Experimental investigation on scaling and stacking up of proton exchange membrane fuel cells

被引:34
|
作者
Karthikeyan, P. [1 ]
Velmurugan, P. [1 ]
George, Abby Joseph [1 ]
Kumar, R. Ram [1 ]
Vasanth, R. J. [1 ]
机构
[1] PSG Coll Technol, Dept Automobile Engn, Coimbatore 641004, Tamil Nadu, India
关键词
Back pressure; Scaling and stacking up; Serpentine and interdigitated flow channels; Cooling channels; Forced and natural convection; FLOW-FIELD; PERFORMANCE;
D O I
10.1016/j.ijhydene.2014.05.086
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
The performance of a proton exchange membrane fuel cell (PEMFC) with various flow channel design (serpentine and interdigitated) with different landing to channel ratios (L:C = 1:1; 2:2) for an active area of 25 cm(2) and 70 cm(2), for single cell and two cells stack is studied and compared. The effect of back pressure on the PEMFC performance is also investigated. This study establishes a strong relation between back pressure and power output from a PEMFC. It was concluded that the interdigitated flow channel gives better results than the serpentine flow channel configuration for various landing to channel ratios. It was also found that power outputs do not proportionally increase with active area of the membrane electrode assembly (MEA). Similarly, stacking up studies with single cell and two cell stack shows that the two cell stack has reduced power densities when compared to that of a single cell. The effect of cooling channels with natural and forced convection by using induced draught fan on the performance of a PEMFC stack is also studied. Fuel distribution and temperature management are found to be the significant factors which determine the performance of a PEMFC stack. Copyright (C) 2014, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:11186 / 11195
页数:10
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