A comparison of different approaches to modelling the PEMFC catalyst layer

被引:114
作者
Harvey, D. [1 ,2 ,4 ]
Pharoah, J. G. [1 ,2 ]
Karan, K. [1 ,3 ]
机构
[1] Queens RMC Fuel Cell Res Ctr, Kingston, ON, Canada
[2] Queens Univ, Dept Mech Engn, Kingston, ON K7L 3N6, Canada
[3] Queens Univ, Dept Chem Engn, Kingston, ON K7L 3N6, Canada
[4] Ballard Power Syst, Burnaby, BC, Canada
关键词
PEMFC; catalyst agglomerate; CFD; performance modelling; cathode; mass transport;
D O I
10.1016/j.jpowsour.2007.12.077
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
This paper compares three different approaches for describing the cathode catalyst layer of a PEMFC, using a three-dimensional CID model. The three catalyst treatments include: a thin-film model, a discrete-catalyst volume model and an agglomerate model. It is shown that, within a single-phase approach using physically meaningful parameters, the commonly employed thin-film or discrete-volume descriptions of the catalyst layer do not show the significant mass transport limitations which occur at higher current densities; while this region is observed using a catalyst agglomerate approach. Further, an in-depth analysis of the current density distributions indicates that for a given electrode overpotential the thin film model significantly over-predicts the current density, compared to the discrete and agglomerate approaches. The thin-film model also greatly exaggerates the variation in current density both along and across the channel. Finally, the agglomerate model predicts noticeable mass transport losses even at very low current densities despite the use of high stoichiometric ratios and thin-electrolyte films. (C) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:209 / 219
页数:11
相关论文
共 42 条
[1]  
BANG M, 2003, P C HYDR FUEL CELLS
[2]  
BANG M, 2004, P 2 INT C FUEL CELL
[3]   Water management in PEM fuel cells [J].
Berg, P ;
Promislow, K ;
St Pierre, J ;
Stumper, J ;
Wetton, B .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 2004, 151 (03) :A341-A353
[4]   Three-dimensional computational analysis of transport phenomena in a PEM fuel cell [J].
Berning, T ;
Lu, DM ;
Djilali, N .
JOURNAL OF POWER SOURCES, 2002, 106 (1-2) :284-294
[5]   A 3D, multiphase, multicomponent model of the cathode and anode of a PEM fuel cell [J].
Berning, T ;
Djilali, N .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 2003, 150 (12) :A1589-A1598
[6]  
BERNING T, 2002, THESIS U VICTORIA
[7]  
BOCTOR SA, 1997, ELECT CONCEPTS APPL
[8]   Water transport in polymer membranes for PEMFC [J].
Choi, KH ;
Peck, DH ;
Kim, CS ;
Shin, DR ;
Lee, TH .
JOURNAL OF POWER SOURCES, 2000, 86 (1-2) :197-201
[9]  
CUSSLER E. L., 1997, DIFFUSION MASS TRANS
[10]   Numerical prediction of mass-exchange between cathode and anode channels in a PEM fuel cell [J].
Dutta, S ;
Shimpalee, S ;
Van Zee, JW .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2001, 44 (11) :2029-2042