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Analyzing oxygen transport resistance and Pt particle growth effect in the cathode catalyst layer of polymer electrolyte fuel cells

机译:聚合物电解质燃料电池阴极催化剂层中的氧传输性和Pt颗粒生长效应分析

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The oxygen transport resistance in the cathode catalyst layer (CL) of polymer electrolyte fuel cells (PEFCs) has been reported to be significantly higher than expected, especially when the platinum (Pt) loading is low and/or the degree of CL degradation is severe. In this paper, the oxygen transport resistance behavior in the cathode CL is numerically analyzed under various CL design and operating conditions. Particular emphasis is placed on the aged CL wherein Pt particle growth and active Pt surface area loss are observed. For this study, a previously developed micro-scale catalyst model is improved upon to account for Pt particle size. The new model includes calculations of catalyst activity and electrochemically active surface areas, as well as various transport resistances through the ionomer and liquid films. After coupling the micro-scale CL model with a three-dimensional PEFC model, multi-scale simulations are carried out under various PEFC catalyst designs (varying Pt loading, ionomer fraction, oxygen permeation rate through the ionomer film) and operating conditions (drying or flooding of the electrode, high or lower current density). The simulation results agree well with experimental oxygen transport resistance data and further indicate that CL design with low Pt loading is more susceptible to degradation. Providing extensive multi-dimensional contours of species concentration, temperature, and current density inside the PEFC, this study provides a comprehensive understanding of oxygen transport resistance in the cathode CL in different PEFC situations. (C) 2020 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
机译:据报道,聚合物电解质燃料电池(PEFC)的阴极催化剂层(CL)中的氧传输性显着高于预期,特别是当铂(Pt)负载低和/或降解程度严重时。本文在各种CL设计和操作条件下进行了数量分析了阴极CL中的氧传输性能。将特别强调放置在老年的Cl上,其中观察到Pt颗粒生长和活性Pt表面积损失。对于该研究,先前显影的微级催化剂模型得到改善以考虑Pt粒径。新模型包括催化剂活性和电化学活性表面积的计算,以及通过离聚物和液体膜的各种传输电阻。在用三维PEFC模型耦合微级CL模型后,在各种PEFC催化剂设计下进行多尺度模拟(改变Pt加载,离聚物级分,通过离聚物膜的氧渗透速率)和操作条件(干燥或泛滥电极,高或较低的电流密度)。仿真结果与实验氧传输抗性数据吻合良好,并进一步表明具有低Pt负载的CL设计更容易降解。本研究提供了PEFC内部浓度,温度和电流密度的广泛的多维轮廓,在不同PEFC情况下,为阴极CL中的氧气传输性综合了解。 (c)2020氢能源出版物LLC。 elsevier有限公司出版。保留所有权利。

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