Visualization and analysis of mass transfer phenomena in a three dimensional domain of a low temperature PEMFC

B. Abderezzak, B. Khelidj, M. T. Abbes
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Abstract

The proton exchange membrane fuel cell (PEMFC) is considered as a potential candidate of the hydrogen applications on the power sources in the future. This work depicts the steady-state single phase transport of reactants and water in a three dimensional computational domain of a low temperature Polymer Electrolyte Membrane Fuel Cell. The model computational domain includes anode and cathode flow channels, gas diffusion layers, membrane and catalyst layers. Both anode and cathode mass and momentum transport phenomena in the flow channels, gas diffusion layers (GDLs) and porous electrodes are included in this study. A Computational Fluid Dynamics code using the finite element method (FEM) is applied on the studied domain. Water analysis in the membrane will be discussed in further works. Mass transfer analysis focused on the air flow velocity parameter, a range of values is applied to observe its effect Simulation results show an important molar concentration of water in the cathode side compared to a low one in the anode side. A good oxygen concentration is obtained with an air flow velocity of 0.5 m/s, increasing this value may cause the membrane flooding phenomena.
低温PEMFC三维传质现象的可视化与分析
质子交换膜燃料电池(PEMFC)被认为是未来氢能源应用的潜在候选。本文描述了低温聚合物电解质膜燃料电池中反应物和水在三维计算域中的稳态单相输运。模型的计算域包括阳极和阴极流道、气体扩散层、膜层和催化剂层。本文研究了流道、气体扩散层和多孔电极中阳极和阴极的质量和动量输运现象。采用有限元方法编制了计算流体力学程序。膜中的水分析将在以后的工作中讨论。传质分析的重点是气流速度参数,采用一定范围的数值来观察其影响。模拟结果表明,水在阴极侧的摩尔浓度较高,而在阳极侧的摩尔浓度较低。当空气流速为0.5 m/s时,氧浓度较好,增大该值可能引起膜泛洪现象。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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