Modeling and simulation of PEM fuel cells with CO poisoning

被引:20
作者
Baschuk, JJ
Rowe, AM
Li, XG [1 ]
机构
[1] Univ Waterloo, Dept Mech Engn, Waterloo, ON N2L 3G1, Canada
[2] Univ Victoria, Dept Mech Engn, Victoria, BC V8W 3P6, Canada
来源
JOURNAL OF ENERGY RESOURCES TECHNOLOGY-TRANSACTIONS OF THE ASME | 2003年 / 125卷 / 02期
关键词
D O I
10.1115/1.1538186
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
A polymer electrolyte membrane (PEM) fuel cell is analyzed by applying the conservation principle to the electrode backing, catalyst layers and polymer electrolyte. The conservation equations used are the conservation of species, momentum and energy, with the Nernst-Planck equation used for the electrolyte. Oxygen reduction at the cathode is modeled using the Butler-Volmer equation while the adsorption, desorption and electrooxidation of hydrogen and CO at the anode are modeled by the Tafel-Volmer and "reactant-pair "mechanism, respectively. Temperature variations within the cell are minimized by decreasing current density or increasing temperature. An increase in pressure increases the cell voltage at low current density, but decreases the cell voltage at high current density. The electrochemical kinetics model used for the adsorption, desorption and electro-oxidation of hydrogen and CO is validated with published, experimental data.
引用
收藏
页码:94 / 100
页数:7
相关论文
共 28 条
[1]   Thermodynamics of insulated pressure vessels for vehicular hydrogen storage [J].
Aceves, SM ;
Berry, GD .
JOURNAL OF ENERGY RESOURCES TECHNOLOGY-TRANSACTIONS OF THE ASME, 1998, 120 (02) :137-142
[2]   PERFORMANCE MODELING OF THE BALLARD-MARK-IV SOLD POLYMER ELECTROLYTE FUEL-CELL .2. EMPIRICAL-MODEL DEVELOPMENT [J].
AMPHLETT, JC ;
BAUMERT, RM ;
MANN, RF ;
PEPPLEY, BA ;
ROBERGE, PR ;
HARRIS, TJ .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 1995, 142 (01) :9-15
[3]  
BASCHUK J, 2001, THESIS U WATERLOO WA
[4]   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
[5]   Analysis of reaction kinetics for carbon monoxide and carbon dioxide on polycrystalline platinum relative to fuel cell operation [J].
Bellows, RJ ;
MarucchiSoos, EP ;
Buckley, DT .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1996, 35 (04) :1235-1242
[6]   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
[7]   NATURE OF CO ADSORPTION DURING H-2 OXIDATION IN RELATION TO MODELING FOR CO POISONING OF A FUEL-CELL ANODE [J].
DHAR, HP ;
CHRISTNER, LG ;
KUSH, AK .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 1987, 134 (12) :3021-3026
[8]   Components for PEM fuel cell systems using hydrogen and CO containing fuels [J].
Divisek, J ;
Oetjen, HF ;
Peinecke, V ;
Schmidt, VM ;
Stimming, U .
ELECTROCHIMICA ACTA, 1998, 43 (24) :3811-3815
[9]   WATER AND THERMAL MANAGEMENT IN SOLID-POLYMER-ELECTROLYTE FUEL-CELLS [J].
FULLER, TF ;
NEWMAN, J .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 1993, 140 (05) :1218-1225
[10]  
Gileadi E., 1975, Interfacial Electrochemistry