Hydroxide exchange membrane electrolyzers (HEMELs) stand to be an effective means of achieving low-cost green hydrogen. However, HEMEL durability remains a substantial barrier to realizing this goal. The United States Department of Energy has set a durability target of a voltage increase of 2 µV/hr1. We have previously demonstrated constant current degradation rates of 1810 and 560 µV/hr with applied current densities of 500 and 200 mA/cm2, respectively, thus illustrating the substantial gap between our current achievable HEMEL durability and our target durability2.Gaseous products are formed at both electrodes in a HEMEL; by manipulating the wettability of the electrodes, recent studies have shown that the failure of gas bubbles to detach from the electrode surface leads to overpotentials associated with the loss of accessible reaction sites and exacerbated mass transport to those sites that remain accessible3,4. While these studies have demonstrated the impact of gas bubbles on acute water electrolyzer performance, we have found little work to investigate the impact of trapped gas bubbles from a durability perspective.Here we find that electrode wettability can change throughout the lifetime of a device. We investigate the durability of an FexNiyOOH – nF anode catalyst supported on nickel felt in a three-electrode setup with 1M KOH. We find that at a moderately low current density of 50 mA/cm2 the performance of this catalyst degrades by tens of mV over several hundred hours and that this performance loss is recoverable with the removal of oxygen bubbles adhered to the anode surface at open circuit. Moreover, when we resume the passage of current, the surface layer of oxygen (and associated performance loss) evolves more rapidly – suggesting that the wettability of the anode has decreased throughout the experiment. This is further supported by contact angle measurements of pre- and post-mortem anodes. Finally, we investigate whether the introduction of hydrophilic ion-conducting polymers can mitigate the emergent hydrophobicity of the anode catalyst layer. Technical Targets for Proton Exchange Membrane Electrolysis, Hydrogen and Fuel Cell Technologies Office. https://www.energy.gov/eere/fuelcells/technical-targets-proton-exchange-membrane-electrolysis. J. Xiao et al., ACS Catal., 11, 264-270 (2021). R. Iwata et al., Joule, 5(4), 887-900 (2021). Z. Kang et al., Electrochimica Acta, 354 (2020).
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