Numerical study on channel size effect for proton exchange membrane fuel cell with serpentine flow field

被引:125
|
作者
Wang, Xiao-Dong [2 ]
Yan, Wei-Mon [1 ]
Duan, Yuan-Yuan [3 ]
Weng, Fang-Bor [4 ]
Jung, Guo-Bin [4 ]
Lee, Chi-Yuan [4 ]
机构
[1] Huafan Univ, Dept Mechatron Engn, Taipei 22305, Taiwan
[2] Univ Sci & Technol Beijing, Dept Thermal Engn, Sch Mech Engn, Beijing 100083, Peoples R China
[3] Tsinghua Univ, Key Lab Thermal Sci & Power Engn, Minist Educ, Beijing 100084, Peoples R China
[4] Yuan Ze Univ, Fuel Cell Ctr, Dept Mech Engn, Tao Yuan 32003, Taiwan
关键词
Proton exchange membrane fuel cell; Two-phase model; Serpentine flow field; Flow channel size; LOCAL TRANSPORT PHENOMENA; MATHEMATICAL-MODEL; PART I; PERFORMANCE; WATER; SIMULATION; PREDICTIONS; MANAGEMENT; CATHODE; DESIGN;
D O I
10.1016/j.enconman.2009.11.037
中图分类号
O414.1 [热力学];
学科分类号
摘要
This work numerically investigates the effect of the channel size on the cell performance of proton exchange membrane (PEM) fuel cells with serpentine flow fields using a three-dimensional, two-phase model. The local current densities in the PEM, oxygen mass flow rates and liquid water concentrations at the interface of the cathode gas diffusion layer and catalyst layer were analyzed to understand the channel size effect. The predictions show that smaller channel sizes enhance liquid water removal and increase oxygen transport to the porous layers, which improve cell performance. Additionally, smaller channel sizes also provide more uniform current density distributions in the cell. However, as the channel size decreases, the total pressure drops across the cell increases, which leads to more pump work. With taking into account the pressure losses, the optimal cell performance occurs for a cell with a flow channel cross-sectional area of 0.535 x 0.535 mm(2). (C) 2009 Elsevier Ltd. All rights reserved.
引用
收藏
页码:959 / 968
页数:10
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