Mesoscopic modeling of two-phase behavior and flooding phenomena in polymer electrolyte fuel cells

被引:217
|
作者
Mukherjee, Partha P. [1 ,2 ]
Wang, Chao-Yang [1 ,2 ]
Kang, Qinjun [3 ]
机构
[1] Penn State Univ, ECEC, University Pk, PA 16802 USA
[2] Penn State Univ, Dept Mech & Nucl Engn, University Pk, PA 16802 USA
[3] Los Alamos Natl Lab, Los Alamos, NM 87545 USA
基金
美国国家科学基金会;
关键词
Polymer electrolyte fuel cell; Two-phase transport; Flooding phenomena; Lattice Boltzmann model; Stochastic microstructure reconstruction; LATTICE-BOLTZMANN MODEL; DIRECT NUMERICAL-SIMULATION; CAPILLARY-PRESSURE; IMMISCIBLE DROPLET; WATER TRANSPORT; DIFFUSION; FLOW; CATHODE; LAYERS; DISPLACEMENT;
D O I
10.1016/j.electacta.2009.06.066
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 polymer electrolyte fuel cells (PEFC), manifested in terms of mass transport loss, originates from liquid water transport and resulting flooding phenomena in the constituent components. Liquid water covers the electrochemically active sites in the catalyst layer (CL) rendering reduced catalytic activity and blocks the available pore space in the porous CL and fibrous gas diffusion layer (GDL) resulting in hindered oxygen transport to the active reaction sites. The cathode CL and the GDL play a major role in the mass transport loss and hence in the water management of a PEFC. In this work the development of a mesoscopic modeling formalism coupled with realistic microstructural delineation is presented to study the influence of the pore structure and surface wettability on liquid water transport and interfacial dynamics in the PEFC catalyst layer and gas diffusion layer. The two-phase regime transition phenomenon in the capillary dominated transport in the CL and the influence of the mixed wetting characteristics on the flooding dynamics in the GDL are highlighted. (C) 2009 Elsevier Ltd. All rights reserved.
引用
收藏
页码:6861 / 6875
页数:15
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