Influences of bipolar plate channel blockages on PEM fuel cell performances

被引:194
作者
Heidary, Hadi [1 ]
Kermani, Mohammad J. [1 ,2 ]
Dabir, Bahram [3 ]
机构
[1] Amirkabir Univ Technol, Tehran Polytech, Dept Mech Engn, Tehran 158754413, Iran
[2] Ctr Solar Energy & Hydrogen Res ZSW, Helmholtzstr 8, D-89081 Ulm, Germany
[3] Amirkabir Univ Technol, Tehran Polytech, Dept Chem Engn, Tehran 158754413, Iran
基金
美国国家科学基金会;
关键词
Computational fluid dynamics; PEM fuel cells; Flow-field channels; Blockage; Pressure drop; INTERDIGITATED FLOW-FIELDS; HEAT-TRANSFER ENHANCEMENT; SINGLE-SERPENTINE; EXCHANGE; TRANSPORT; PARALLEL; PARAMETERS; GEOMETRY; DESIGNS;
D O I
10.1016/j.enconman.2016.06.043
中图分类号
O414.1 [热力学];
学科分类号
摘要
In this paper, the effect of partial- or full-block placement along the flow channels of PEM fuel cells is numerically studied. Blockage in the channel of flow-field diverts the flow into the gas diffusion layer (GDL) and enhances the mass transport from the channel core part to the catalyst layer, which in turn improves the cell performance. By partial blockage, only a part of the channel flow is shut off. While in full blockage, in which the flow channel cross sections are fully blocked, the only avenue left for the continuation of the gas is to travel over the blocks via the porous zone (GDL). In this study, a 3D numerical model consisting of a 9-layer PEM fuel cell is performed. A wide spectrum of numerical studies is performed to study the influences of the number of blocks, blocks height, and anode/cathode-side flow channel blockage. The results show that the case of full blockage enhances the net electrical power more than that of the partial blockage, in spite of higher pressure drop. Performed studies show that full blockage of the cathode-side flow channels with five blocks along the 5 cm channel enhances the net power by 30%. The present work provides helpful guidelines to bipolar plate manufacturers. (C) 2016 Elsevier Ltd. All rights reserved.
引用
收藏
页码:51 / 60
页数:10
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