Influences of gas relative humidity on the temperature of membrane in PEMFC with interdigitated flow field

被引:49
作者
Jian, Qi-fei [1 ]
Ma, Guang-qing [1 ]
Qiu, Xiao-liang [1 ]
机构
[1] S China Univ Technol, Sch Mech & Automobile Engn, Guangzhou 510640, Guangdong, Peoples R China
关键词
Interdigitated; PEM; Fuel cell; CFD modeling; Humidification; Temperature difference; FUEL-CELLS; WATER; MODEL; PERFORMANCE; DESIGNS;
D O I
10.1016/j.renene.2013.06.046
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A fundamental understanding of the water balance of a fuel cell during operation is crucial for improving the cell performance and durability. The humidification in the anode or cathode has an important effect on the flow characteristics and cell efficiency. Three-dimensional steady mathematical model based on the electrochemical, current distribution, fluid motion continuity equation, momentum and energy equation, boundary layer theory has been developed to simulate PEMFC with interdigitated flow field using the computational fluid dynamics (CFD). Effects on the current density and temperature differences have been simulated and analyzed respectively, when the humidification in the anode or cathode is from 0% to 100% respectively. The numerical results show that the humidification strongly influences the current density and temperature difference so as to affect the cell efficiency. Under the same operation conditions and low humidification conditions, anode humidification can better enhance the performance of the battery and improve the extent of PEM humidification. (C) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码:129 / 136
页数:8
相关论文
共 19 条
[1]   Three-dimensional computational fluid dynamics model of a tubular-shaped PEM fuel cell [J].
Al-Baghdadi, Maher A. R. Sadiq .
RENEWABLE ENERGY, 2008, 33 (06) :1334-1345
[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]   Investigating the effects of operational factors on PEMFC performance based on CFD simulations using a three-level full-factorial design [J].
Cheng, Shan-Jen ;
Miao, Jr-Ming ;
Wu, Sheng-Ju .
RENEWABLE ENERGY, 2012, 39 (01) :250-260
[4]   A three-dimensional full-cell CFD model used to investigate the effects of different flow channel designs on PEMFC performance [J].
Ferng, Yuh Ming ;
Su, Ay .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2007, 32 (17) :4466-4476
[5]   A droplet size dependent multiphase mixture model for two phase flow in PEMFCs [J].
He, Guangli ;
Yamazaki, Yohtaro ;
Abudula, Abuliti .
JOURNAL OF POWER SOURCES, 2009, 194 (01) :190-198
[6]   Three-dimensional numerical analysis of proton exchange membrane fuel cells (PEMFCs) with conventional and interdigitated flow fields [J].
Hu, GL ;
Fan, JR ;
Chen, S ;
Liu, YJ ;
Cen, KF .
JOURNAL OF POWER SOURCES, 2004, 136 (01) :1-9
[7]   The effect of serpentine flow-field designs on PEM fuel cell performance [J].
Jeon, D. H. ;
Greenway, S. ;
Shimpalee, S. ;
Van Zee, J. W. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2008, 33 (03) :1052-1066
[8]   Water transport in polymer electrolyte membrane fuel cells [J].
Jiao, Kui ;
Li, Xianguo .
PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2011, 37 (03) :221-291
[9]   Cross-leakage flow between adjacent flow channels in PEM fuel cells [J].
Kanezaki, Toshihiko ;
Li, Xianguo ;
Baschuk, J. J. .
JOURNAL OF POWER SOURCES, 2006, 162 (01) :415-425
[10]   A generalized numerical model for liquid water in a proton exchange membrane fuel cell with interdigitated design [J].
Le, Anh Dinh ;
Zhou, Biao .
JOURNAL OF POWER SOURCES, 2009, 193 (02) :665-683