Three-dimensional transient modeling and analysis of two-phase mass transfer in air-breathing cathode of a fuel cell

被引:20
作者
Guo, Hang [1 ,2 ]
Chen, Yue Ping [1 ,2 ]
Xue, Yan Qing [1 ,2 ]
Ye, Fang [1 ,2 ]
Ma, Chong Fang [1 ,2 ]
机构
[1] Beijing Univ Technol, Coll Environm & Energy Engn, MOE Key Lab Enhanced Heat Transfer & Energy Conse, Beijing 100124, Peoples R China
[2] Beijing Univ Technol, Coll Environm & Energy Engn, Beijing Key Lab Heat Transfer & Energy Convers, Beijing 100124, Peoples R China
基金
中国国家自然科学基金; 高等学校博士学科点专项科研基金;
关键词
Dynamic models; Fuel cells; Mass transfer; Passive feeding; Three-dimensional; FEED DIRECT METHANOL; WATER TRANSPORT; PERFORMANCE;
D O I
10.1016/j.ijhydene.2013.03.054
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 transport is essential for water and thermal management of passive direct methanol fuel cells (DMFCs). This paper develops a three-dimensional (3D), transient, isothermal and two-phase mixture model and investigates the mass transfer characteristic in the air-breathing cathode of a direct methanol fuel cell. The velocity and volume fraction of species inside the fuel cell along with the process of electrochemical reaction are studied. The effects of several key parameters such as porosity of porous medium, current density and cell operation pressure are investigated to discuss mass transfer characteristic in the passive DMFC cathode. The numerical simulation results indicate that cathode catalyst layer porosity has definite effects on oxygen transfer and removal of water. It is also found that an adequate current density and appropriate cathode pressure could facilitate a more quickly removal of water from the cathode to the ambient. Copyright (C) 2013, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:11028 / 11037
页数:10
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