Analysis of PEM (Polymer Electrolyte Membrane) fuel cell cathode two-dimensional modeling

被引:60
作者
Abdollahzadeh, M. [1 ]
Pascoa, J. C. [1 ]
Ranjbar, A. A. [2 ]
Esmaili, Q. [3 ]
机构
[1] Univ Beira Interior, Dept Electromech Engn, C MAST Ctr Mech & Aerosp Sci & Technol, FCT Portuguese Fdn Sci & Technol, Covilha, Portugal
[2] Babol Univ Technol, Dept Mech Engn, Babol Sar, Iran
[3] Islamic Azad Univ, Dept Mech Engn, Ayatollah Amoli Branch, Amol, Iran
关键词
Two phase flow; Multi-component mixture model; Flooding; Interdigitated flow field; GAS-DIFFUSION LAYER; 2-PHASE FLOW; TRANSPORT MODEL; WATER TRANSPORT; MASS-TRANSFER; PERFORMANCE; PARALLEL;
D O I
10.1016/j.energy.2014.01.075
中图分类号
O414.1 [热力学];
学科分类号
摘要
The performance of PEMFC (Polymer Electrolyte Membrane Fuel Cells) with different configuration of gas feeding channels is investigated. Multi-component mixture model is used in order to simulate the two phase flow and transport in cathode gas diffusion layer of PEM fuel cell. This model reduces the numerical simulation complexity by reducing the number of nonlinear governing equations. A wide detailed parametric study is done to investigate different operational parameter such as; pressure difference, operating temperature, different geometrical parameters such as; gas diffusion layer thickness, and various material parameters such as porosity and wettability. Computational simulations have been conducted and the simulation results were compared with the available results in literature and showed very little difference. Results have been presented with different polarization curves, power density and local current density curves and also the plots of saturation level at catalyst layer surface. Furthermore the changes in the place of the interface between single and two phase zones is presented for further understating of the effects of different parameters. This parametric study confirms qualitatively to the validity of the considered model for systematic simulation of the PEM fuel cells. (c) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:478 / 494
页数:17
相关论文
共 35 条
[1]   (1D+1D) approach mathematical modeling of two phase multicomponent transport flow in PEMFC [J].
Abdollahzadeh, M. ;
Ranjbar, A. A. ;
Esmaili, Q. .
RUSSIAN JOURNAL OF ELECTROCHEMISTRY, 2012, 48 (12) :1187-1196
[2]   A critical review of two-phase flow in gas flow channels of proton exchange membrane fuel cells [J].
Anderson, Ryan ;
Zhang, Lifeng ;
Ding, Yulong ;
Blanco, Mauricio ;
Bi, Xiaotao ;
Wilkinson, David P. .
JOURNAL OF POWER SOURCES, 2010, 195 (15) :4531-4553
[3]  
Anil W., 2005, INTRO COMPUTATIONAL
[4]   A two-dimensional, transient, compressible isothermal and two-phase model for the air-side electrode of PEM fuel cells [J].
Baboh, M. Khakbaz ;
Kermani, M. J. .
ELECTROCHIMICA ACTA, 2008, 53 (26) :7644-7654
[5]   TWO-PHASE FLOW AND MASS TRANSFER WITHIN THE DIFFUSION LAYER OF A POLYMER ELECTROLYTE MEMBRANE FUEL CELL [J].
Beale, S. B. ;
Schwarz, D. H. ;
Malin, M. R. ;
Spalding, D. B. .
COMPUTATIONAL THERMAL SCIENCES, 2009, 1 (02) :105-120
[6]   Three-dimensional computational analysis of transport phenomena in a PEM fuel cell - a parametric study [J].
Berning, T ;
Djilali, N .
JOURNAL OF POWER SOURCES, 2003, 124 (02) :440-452
[7]  
Carton JG, WATER DROPLET ACCUMA
[8]   Two-phase transport in the cathode gas diffusion layer of PEM fuel cell with a gradient in porosity [J].
Chen, Falin ;
Chang, Min-Hsing ;
Hsieh, Ping-Tso .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2008, 33 (10) :2525-2529
[9]   Gas diffusion layer for proton exchange membrane fuel cells-A review [J].
Cindrella, L. ;
Kannan, A. M. ;
Lin, J. F. ;
Saminathan, K. ;
Ho, Y. ;
Lin, C. W. ;
Wertz, J. .
JOURNAL OF POWER SOURCES, 2009, 194 (01) :146-160
[10]   On the influence of temperature on PEM fuel cell operation [J].
Coppo, M. ;
Siegel, N. P. ;
von Spakovsky, M. R. .
JOURNAL OF POWER SOURCES, 2006, 159 (01) :560-569