Two-Phase Behavior and Compression Effect in the PEFC Gas Diffusion Medium

被引:9
|
作者
Mukherjee, P. P. [1 ]
Wang, C. Y. [2 ]
Schulz, V. P. [3 ]
Kang, Q. [1 ]
Becker, J. [4 ]
Wiegmann, A. [4 ]
机构
[1] Los Alamos Natl Lab, MS T003, Los Alamos, NM 87545 USA
[2] Penn State Univ, Dept Mech & Nucl Engn, Ctr Electrochem Engine, University Pk, PA 16802 USA
[3] APL Landau GmbH, Landau, Germany
[4] Fraunhofer Inst Ind Math ITWM, Kaiserslautern, Germany
来源
PROTON EXCHANGE MEMBRANE FUEL CELLS 9 | 2009年 / 25卷 / 01期
关键词
ELECTROLYTE FUEL-CELLS; MODEL; FLOWS; GDL;
D O I
10.1149/1.3210705
中图分类号
O646 [电化学、电解、磁化学];
学科分类号
081704 ;
摘要
A key performance limitation in the polymer electrolyte fuel cell (PEFC), manifested in terms of mass transport loss, originates from liquid water transport and resulting flooding phenomena in the constituent components. A key contributor to the mass transport loss is the cathode gas diffusion layer (GDL) due to the blockage of available pore space by liquid water thus rendering hindered oxygen transport to the active reaction sites in the electrode. The GDL, therefore, plays an important role in the overall water management in the PEFC. The underlying pore-morphology and the wetting characteristics have significant influence on the flooding dynamics in the GDL. Another important factor is the role of cell compression on the GDL microstructural change and hence the underlying two-phase behavior. In this article, we present the development of a pore-scale modeling formalism coupled with realistic microstructural delineation and reduced order compression model to study the structure-wettability influence and the effect of compression on two-phase behavior in the PEFC GDL.
引用
收藏
页码:1485 / 1494
页数:10
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