PEM fuel cells modeling and analysis through current and voltage transient behaviors

被引:81
作者
Adzakpa, K. P. [1 ]
Agbossou, K. [1 ,2 ]
Dube, Y. [3 ]
Dostie, M. [4 ]
Fournier, M. [4 ]
Poulin, A. [4 ]
机构
[1] Univ Quebec, Hydrogen Res Inst, Trois Rivieres, PQ G9A 5H7, Canada
[2] Univ Quebec, Dept Elect & Comp Engn, Trois Rivieres, PQ G9A 5H7, Canada
[3] Univ Quebec, Dept Engn Mech, Trois Rivieres, PQ G9A 5H7, Canada
[4] LTE Hydro Quebec, Quebec City, PQ G9N 7N5, Canada
关键词
capacitance; diffusion; double layer; overshoot/undershoot; polymer electrolyte membrane (PEM) fuel cells; transient voltage;
D O I
10.1109/TEC.2007.914170
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
In the last 15 years, polymer electrolyte membrane (PEM) fuel cells have received much attention, mostly through experimental and empirical studies in scientific and industrial research. In most of the works, attention has been given to the steady state analysis of the PEM fuel cells. However, considerable efforts still need to be done to explain different transient behaviors of PEM fuel cells. This paper presents an analysis of the double layer charging effect and reactant diffusion through the cathode gas diffusion layer on voltage transients after sudden current variations. These transient phenomena have typical time durations of less than 5 s. The double layer charging dynamic explains the main voltage transient behaviors when the cathode inlet pressure is constant. In this case, a bicriteria optimization procedure is proposed for numerical characterization of the double-layer charging capacitance. When the air pressure is variable, a pseudo 2-D modeling of oxygen diffusion through the cathode gas diffusion layers, based on the Stephan - Maxwell multicomponent diffusion equations, is used to explain its contribution to the voltage transient overshoots/undershoots.
引用
收藏
页码:581 / 591
页数:11
相关论文
共 23 条
[1]   Performance of a stand-alone renewable energy system based on energy storage as hydrogen [J].
Agbossou, K ;
Kolhe, M ;
Hamelin, J ;
Bose, TK .
IEEE TRANSACTIONS ON ENERGY CONVERSION, 2004, 19 (03) :633-640
[2]  
AMPHLETT JC, 1995, J ELECTROCHEM SOC, V142, P1, DOI 10.1149/1.2043866
[3]   Dynamic interaction of a proton exchange membrane fuel cell and a lead-acid battery [J].
Amphlett, JC ;
deOliveira, EH ;
Mann, RF ;
Roberge, PR ;
Rodrigues, A ;
Salvador, JP .
JOURNAL OF POWER SOURCES, 1997, 65 (1-2) :173-178
[4]   MATHEMATICAL-MODEL OF A GAS-DIFFUSION ELECTRODE BONDED TO A POLYMER ELECTROLYTE [J].
BERNARDI, DM ;
VERBRUGGE, MW .
AICHE JOURNAL, 1991, 37 (08) :1151-1163
[5]   Modelling static and dynamic behaviour of proton exchange membrane fuel cells on the basis of electro-chemical description [J].
Ceraolo, M ;
Miulli, C ;
Pozio, A .
JOURNAL OF POWER SOURCES, 2003, 113 (01) :131-144
[6]   Transient behavior of water transport in the membrane of a PEM fuel cell [J].
Chen, FL ;
Su, YG ;
Soong, CY ;
Yan, WM ;
Chu, HS .
JOURNAL OF ELECTROANALYTICAL CHEMISTRY, 2004, 566 (01) :85-93
[7]   Sensitivity analysis of the modeling parameters used in simulation of proton exchange membrane fuel cells [J].
Corrêa, JM ;
Farret, FA ;
Popov, VA ;
Simoes, MG .
IEEE TRANSACTIONS ON ENERGY CONVERSION, 2005, 20 (01) :211-218
[8]  
EATON BM, 2001, THESIS STATE U BLACK
[9]  
FOURNIER M, 2006, WHEC, V16, P13
[10]   Dynamic behavior of a PEM fuel cell stack for stationary applications [J].
Hamelin, J ;
Agbossou, K ;
Laperrière, A ;
Laurencelle, F ;
Bose, TK .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2001, 26 (06) :625-629