Three-dimensional transient two-phase study of the cathode side of a PEM fuel cell

被引:25
|
作者
Khajeh-Hosseini-Dalasm, N. [1 ]
Fushinobu, Kazuyoshi [1 ]
Okazaki, Ken [1 ]
机构
[1] Tokyo Inst Technol, Dept Mech & Control Engn, Meguro Ku, Tokyo 1528552, Japan
关键词
Proton exchange membrane fuel cell; Three-dimensional; Transient; Two-phase; Liquid water production; GAS-DIFFUSION LAYER; MODEL; FLOW; TRANSPORT; WATER; PERFORMANCE; SIMULATION;
D O I
10.1016/j.ijhydene.2010.02.060
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
A three-dimensional transient two-phase isothermal model has been developed for the cathode side of a proton exchange membrane fuel cell (PEMFC). This has been done in order to fully investigate the effects and the time variation of liquid water formation as well as the gas phase transport under the start up condition. It is considered that the generated water in the cathode catalyst layer (CL) is liquid water and that the gas diffusion layer (GDL) is hydrophobic. A non-equilibrium water condensation-evaporation is also assumed. The time variations of liquid water distribution in along-channel and through-plane directions are investigated. This is to determine the liquid water accumulation at the start up time (above the channel under the CL), then the movement of the liquid water in the domain and the final accumulation at the steady state condition (above the rib and near the CL). It has also been found that it takes less time for a high average current density to attain the steady state condition which is due to the capillary pressure gradient inside the porous media. Validation of the numerical results has been implemented via a polarization curve comparison with the experimental data. Both sets show good agreement. (C) 2010 Professor T. Nejat Veziroglu. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:4234 / 4246
页数:13
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