Calculation procedure for mass transfer in fuel cells

被引:18
作者
Beale, SB [1 ]
机构
[1] Natl Res Council Canada, Ottawa, ON K1A 0R6, Canada
关键词
fuel cells; transport phenomena; mass transfer; concentration polarisation; over-potential; diffusion;
D O I
10.1016/j.jpowsour.2003.09.053
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
An analysis of mass transfer losses, or concentration over-potentials in fuel cells is provided. An elementary theory, based on an equivalent film thickness, as proposed in some texts, is derived. This is followed by a more rigorous theoretical treatment of mass transfer theory, for which the mass transfer factor is obtained as a function of the driving force. The solution for the driving force is derived, for the well-known one-dimensional convection-diffusion problem. It is shown that mass transfer in planar and square geometries approximates this idealised situation. A linearised theory, appropriate for low mass flow rates is also presented. The methodology is illustrated using the simple example of a solid oxide fuel cell (SOFC). It is shown that the simplified theory is only applicable for very dilute binary mixtures. A step-by-step procedure for computing mass transfer in fuel cells is detailed, together with a discussion of the scope and range of application of the results. (C) 2004 National Research Council of Canada. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:185 / 192
页数:8
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