Modeling the Effects of the Microporous Layer on the Net Water Transport Rate Across the Membrane in a PEM Fuel Cell

被引:38
作者
Wang, Xuhai [1 ]
Nguyen, Trung Van [1 ]
机构
[1] Univ Kansas, Dept Chem & Petr Engn, Lawrence, KS 66045 USA
基金
美国国家科学基金会;
关键词
catalysts; diffusion; electrochemical electrodes; hydrophobicity; liquid theory; porous materials; proton exchange membrane fuel cells; water; MICRO-POROUS LAYER; GAS-DIFFUSION LAYER; VALIDATED LEVERETT APPROACH; COMPOSITE CARBON-BLACK; CAPILLARY-PRESSURE; MULTIPHASE FLOW; MATHEMATICAL-MODEL; 2-PHASE TRANSPORT; PTFE CONTENT; PERFORMANCE;
D O I
10.1149/1.3292287
中图分类号
O646 [电化学、电解、磁化学];
学科分类号
081704 ;
摘要
In this study, a model was developed to evaluate the effects of the microporous layer (MPL) on the net liquid water transport rate across the membrane. The results support the hypothesis that the improvement in fuel cell performance observed when an MPL is used in the cathode side is related to its effect on the water transport process in the electrode and membrane. Due to its high hydrophobicity, the MPL increases the liquid water pressure in the cathode to levels much higher than that in the anode, resulting in an increased back-transport rate of liquid water from the cathode to the anode. This reduces the amount of water that is transported out of the cathode through the gas diffusion layer (GDL) to the cathode flow channels resulting in a lower saturation level in the GDL, and consequently, faster oxygen transport to the catalyst sites. This model showed that the state of zero-net-water-transport-across-the-membrane could be achieved with the appropriate capillary properties of the porous media. Two capillary properties of the MPL identified to have the greatest impact on the proton-exchange-membrane (PEM) fuel cell performance are the liquid water saturation level at p(c)=0 (p(g)=p(l)) and the slope of the capillary curve in the hydrophobic region.
引用
收藏
页码:B496 / B505
页数:10
相关论文
共 41 条
[11]   Capillary pressure and hydrophilic porosity in gas diffusion layers for polymer electrolyte fuel cells [J].
Gostick, Jeffrey T. ;
Fowler, Michael W. ;
Ioannidis, Marios A. ;
Pritzker, Mark D. ;
Volfkovich, Y. M. ;
Sakars, A. .
JOURNAL OF POWER SOURCES, 2006, 156 (02) :375-387
[12]   The use of a novel water porosimeter to predict the water handling behaviour of gas diffusion media used in polymer electrolyte fuel cells [J].
Harkness, I. R. ;
Hussain, N. ;
Smith, L. ;
Sharman, J. D. B. .
JOURNAL OF POWER SOURCES, 2009, 193 (01) :122-129
[13]  
Hizir F.E., 2009, P ASME 2009 7 INT FU
[14]   The influence of the gas diffusion layer on water management in polymer electrolyte fuel cells [J].
Holmstrom, N. ;
Ihonen, J. ;
Lundblad, A. ;
Lindbergh, G. .
FUEL CELLS, 2007, 7 (04) :306-313
[15]   An experimental investigation of water transport in PEMFCs - The role of microporous layers [J].
Karan, Kunal ;
Atiyeh, Hasan ;
Phoenix, Aaron ;
Halliop, Ela ;
Pharoah, Jon ;
Peppley, Brant .
ELECTROCHEMICAL AND SOLID STATE LETTERS, 2007, 10 (02) :B34-B38
[16]  
Kumbur EC, 2007, J ELECTROCHEM SOC, V154, pB1315, DOI 10.1149/1.2784286
[17]   Validated leverett approach for multiphase flow in PEFC diffusion media [J].
Kumbur, E. C. ;
Sharp, K. V. ;
Mench, M. M. .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 2007, 154 (12) :B1305-B1314
[18]  
Kumbur EC, 2007, J ELECTROCHEM SOC, V154, pB1295, DOI 10.1149/1.2784283
[19]  
LIN G, COMMUNICATION
[20]   Effect of thickness and hydrophobic polymer content of the gas diffusion layer on electrode flooding level in a PEMFC [J].
Lin, GY ;
Nguyen, TV .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 2005, 152 (10) :A1942-A1948