In this work the influence of H2S contamination on commercially available Pt catalyst with carbon support was studied by means of rotating ring-disk electrode experiments in perchloric acid. Accelerated stress testing (AST) was performed in terms of potential cycling up to 10.000 cycles in the absence of contaminants and in the presence of H2S for comparison. Cyclic voltammetry technique in terms of hydrogen under potential deposition (HUPD) and CO stripping was employed in order to determine the electrochemical surface area (ECSA). Oxygen reduction reaction (ORR) was used to identify kinetic parameters including kinetic limited current, Tafel slopes, mass and specific activity of the catalyst before and after degradation.
After AST the platinum degradation was observed in the presence of the contaminant as well as in the absence of H2S. Highly reproducible measurements showed that derived from HUPD and CO methods ECSA in the presence of poisoning species was slightly higher in comparison to the ECSA obtained in the absence of contamination. In contrast, the calculated catalyst activity after stress test in the presence of contaminations dropped more significantly compared to the test without poisoning species. This fact may be attributed to the sulfur adsorption on the catalyst layer leading to morphology changes [3]. Moreover, the increased Tafel slopes after AST may be an indication of the changes of the ORR mechanism from a four electron reaction to a two electron process reaction.
[1] R. Borup, Chemical Reviews 107 (2007) 3904–3951.
[2] Fuel Cell Handbook, US Department of Energy (2008).
[3] R. Mohtadi et al., Electrochemical and Solid-State Letters 6 (2003) A272–A274.
