CFD Investigation of Pressure Drop Reduction in PEMFC Flow Channels with Distinct Cross-Section Shapes

Mahmut Kaplan
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Abstract

Proton exchange membrane fuel cells (PEMFCs) have great potential to produce renewable, sustainable and clean energy and reduce air pollutants to mitigate climate change. PEMFCs consist of distinct parts including anode and cathode bipolar plates having flow channels, gas diffusion layers, catalyst layers, and membrane. The flow channel geometry influences the the flow and pressure drop characteristics of the channel and cell performance. In this work, a three-dimensional (3D) CFD model is built employing SOLIDWORKS and ANSYS Workbench. The innovative configurations are generated by changing the half of 2 x 2 mm square channel to 0.3 x 0.1 mm, 0.3 x 0.15 mm, 0.3 x 0.2 mm and 0.3 x 0.25 mm rectangular section at the top. The results showed that increasing rectangular section height significantly reduced pressure drop at the anode and cathode with a slight decrease in the current density at 0.4 and 0.6 V. The new configuration with 0.2 x 0.1 mm half square section at the bottom and 0.3 x 0.25 mm rectangular section decreases the current density, anode and cathode pressure drop of 11%, 69% and 58% , respectively in comparison to 0.2 x 0.2 flow channel at 0.4 V. Taking into account pressure loss along the flow channels, this configuration is a good option to improve the cell performance.
具有不同截面形状的 PEMFC 流道压降的 CFD 研究
质子交换膜燃料电池(PEMFCs)在生产可再生、可持续和清洁能源以及减少空气污染物以减缓气候变化方面具有巨大潜力。质子交换膜燃料电池由不同部分组成,包括具有流道的阳极和阴极双极板、气体扩散层、催化剂层和膜。流道的几何形状会影响流道的流量和压降特性以及电池性能。本研究采用 SOLIDWORKS 和 ANSYS Workbench 建立了三维 CFD 模型。通过将 2 x 2 毫米方形通道的一半改为顶部为 0.3 x 0.1 毫米、0.3 x 0.15 毫米、0.3 x 0.2 毫米和 0.3 x 0.25 毫米的矩形截面,产生了创新配置。结果表明,在 0.4 和 0.6 V 电压下,增加矩形截面高度可显著降低阳极和阴极的压降,但电流密度略有下降。与 0.2 x 0.2 流道相比,在 0.4 V 电压下,底部 0.2 x 0.1 毫米半方形截面和 0.3 x 0.25 毫米矩形截面的新配置可使电流密度、阳极和阴极压降分别降低 11%、69% 和 58%。考虑到流道沿线的压力损失,这种配置是提高电池性能的良好选择。
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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