A three-dimensional full-cell CFD model used to investigate the effects of different flow channel designs on PEMFC performance

被引:145
作者
Ferng, Yuh Ming [1 ]
Su, Ay [2 ]
机构
[1] Fuel Cell Ctr, Tao Yuan 32026, Taiwan
[2] Yuan Ze Univ, Dept Mech Engn, Chungli 320, Taiwan
关键词
PEMFC; flow channel design; CFD;
D O I
10.1016/j.ijhydene.2007.05.012
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
A three-dimensional "full-cell" computational fluid dynamics (CFD) model is proposed in this paper to investigate the effects of different flow channel designs on the performance of proton exchange membrane fuel cells (PEMFC). The flow channel designs selected in this work include the parallel and serpentine flow channels, single-path and multi-path flow channels, and uniform depth and step-wise depth flow channels. This model is validated by the experiments conducted in the fuel cell center of Yuan Ze University, showing that the present model can investigate the characteristics of flow channel for the PEMFC and assist in the optima designs of flow channels. The effects of different flow channel designs on the PEMFC performance obtained by the model predictions agree well with those obtained by experiments. Based on the simulation results, which are also confirmed by the experimental data, the parallel flow channel with the step-wise depth design significantly promotes the PEMFC performance. However, the performance of PEMFC with the serpentine flow channel is insensitive to these different depth designs. In addition, the distribution characteristics of fuel gases and current density for the PEMFC with different flow channels can be also reasonably captured by the present model. (c) 2007 International Association for Hydrogen Energy. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:4466 / 4476
页数:11
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