Numerical modeling and performance prediction of water transport for PEM fuel cell

被引:3
作者
Shao, Yangbin [1 ,2 ]
Xu, Liangfei [1 ,2 ]
Li, Jianqiu [1 ,2 ]
Ouyang, Minggao [1 ]
机构
[1] Tsinghua Univ, State Key Lab Automot Safety & Energy, Beijing 100084, Peoples R China
[2] Collaborat Innovat Ctr Elect Vehicles Beijing, Beijing 100081, Peoples R China
来源
INNOVATIVE SOLUTIONS FOR ENERGY TRANSITIONS | 2019年 / 158卷
基金
国家重点研发计划; 中国国家自然科学基金;
关键词
current density; liquid water distribution; two phase flow; cathode; model prediction; model simulation; 2-PHASE FLOW; CATHODE; EXCHANGE;
D O I
10.1016/j.egypro.2019.01.186
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
A 2D PEMFC model has been built to simulate the current density distribution and liquid water distribution in cathode. In this simulation, the air mass flow rate, relative humidity of the air and cell voltage are considered as the input parameters into the model, the diagram of current density and liquid water distribution in cathode are shown according to the simulation result and compared to each other. The result indicates that the liquid water distribution has a strong positive relation to the current density, where water drops diffuse mainly by the pressure difference (capillary force) in the porous media (the porous media coefficient 8p is very low), where the shear force of the air can hardly drive the water drops due to the high friction force of the porous media. In the thin porous media (the porous media coefficient 8p is relatively high), the purge effect of the air flow can be enhanced, decreasing the flooding areas in the cathode. Due to the purge effect of the air flow, the outlet of the cathode is the critical areas, where the flooding is most likely to happen. The steep trough at the current density distribution may mean the local flooding, which blocks the oxygen and weaken the chemical reaction. (C) 2019 The Authors. Published by Elsevier Ltd.
引用
收藏
页码:2256 / 2265
页数:10
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