Hydrogen crossover in high-temperature PEM fuel cells

被引:135
作者
Cheng, Xuan [1 ]
Zhang, Jianlu [1 ]
Tang, Yanghua [1 ]
Song, Chaojie [1 ]
Shen, Jun [1 ]
Song, Datong [1 ]
Zhang, Jiujun [1 ]
机构
[1] Natl Res Council Canada, Inst Fuel Cell Innovat, Vancouver, BC V6T 1W5, Canada
基金
中国国家自然科学基金;
关键词
proton exchange membrane (PEM) fuel cells; hydrogen crossover; permeability coefficient; temperature; backpressure; relative humidity;
D O I
10.1016/j.jpowsour.2007.02.027
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 this paper, hydrogen crossover was measured in an environment of high-temperature proton exchange membrane (PEM) fuel cells using a steady-state electrochemical method at various temperatures (T) (80-120 degrees C), backpressures (P) (1.0-3.0atm), and relative humidities (RH) (25-100%). An H-2 crossover model based on an MEA consisting of five layers - anode gas diffusion layer, anode catalyst layer, proton exchange membrane (Nation 112 or Nation 117), cathode catalyst layer, and cathode gas diffusion layer - was constructed to obtain an expression for H-2 permeability coefficients as a function of measured H-2 crossover rates and controlled H-2 partial pressures. The model analysis suggests that the dominant factor in the overall H-2 crossover is the step of H-2 diffusing through the PEM. The H-2 permeability coefficients as a function of T, P, and RH obtained in this study show that the increases in both T and P could increase the H-2 permeability coefficient at any given RH. However, the effect of RH on the permeability coefficient seems to be more complicated. The T effect is much larger than that of P and RH. Through experimental data simulation an equation was obtained to describe the T dependencies of the H-2 permeability coefficient, based on which other parameters such as maximum permeability coefficients and activation energies for H-2 crossover through both Nation 112 and 117 membranes were also evaluated. Both Nation 112 and Nation 117 showed similar values of such parameters, suggesting that membrane thickness does not play a significant role in the H, crossover mechanism. (C) 2007 Elsevier B.V. All rights reserved.
引用
收藏
页码:25 / 31
页数:7
相关论文
共 29 条
[1]   Oxygen and hydrogen permeation properties and water uptake of Nafion(R) 117 membrane and recast film for PEM fuel cell [J].
Broka, K ;
Ekdunge, P .
JOURNAL OF APPLIED ELECTROCHEMISTRY, 1997, 27 (02) :117-123
[2]   Degradation of polymer electrolyte membranes [J].
Collier, Amanda ;
Wang, Haijiang ;
Yuan, Xiao Zi ;
Zhang, Jiujun ;
Wilkinson, David P. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2006, 31 (13) :1838-1854
[3]  
ERANISHI K, 2006, ELECTROCHEM SOLID ST, V9, pA475
[4]  
GIERKE TD, 1982, ACS SYM SER, V180, P283
[5]   Gas crossover and membrane degradation in polymer electrolyte fuel cells [J].
Inaba, Minoru ;
Kinumoto, Taro ;
Kiriake, Masayuki ;
Umebayashi, Ryota ;
Tasaka, Akimasa ;
Ogumi, Zempachi .
ELECTROCHIMICA ACTA, 2006, 51 (26) :5746-5753
[6]   Investigation of membrane property and fuel cell behavior with sulfonated poly(ether ether ketone) electrolyte: Temperature and relative humidity effects [J].
Jiang, RC ;
Kunz, HR ;
Fenton, JM .
JOURNAL OF POWER SOURCES, 2005, 150 :120-128
[7]  
KOCH S, 2002, PREPRINT ARCHIVE
[8]   Characterization of gas crossover and its implications in PEM fuel cells [J].
Kocha, SS ;
Yang, JDL ;
Yi, JS .
AICHE JOURNAL, 2006, 52 (05) :1916-1925
[9]   GAS PERMEATION IN SPE METHOD .1. OXYGEN PERMEATION THROUGH NAFION AND NEOSEPTA [J].
OGUMI, Z ;
TAKEHARA, Z ;
YOSHIZAWA, S .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 1984, 131 (04) :769-773
[10]   GAS PERMEATION IN SPE METHOD .2. OXYGEN AND HYDROGEN PERMEATION THROUGH NAFION [J].
OGUMI, Z ;
KUROE, T ;
TAKEHARA, Z .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 1985, 132 (11) :2601-2605