Numerical investigation of transport component design effect on a proton exchange membrane fuel cell

被引:33
作者
Chiang, Mu-Sheng
Chu, Hsin-Sen [1 ]
机构
[1] Natl Chiao Tung Univ, Dept Mech Engn, Hsinchu 30010, Taiwan
[2] Nan Kai Inst Technol, Dept Mech Engn, Nantou 54243, Taiwan
关键词
proton exchange membrane fuel cell; channel aspect ratio; gas diffusion layer; overpotential; cell performance; reactant concentration;
D O I
10.1016/j.jpowsour.2006.01.086
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 [物理化学]; 081704 [应用化学];
摘要
A numerical investigation of the transport phenomena and performance of a proton exchange membrane fuel cell (PEMFC) with various design parameters of the transport component is presented. A three-dimensional fuel cell model, incorporating conservations of species, momentum, as well as current transport, is used. The Bulter-Volmer equation that describes the electrochemical reaction in the catalyst layer is introduced; the activation overpotential connects the solid phase potential field to that of the electrolyte phase. Through cell performance simulation with various channel aspect ratios and gas diffusion layer (GDL) thicknesses, a slender channel is found suitable for cells operating at moderate reaction rate, and a flat channel produces more current at low cell voltage. Plots of transverse oxygen concentration and phase potential variation indicate that these oppositely affect the local current density pattern. The relative strengths of these two factors depend on the transport component position and geometry, as well as on the cell operating conditions. Consequently, the curves of cell output current density demonstrate that the optimal GDL thickness increases as the cell voltage decreases. However, at the lowest considered cell voltage of 0.14 V optimal thickness decreases as that of a thick GDL. The oxygen deficiency caused by long traveling length and clogging effect of liquid water reverses this relationship. (c) 2006 Elsevier B.V. All rights reserved.
引用
收藏
页码:340 / 352
页数:13
相关论文
共 35 条
[1]
[Anonymous], 1980, SERIES COMPUTATIONAL, DOI [DOI 10.1201/9781482234213, 10.1201/9781482234213]
[2]
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
[3]
Three-dimensional computational analysis of transport phenomena in a PEM fuel cell - a parametric study [J].
Berning, T ;
Djilali, N .
JOURNAL OF POWER SOURCES, 2003, 124 (02) :440-452
[4]
*CFD RES CORP, 2004, CFD ACE U US MAN
[5]
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
[6]
Three-dimensional numerical simulation of straight channel PEM fuel cells [J].
Dutta, S ;
Shimpalee, S ;
Van Zee, JW .
JOURNAL OF APPLIED ELECTROCHEMISTRY, 2000, 30 (02) :135-146
[7]
Influence of the PTFE content in the diffusion layer of low-Pt loading electrodes for polymer electrolyte fuel cells [J].
Giorgi, L ;
Antolini, E ;
Pozio, A ;
Passalacqua, E .
ELECTROCHIMICA ACTA, 1998, 43 (24) :3675-3680
[8]
Two-phase flow model of the cathode of PEM fuel cells using interdigitated flow fields [J].
He, WS ;
Yi, JS ;
Nguyen, TV .
AICHE JOURNAL, 2000, 46 (10) :2053-2064
[9]
Two-dimensional analysis of PEM fuel cells [J].
Hum, B ;
Li, XG .
JOURNAL OF APPLIED ELECTROCHEMISTRY, 2004, 34 (02) :205-215
[10]
A three-dimensional numerical simulation of the transport phenomena in the cathodic side of a PEMFC [J].
Hwang, JJ ;
Chen, CK ;
Savinell, RF ;
Liu, CC ;
Wainright, J .
JOURNAL OF APPLIED ELECTROCHEMISTRY, 2004, 34 (02) :217-224