质子交换膜燃料电池内传输反应过程中阴极催化剂层降解的格子Boltzmann模拟

Yulin Wang , Xiangling Liao , Haokai Xu , Wei He , Hua Li , Lei Xing , Xiaodong Wang
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引用次数: 1

摘要

催化剂层的降解显著影响多孔电极中的气体传输和电化学过程,从而影响质子交换膜燃料电池的性能。为了揭示催化剂层降解的影响,本工作采用随机算法重建了阴极催化剂层的微观多孔结构。因此,使用Lattice Boltzmann方法研究了极限电流密度条件下的氧传输和电化学反应过程,分别考虑了铂、碳颗粒和离聚物在均匀和指数降解速率下的降解。结果表明,铂的降解降低了催化剂层中的反应位点,从而恶化了电化学动力学并降低了总反应速率。相反,碳和离聚物的降解表现出两种截然相反的效果。一方面,由于碳和离聚物的降解,特别是离聚物降解,氧传输得到改善,从而加快了总反应速率。另一方面,碳和离聚物的降解引发铂颗粒的分离,导致反应速率降低。在多组分同时降解过程的早期阶段,总反应速率受到催化剂层内氧传输限制的限制;随着降解程度的增加,氧在离聚物膜中的传输增强,电化学动力学成为速率的决定因素,尤其是指数降解速率。本研究对不同程度的催化剂层降解情况下催化剂层内的氧传输和电化学反应进行了全面评估,可指导下一代燃料电池高性能抗降解催化剂层的设计。
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Lattice Boltzmann simulation of cathode catalyst layer degradation on transport reaction process within a proton exchange membrane fuel cell

The degradation of the catalyst layer significantly affects the gas transport and electrochemical processes in the porous electrodes, thus affecting the performance of proton exchange membrane fuel cells. To reveal the catalyst layer degradation impact, the microscopic porous structure of the cathode catalyst layer was reconstructed by a random algorithm in this work. Consequently, Lattice Boltzmann method was used to study the oxygen transport and electrochemical reaction processes at the limiting current density condition with considering the degradation of platinum, carbon particles, and ionomers under uniform and exponential degradation rates, respectively. The results reveal that the degradation of platinum reduces the reaction sites in the catalyst layer, thus deteriorating the electrochemical kinetics and lowering the total reaction rate. On the contrary, the degradation of carbon and ionomer shows two diametrically opposed effects. On the one hand, the oxygen transport is improved due to carbon and ionomer degradation, especially for ionomer degradation, thereby accelerating the total reaction rate. On the other hand, the degradation of carbon and ionomer triggers the detachment of platinum particles, leading to a decrease in reaction rate. In the early stages of the multi-component simultaneous degradation process, the total reaction rate is prohibited by oxygen transport limitation inside the catalyst layer; as the degradation degree increases, the oxygen transport through the ionomer films is enhanced and the electrochemical kinetics becomes the rate determining factor, especially for exponential degradation rate. This study provides a comprehensive assessment of the oxygen transport and electrochemical reaction within the catalyst layers with respect to different degrees of catalyst layer degradation, which can guide the design of high-performance anti-degradation catalyst layers for the next generation of fuel cells.

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