In this context, proton exchange membrane (PEM) fuel cells are considered to play a pivotal role in the decarbonization of the mobility sector, as they allow a simple power scaling through a modular stack design, offer a refueling time and range comparable to conventional combustors, but in contrast, are pollutant- and emission-free when green hydrogen is used [2]. In applications with high lifetime requirements, the management of challenging operating conditions is of key importance. Recently, particular attention was paid to cell reversal events triggered by hydrogen starvation, which – without proper countermeasures – lead to a sharp decline in performance within seconds as the carbon-supported catalyst significantly corrodes at the anode [3].
Among other remedies, the incorporation of a co-catalyst, like iridium oxide [4], that favors the harmless oxygen evolution reaction (OER) of water over the destructive carbon oxidation reaction (COR) is broadly employed to improve the intrinsic stability of Pt/C-based anode catalysts. However, the scarcity of platinum and especially iridium makes sophisticated catalyst and electrode concepts indispensable to serve the stability requirements in a resource-saving way. Based on the latest findings and developments, we derived a wide range of material requirements and material adjustments, which in combination enhance the tolerance against hydrogen starvation induced degradation. Incremental improvements of the Pt/C-based anode catalyst form the foundation [5], which is further extended by a broad screening of several iridium-based co-catalysts under application-relevant conditions [6]. As will be emphasized, a careful selection of the anode catalyst system properties not only results in a significant increase in the initial cell reversal tolerance but is also crucial to maintaining this stability after operation under reductive H2 conditions.
References
[1] V. Masson-Delmotte et al., In Press, IPCC: Global Warming of 1.5°C (2018).
[2] O. Gröger et al., J. Electrochem. Soc., 162 (14) A2605-A2622 (2015).
[3] M. F. Tovini et al., J. Electrochem. Soc., 168 064521 (2021).
[4] K. H. Lim et al., J. Electrochem. Soc., 164 (14) F1580-F1586 (2017).
[5] R. Marić, C. Gebauer, F. Eweiner, and P. Strasser, to be submitted.
[6] R. Marić, C. Gebauer, F. Eweiner, and P. Strasser, to be submitted.