reactions were higher in the sulfuric acid system than in the chromic acid system, which were associated with less available electroactive sites on the electrodes and/or the inhibition of oxygen reduction in the chromic acid. In addition, impurities (i.e., Cu) were more difficult to deposit on Pt in the chromic acid than in the sulfuric acid. In sulfuric acid, the Tafel slopes were similar for the two electrodes, but in chromic acid, the Pt-C vertical bar Nafion electrode had a Tafel slope close to -120 mV decade(-1) while the Pt vertical bar Nafion did not have a clear Tafel region in similar to 600-400 mV versus Ag/AgCl. The polarization results suggest that, in practical applications, flooding, if it occurs, will be more responsible than slow oxygen reduction kinetics for the cathodic potential/cell voltage increase in the fuel cell cathode system using chromic acid. (c) 2004 Elsevier B.V. All rights reserved.