Through-Plane Water Distribution in a Polymer Electrolyte Fuel Cell: Comparison of Numerical Prediction with Neutron Radiography Data

被引:53
作者
Wang, Yun [1 ,2 ]
Chen, Ken S. [3 ]
机构
[1] Univ Calif Irvine, Renewable Energy Resources Lab, Irvine, CA 92697 USA
[2] Univ Calif Irvine, Natl Fuel Cell Res Ctr, Dept Mech & Aerosp Engn, Irvine, CA 92697 USA
[3] Sandia Natl Labs, Engn Sci Ctr, Albuquerque, NM 87185 USA
基金
美国能源部;
关键词
GAS-DIFFUSION LAYER; LIQUID WATER; 2-PHASE FLOW; EXPERIMENTAL VALIDATION; CAPILLARY-PRESSURE; MATHEMATICAL-MODEL; TRANSPORT; MEMBRANE; CATHODE; MANAGEMENT;
D O I
10.1149/1.3498997
中图分类号
O646 [电化学、电解、磁化学];
学科分类号
081704 ;
摘要
A multidimensional mathematical model is presented for simulating the coupled phenomena of gaseous fuel/reactant flows, species (including liquid water) transport, heat transfer, hydrogen oxidation, and oxygen reduction reactions in a polymer electrolyte fuel cell (PEFC). The present work focuses on elucidating water distribution in the through-plane direction, in particular across the membrane electrode assembly (MEA) and gas diffusion layer (GDL). Two-dimensional model predictions are computed numerically and compared with available experimental data from neutron radiography or imaging. Using the same set of model parameters, reasonably good agreements are obtained quantitatively between the computed water profile in the MEA-GDL component and the neutron-imaging data reported by two separate research groups, and qualitatively between model prediction and the data from another (third) group. Case-study simulations are carried out for PEFC operation at various temperatures, relative humidities, and current densities. It is found that liquid-water content is lower at higher cell temperatures due to greater water evaporation and stronger water diffusion in the vapor phase, as expected. Without strong water diffusion in the vapor phase, the liquid-water profiles are found to increase with current density in the cathode GDL but indicate a complex trend in the anode. Effect of varying GDL thermal conductivity on water distribution is also examined. (C) 2010 The Electrochemical Society. [DOI: 10.1149/1.3498997] All rights reserved.
引用
收藏
页码:B1878 / B1886
页数:9
相关论文
共 58 条
[21]  
Moon B.S, 2001, KOREAN J COMPUT APPL, V8, P507
[22]   Diffusion of water in Nafion 115 membranes [J].
Motupally, S ;
Becker, AJ ;
Weidner, JW .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 2000, 147 (09) :3171-3177
[23]   Direct numerical simulation modeling of bilayer cathode catalyst layers in polymer electrolyte fuel cells [J].
Mukherjee, Partha P. ;
Wang, Chao-Yang .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 2007, 154 (11) :B1121-B1131
[24]   Mesoscopic modeling of two-phase behavior and flooding phenomena in polymer electrolyte fuel cells [J].
Mukherjee, Partha P. ;
Wang, Chao-Yang ;
Kang, Qinjun .
ELECTROCHIMICA ACTA, 2009, 54 (27) :6861-6875
[25]   Visualising Liquid Water in PEM Fuel Cells Using Neutron Imaging [J].
Mukundan, R. ;
Borup, R. L. .
FUEL CELLS, 2009, 9 (05) :499-505
[26]   Effective diffusivity and water-saturation distribution in single- and two-layer PEMFC diffusion medium [J].
Nam, JH ;
Kaviany, M .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2003, 46 (24) :4595-4611
[27]   A two-dimensional, two-phase, multicomponent, transient model for the cathode of a proton exchange membrane fuel cell using conventional gas distributors [J].
Natarajan, D ;
Nguyen, TV .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 2001, 148 (12) :A1324-A1335
[28]   A WATER AND HEAT MANAGEMENT MODEL FOR PROTON-EXCHANGE-MEMBRANE FUEL-CELLS [J].
NGUYEN, TV ;
WHITE, RE .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 1993, 140 (08) :2178-2186
[29]   Effects of flow field and diffusion layer properties on water accumulation in a PEM fuel cell [J].
Owejan, J. P. ;
Trabold, T. A. ;
Jacobson, D. L. ;
Arif, M. ;
Kandlikar, S. G. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2007, 32 (17) :4489-4502
[30]   In situ investigation of water transport in an operating PEM fuel cell using neutron radiography: Part 2 - Transient water accumulation in an interdigitated cathode flow field [J].
Owejan, J. P. ;
Trabold, T. A. ;
Jacobson, D. L. ;
Baker, D. R. ;
Hussey, D. S. ;
Arif, M. .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2006, 49 (25-26) :4721-4731