Two-phase flow pressure drop hysteresis in an operating proton exchange membrane fuel cell

被引:26
作者
Anderson, Ryan [1 ,2 ]
Wilkinson, David P. [1 ,2 ]
Bi, Xiaotao [1 ,2 ]
Zhang, L. [1 ,2 ]
机构
[1] Univ British Columbia, Dept Chem & Biol Engn, Vancouver, BC V6T 1Z3, Canada
[2] Univ British Columbia, Clean Energy Res Ctr, Vancouver, BC V6T 1Z3, Canada
关键词
Two-phase flow; Hysteresis; PEM fuel cell; Water management; LIQUID WATER TRANSPORT; PARALLEL CHANNELS; SINGLE-SERPENTINE; GAS CHANNELS; MANAGEMENT; MALDISTRIBUTION; DISTRIBUTIONS; VISUALIZATION; MINICHANNELS; PERFORMANCE;
D O I
10.1016/j.jpowsour.2011.05.050
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
Two-phase flow pressure drop hysteresis was studied in an operating PEM fuel cell. The variables studied include air stoichiometry (1,5, 2,3,4), temperature (50,75,90 degrees C), and the inclusion of a microporous layer. The cathode channel pressure drops can differ in PEM fuel cells when the current density is increased along a path and then decreased along the same path (pressure drop hysteresis). Generally, the descending pressure drop is greater than the ascending pressure drop at low current densities (<200 mA cm(-2)), and the effect is worse at low stoichiometries and low temperatures. The results show that the hysteresis occurs with or without the inclusion of a microporous layer. Initial results show a modified Lockhart-Martinelli approach seems to be able to predict the two-phase flow pressure drop during the ascending path. The results compare well with photographs taken from the cathode flow field channel of a visualization cell. (C) 2011 Elsevier B.V. All rights reserved.
引用
收藏
页码:8031 / 8040
页数:10
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