Analysis of mass transport of methanol at the anode of a direct methanol fuel cell

被引:67
|
作者
Xu, C.
He, Y. L.
Zhao, T. S.
Chen, R.
Ye, Q.
机构
[1] Hong Kong Univ Sci & Technol, Dept Mech Engn, Kowloon, Hong Kong, Peoples R China
[2] Xi An Jiao Tong Univ, Sch Energy & Power Engn, Xian 710049, Peoples R China
关键词
D O I
10.1149/1.2201467
中图分类号
O646 [电化学、电解、磁化学];
学科分类号
081704 ;
摘要
We present an analysis of the mass transport of methanol at the anode of a direct methanol fuel cell (DMFC) and show that the overall mass-transfer coefficient can be determined by measuring the cell limiting current density. We measured the cell limiting current density of an in-house-fabricated DMFC with different flow fields for various methanol concentrations and flow rates of methanol solution. The experimental data showed that the overall mass-transfer coefficient was nearly independent of current density, although the rate of CO2 gas bubble liberation changed with current density. We found that the overall methanol-transfer coefficient in the serpentine flow field could be significantly increased with increased methanol flow rate due to the enhanced under-rib convection. We developed the correlation equations predicting the overall methanol transfer coefficient in terms of the methanol flow rate for a given DMFC hardware. Finally, we showed that the polarization curves predicted based on the correlation equation of the overall mass-transfer coefficient in the DMFC with the serpentine flow field for different flow rates were in fairly good agreement with the experimental data. (c) 2006 The Electrochemical Society.
引用
收藏
页码:A1358 / A1364
页数:7
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