Effects of two-phase transport in the cathode gas diffusion layer on the performance of a PEMFC

被引:30
作者
Chang, Min-Hsing [1 ]
Chen, Falin
Teng, Hong-She
机构
[1] Yung Ta Inst Technol & Commerce, Dept Mech Engn, Pingtung 909, Taiwan
[2] Natl Taiwan Univ, Inst Appl Mech, Taipei 10764, Taiwan
关键词
PEM fuel cell; cathode gas diffusion layer; two-phase flow;
D O I
10.1016/j.jpowsour.2006.01.027
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 study investigates the characteristics of transport phenomena in the cathode gas diffusion layer (GDL) of a proton exchange membrane fuel cell (PEMFC) and their influences on cell performance by utilizing a two-phase flow model based on a multiphase mixture formulation. The profiles of liquid water saturation and oxygen concentration across the GDL are obtained by a direct numerical procedure, and the corresponding polarization curves are determined as well. The results show that the liquid water generated by the electrochemical reaction could significantly reduce the effective porosity of the GDL under high current density conditions to hinder oxygen transport through the GDL. The removal rate of liquid water due to capillarity-induced motion can be enhanced conspicuously by an increase in hydrophobicity at first, and this effect then diminishes gradually. The effects of porosity and thickness of the GDL, inlet velocity of reactant gas, and gas channel length on the cell performance are also examined in detail. The results provide insights into the transport mechanisms in the GDL and benefit the design of PEMFCs. (c) 2006 Elsevier B.V. All rights reserved.
引用
收藏
页码:268 / 276
页数:9
相关论文
共 23 条
[1]  
[Anonymous], 1995, PRINCIPLE HEAT TRANS
[2]   Modelling of polymer electrolyte membrane fuel cells with variable degrees of water flooding [J].
Baschuk, JJ ;
Li, XH .
JOURNAL OF POWER SOURCES, 2000, 86 (1-2) :181-196
[3]   A MATHEMATICAL-MODEL OF THE SOLID-POLYMER-ELECTROLYTE FUEL-CELL [J].
BERNARDI, DM ;
VERBRUGGE, MW .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 1992, 139 (09) :2477-2491
[4]   MATHEMATICAL-MODEL OF A GAS-DIFFUSION ELECTRODE BONDED TO A POLYMER ELECTROLYTE [J].
BERNARDI, DM ;
VERBRUGGE, MW .
AICHE JOURNAL, 1991, 37 (08) :1151-1163
[5]   WATER-BALANCE CALCULATIONS FOR SOLID-POLYMER-ELECTROLYTE FUEL-CELLS [J].
BERNARDI, DM .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 1990, 137 (11) :3344-3350
[6]   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
[7]   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
[8]   WATER AND THERMAL MANAGEMENT IN SOLID-POLYMER-ELECTROLYTE FUEL-CELLS [J].
FULLER, TF ;
NEWMAN, J .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 1993, 140 (05) :1218-1225
[9]   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
[10]  
Meredith R.E., 1962, ADV ELECTROCHEMICAL