Predicting water and current distributions in a commercial-size PEMFC

被引:124
作者
Shimpalee, S
Greenway, S
Spuckler, D
Van Zee, JW [1 ]
机构
[1] Univ S Carolina, Dept Chem Engn, Columbia, SC 29208 USA
[2] CD Adapco Grp, Melville, NY 11747 USA
关键词
PEM fuel cell; CFD modeling; parallel computing; STAR-CD; flow-field design; water management; large-scale PEMFC;
D O I
10.1016/j.jpowsour.2004.03.059
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
Many researchers have experimentally studied small (similar to 10-50 cm(2)), single cell PEMFC systems to understand the behavior and electrochemistry of PEMFC. Also, three-dimensional electrochemical models have been used to predict the distributions of current, temperature, and species mole fractions as a function of the operating conditions and geometry of small cells and these predictions have been compared with experimental data. However, the commercial viability of PEMFC systems depends on understanding the mass transport and electrochemistry of large-scale electrodes with reacting area on the order of 200-600 cm(2) and numerical investigation of PEMFCs of this size have been effectively impossible without the recent advances in parallel computation and processor speed. This paper applies a parallelized three-dimensional computational fluid dynamics (CFD) model to a 480 cm(2) PEMFC flow-field selected from US patent literature to demonstrate that analysis of large-scale cells is possible. The distributions of pressure, temperature, and electrochemical variables for stationary and automotive operating conditions are examined. Using parallel computing techniques, the computational time is shown to be significantly reduced by increasing the number of processors while maintaining less than 1% error in mass balance. (C) 2004 Elsevier B.V. All rights reserved.
引用
收藏
页码:79 / 87
页数:9
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