溶解
质子交换膜燃料电池
电解
气体扩散电极
催化作用
化学工程
膜电极组件
扩散
材料科学
聚合物电解质膜电解
电化学
电极
化学
纳米技术
阳极
电解质
热力学
有机化学
物理
物理化学
工程类
作者
Moritz Geuß,Lukas Löttert,Thomas Böhm,Andreas Hutzler,Karl J. J. Mayrhofer,Simon Thiele,Serhiy Cherevko
出处
期刊:ACS Catalysis
[American Chemical Society]
日期:2024-07-24
卷期号:14 (15): 11819-11831
标识
DOI:10.1021/acscatal.4c02159
摘要
Recently, attempts have been made to understand and quantify Ir dissolution in application-relevant single-cell electrolyzers. While obtaining crucial insights, these studies are hindered by intrinsic system complexity and the required labor-intensive microscopic analyses of cross sections of the used catalyst coated membranes. To expand the understanding of dissolution processes in realistic catalyst layers for the oxygen evolution reaction and to accelerate the discovery of dissolution-stable materials, we utilize herein a gas-diffusion type half-cell setup to observe and quantify Ir dissolution at application-relevant conditions. The operation of this setup allows the recording of multiple measurement points for a single electrode throughout an electrochemical protocol and, thus, the monitoring of changes in the dissolution of the Ir-containing catalyst layer over time. The results indicate (I) a temperature-dependent stabilization and activation of the catalyst during conditioning, (II) a beneficial effect on the Ir stability by the application of a protective voltage, and (III) a lower dissolution of Ir from catalyst layers containing rutile IrO2. Therefore, fast benchmarking in a gas-diffusion type setup can accelerate the development of improved dissolution-resistant catalyst layers and aid in developing dissolution-mitigating cell voltage management, which are crucial to achieving significant Ir-loading and cost reduction in proton exchange membrane water electrolysis.
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