Two-phase flow and maldistribution in gas channels of a polymer electrolyte fuel cell

被引:73
作者
Basu, Suman [1 ,2 ]
Li, Jun [1 ,2 ]
Wang, Chao-Yang [1 ,2 ]
机构
[1] Penn State Univ, Dept Mech & Nucl Engn, University Pk, PA 16802 USA
[2] Penn State Univ, ECEC, University Pk, PA 16802 USA
基金
美国国家科学基金会;
关键词
PEFC; Two-phase flow; Gas channel; Flow maldistribution; Pressure drop; LIQUID WATER TRANSPORT; EXCHANGE; CATHODE; MODEL; MULTICOMPONENT; PREDICTION; MULTIPHASE; VISUALIZATION; PERFORMANCE; MANIFOLDS;
D O I
10.1016/j.jpowsour.2008.11.039
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
Liquid water transport in a polymer electrolyte fuel cell (PEFC) is a major issue for automotive applications. Mist flow with tiny droplets suspended in gas has been commonly assumed for channel flow while two-phase flow has been modeled in other cell components. However. experimental studies have found that two-phase flow in the channels has a profound effect on PEFC performance, stability and durability. Therefore, a complete two-phase flow model is developed in this work for PEFC including two-phase flow in both anode and cathode channels. The model is validated against experimental data of the wetted area ratio and pressure drop in the cathode side. Due to the intrusion of soft gas diffusion layer (GDL) material in the channels, flow resistance is higher in some channels than in others. The resulting flow maldistribution among PEFC channels is of great concern because non-uniform distributions of fuel and oxidizer result in non-uniform reaction rates and thus adversely affect PEFC performance and durability. The two-phase flow maldistribution among the parallel channels in an operating PEFC is explored in detail. (C) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:431 / 443
页数:13
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