Effects of the electrical resistances of the GDL in a PEM fuel cell

被引:90
作者
Zhou, Tianhong [1 ]
Liu, Hongtan [1 ]
机构
[1] Univ Miami, Dept Mech Engn, Coral Gables, FL 33124 USA
关键词
fuel cell; model; GDL electrical resistance;
D O I
10.1016/j.jpowsour.2006.04.106
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
In most PEM fuel cell models, the electrical resistance of the gas diffusion layers (GDL) is neglected under the assumptions that the GDL electrical conductivity is orders of magnitude higher than the ionic conductivity of the membrane. Recently some modeling efforts have taken the effects of electrical resistance of the GDL into consideration [H. Meng, C.Y. Wang, Electron transport in PEFCs, J. Electrochem. Soc. 151 (2004) A358-A367; BR. Sivertsen, N. Djilali, CFD-based modeling of proton exchange membrane fuel cells, J. Power Sources 141 (2005) 65-78] and some of the results showed that under certain conditions, this effect was significant enough to alter the characteristics of current density distributions under the gas channels and the land areas. If these results are applicable to real-life fuel cells, the present design criteria and optimization procedures must be significantly changed to incorporate the effect of GDL electrical resistance. To examine this issue closely, a three-dimensional fuel cell model incorporating electron transport in the GDL is developed and employed to investigate the effect of electrical resistance through the GDL. In this model, the anisotropic nature of the GDL is taken into consideration by using different electrical conductivities in the through-plane and in-plane directions. The modeling results show that when realistic electrical conductivities for the GDL are used, the effect of the electrical resistance of GDL is slight and can be neglected for all industrial applications. It is believed that the over-estimations of the GDL resistance were mainly caused by neglecting the anisotropic nature of the GDL and/or lumping the contact resistance indiscriminately into the GDL, thus overestimating the electrical resistance of the GDL in the in-plane direction. Besides taking into consideration of the electrical resistance of GDL, the present model also take into consideration of the electron transport in the catalyst layers. When realistic values of electrical conductivities are used for both the GDL and catalyst layers, there is no significant change in the characteristics of current density distribution across the land and channel. (c) 2006 Elsevier B.V. All rights reserved.
引用
收藏
页码:444 / 453
页数:10
相关论文
共 13 条
[1]  
Barbir F, 2005, SUSTAIN WORLD SER, P1
[2]   Temperature and pressure dependence of O2 reduction at Pt | Nafion® 117 and Pt | BAM® 407 interfaces [J].
Beattie, PD ;
Basura, VI ;
Holdcroft, S .
JOURNAL OF ELECTROANALYTICAL CHEMISTRY, 1999, 468 (02) :180-192
[3]   A MATHEMATICAL-MODEL OF THE SOLID-POLYMER-ELECTROLYTE FUEL-CELL [J].
BERNARDI, DM ;
VERBRUGGE, MW .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 1992, 139 (09) :2477-2491
[4]  
DAGAN D, 1989, FLOW TRANSPORT POROU
[5]   Two-dimensional model for proton exchange membrane fuel cells [J].
Gurau, V ;
Liu, HT ;
Kakac, S .
AICHE JOURNAL, 1998, 44 (11) :2410-2422
[6]   Fuel cell performance augmentation: Mass transfer enhancement [J].
Liu, HT ;
Zhou, TH .
JOURNAL OF ENHANCED HEAT TRANSFER, 2003, 10 (03) :257-274
[7]   Electron transport in PEFCs [J].
Meng, H ;
Wang, CY .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 2004, 151 (03) :A358-A367
[8]   Electrical conductivity of conductive carbon blacks: influence of surface chemistry and topology [J].
Pantea, D ;
Darmstadt, H ;
Kaliaguine, S ;
Roy, C .
APPLIED SURFACE SCIENCE, 2003, 217 (1-4) :181-193
[9]   CFD-based modelling of proton exchange membrane fuel cells [J].
Sivertsen, BR ;
Djilali, N .
JOURNAL OF POWER SOURCES, 2005, 141 (01) :65-78
[10]   POLYMER ELECTROLYTE FUEL-CELL MODEL [J].
SPRINGER, TE ;
ZAWODZINSKI, TA ;
GOTTESFELD, S .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 1991, 138 (08) :2334-2342