• Ehelebe, Konrad
• Milosevic, Maja
• Knöppel, Julius
• López, Daniel Escalera
• Abbas, Dunia
• Cherevko, Serhiy
• Thiele, Simon

Abstract

<jats:p>Sustainable development of the global energy sector requires a transition from fossil fuels to renewable energies. Considering the continuously increasing energy demand, effective utilization of intermittent output from the renewable sources will depend on the efficiency of energy storage and utilization processes. Low chemical complexity and high energy density and efficiency make hydrogen produced via proton exchange membrane water electrolysis (PEMWE) a prominent solution for the mentioned challenges.</jats:p><jats:p>Acidic conditions and high potentials at the anode side of PEM water electrolyzers, where the oxygen evolution reaction (OER) takes place, demand for materials with high catalytic activity and corrosion stability. The state-of-the-art platinum and iridium (oxide) catalysts in the cathode and anode catalyst layers (CLs), respectively, demonstrate relatively good activity and stability during steady operation at low and moderate electrical loads. Indeed, it is anticipated that a significant decrease in the noble metal amount may be achieved without sacrificing the cell performance [1]. An intermittent operation of PEMWE, however, represents a considerable risk factor as both CLs may degrade with time. The extent of such degradation, especially at low catalyst loadings and high current densities, alternated with numerous off cycles is still not well understood and hence, difficult to predict and mitigate.</jats:p><jats:p>Recent results from our group indicate a severe discrepancy between OER catalyst dissolution in aqueous model systems (AMS) and membrane electrode assemblies (MEA), with the main reasons being a suggested discrepancy between estimated and real pH in MEA and stabilization occurring over time [2]. In this work, CLs degradation during dynamic electrolyzer operation in a specially designed PEMWE test station was studied via ex-situ inductively coupled mass spectrometry analysis (ICP-MS) and its influence on the cell’s overall performance was analyzed. The S number, a new metric for OER catalyst lifetime estimation [3], was also used to compare catalyst stability properties within the two systems.</jats:p><jats:p><jats:bold>References:</jats:bold><jats:list list-type="roman-lower"><jats:list-item><jats:p>Bernt, A. Siebel, H. Gasteiger, J. Electrochem. Soc. 165 (5), F305-F314 (2018)</jats:p></jats:list-item><jats:list-item><jats:p>Knöppel, M. Möckl, D. Escalera-Lopez, K. Stojanovski, M. Bierling, T. Böhm, S, Thiele, M. Rzepka, S. Cherevko, Nat. Commun. 12, 2231 (2021)</jats:p></jats:list-item><jats:list-item><jats:p>Geiger, O. Kasian, M. Ledendecker, E. Pizzutilo, A. M. Mingers, W. T. Fu, O. Diaz-Morales, Z. Li, T. Oellers, L. Fruchter, A. Ludwig, K. J. J. Mayrhofer, M. T. M. Koper, Serhiy Cherevko, Nat. Cat. 1, 508 (2018)</jats:p></jats:list-item></jats:list></jats:p><jats:p><jats:bold>Figure 1. Longterm stability of IrOx in AMS and MEA environment.</jats:bold> a) Loading-normalized total dissolved iridium amount at current densities of 0.2 A mg<jats:sub>Ir</jats:sub><jats:sup>-1</jats:sup> and 2 A mg<jats:sub>Ir</jats:sub><jats:sup>-1</jats:sup> in AMS and MEA respectively; b) S-numbers calculated from the amount of dissolved iridium.</jats:p><jats:p><jats:inline-formula><jats:inline-graphic xmlns:xlink="http://www.w3.org/1999/xlink" xlink:href="1369fig1.jpg" xlink:type="simple" /></jats:inline-formula></jats:p><jats:p>Figure 1</jats:p><jats:p />

Topics

• density
• impedance spectroscopy
• energy density
• corrosion
• Oxygen
• Platinum
• Hydrogen
• additive manufacturing
• spectrometry
• Iridium
• inductively coupled plasma mass spectrometry
• Accelerator mass spectrometry