Effect of process conditions on dynamics and performance of PEMFC: Comparison with experiments

被引:1
|
作者
Park, Hye Yeon [1 ]
Hwang, Ji Won [1 ]
Park, Ki Tae [1 ]
Kim, Sunhoe [2 ]
Jeong, Yeon Uk [3 ]
Jung, Hyun Wook [1 ]
Kim, Sung Hyun [1 ]
机构
[1] Korea Univ, Dept Chem & Biol Engn, Seoul 136713, South Korea
[2] Sangji Univ, Dept Minerals & Min Engn, Wonju 220702, South Korea
[3] Kyungpook Natl Univ, Sch Mat Sci & Engn, Taegu 702701, South Korea
关键词
Proton-exchange membrane fuel cell; Polarization curve; Cell design; CFD simulation; Relative humidity; Cell configuration; MEMBRANE FUEL-CELL; MATHEMATICAL-MODEL; WATER; FLOW; MANAGEMENT; CATHODE; GDL;
D O I
10.1016/j.tsf.2010.01.051
中图分类号
T [工业技术];
学科分类号
08 ;
摘要
Three-dimensional numerical computations have been carried out to investigate the dynamics inside proton-exchange membrane fuel cell (PEMFC) and its performance using Star-CD solver, the computational fluid dynamics software. Theoretical results in polarization curves quantitatively corroborate the experimental findings previously reported in Jung et al. [2]. Also, effects of various process conditions such as relative humidity, stoichiometric ratio at anode and cathode channels, and cell configuration on the performance of fuel cell have been further scrutinized. It has been revealed that the moderately high stoichiometric ratio at cathode channel and single serpentine geometry improve the cell performance and also the humidity change at cathode makes the cell voltage variation high, comparing with the humidity change at anode. (C) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:6505 / 6509
页数:5
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