Tracking the Catalyst Layer Depth-Dependent Electrochemical Degradation of a Bimodal Pt/C Fuel Cell Catalyst: A Combined Operando Small- and Wide-Angle X-ray Scattering Study

催化作用 奥斯特瓦尔德成熟 材料科学 粒径 电解质 粒子(生态学) 化学工程 化学 电极 纳米技术 物理化学 有机化学 工程类 海洋学 地质学
作者
Johanna Schröder,Rebecca K. Pittkowski,Isaac Martens,Raphaël Chattot,Jakub Drnec,Jonathan Quinson,Jacob J. K. Kirkensgaard,Matthias Arenz
出处
期刊:ACS Catalysis [American Chemical Society]
卷期号:12 (3): 2077-2085 被引量:24
标识
DOI:10.1021/acscatal.1c04365
摘要

A combination of operando small- and wide-angle X-ray scattering is here presented to provide insights into the changes in mean particle sizes and phase fractions in fuel cell catalyst layers during accelerated stress tests (ASTs). As a fuel cell catalyst, a bimodal Pt/C catalyst was chosen that consists of two distinguishable particle size populations. The presence of the two different sizes should favor and uncover electrochemical Ostwald ripening as a degradation mechanism, that is, the growth of larger particles in the Pt/C catalyst at the expense of the smaller particles via the formation of ionic metal species. However, instead of electrochemical Ostwald ripening, the results point toward classical Ostwald ripening via the local diffusion of metal atoms on the support. Furthermore, the grazing incidence mode provides insights into the catalyst layer depth-dependent degradation. Although the larger particles show the same particle size changes close to the electrolyte–catalyst interface and within the catalyst layer, the smaller Pt nanoparticles exhibit a slightly decreased size at the electrolyte–catalyst interface. During the AST, both size populations increase in size, independent of the depth. Their phase fraction, that is, the ratio of smaller- to larger-size population, however, exhibits a depth-dependent behavior. Although at the electrolyte–catalyst interface, the phase fraction of the smaller-size population decreases, it increases in the inner catalyst layer. The results of a depth-dependent degradation suggest that employing a depth-dependent catalyst design can be used for future improvement of catalyst stability.
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