Effect of porosity gradient in cathode gas diffusion layer of polymer electrolyte membrane fuel cells on the liquid water transport using lattice Boltzmann method

被引:14
作者
Habiballahi, Mohammad [1 ]
Hassanzadeh, Hasan [1 ]
Rahnama, Mohammad [2 ]
Mirbozorgi, Seyed Ali [1 ]
Javaran, Ebrahim Jahanshahi [3 ]
机构
[1] Univ Birjand, Dept Mech Engn, Birjand 9717494133, Iran
[2] Shahid Bahonar Univ Kerman, Dept Mech Engn, Kerman, Iran
[3] Grad Univ Adv Technol, Dept Energy, Kerman, Iran
关键词
Polymer electrolyte membrane fuel cell; lattice Boltzmann method; two phase flow; liquid water transfer; gas diffusion layer; porosity gradient; MICROPOROUS LAYER; FLOW SIMULATION; 2-PHASE FLOW; MODEL; PERFORMANCE; MULTIPHASE; PERMEABILITY; CHANNEL;
D O I
10.1177/0957650920934312
中图分类号
O414.1 [热力学];
学科分类号
摘要
In this paper, a two-dimensional model has been developed to simulate the liquid water transport in a cathode gas diffusion layer with different porosity gradients in polymer electrolyte membrane fuel cells (PEMFCs). Due to the complexity of porous media, the simulation was carried out by lattice Boltzmann method. According to dimensionless numbers that characterize liquid water transport in porous media, simulation conditions were similar to the liquid water transfer into the gas diffusion layer of PEMFC. Different gas diffusion layers were created randomly by solid circular particles with an average diameter of5 mu m,and the numerical code was validated by conducting several tests. The results indicated that capillary force is the main factor in liquid water transport in the gas diffusion layer, while viscous and gravitational forces do not have a significant effect. In addition to improve the water management, the gas diffusion layer should have a positive porosity gradient, i.e. the porosity increases along the thickness. Also, under the same boundary conditions and at the average porosity (0.659), the saturation distribution curves in three porous media were compared including the gas diffusion layer with porosity gradient, the gas diffusion layer with the micro-porous layer, and the gas diffusion layer with uniform porosity. The average liquid water saturation in the gas diffusion layer with the 10% porosity gradient was 20.2% lower than in the gas diffusion layer with uniform porosity and 10.5% lower than the gas diffusion layer + micro-porous layer. Furthermore, upon elevation of the porosity gradient in the gas diffusion layer, the average liquid water saturation in the gas diffusion layer decreased. Specifically, as the porosity gradient rose from 10% to 14% and 18.5%, the average liquid water saturation values decreased to 29.8% and 38.8%, respectively compared with the gas diffusion layer with uniform porosity.
引用
收藏
页码:546 / 562
页数:17
相关论文
共 48 条
  • [1] Numerical analysis of a proton exchange membrane fuel cell. Part 2: parametric study
    Al-Baghdadi, M. A. R. Sadiq
    Al-Janabi, H. A. K. Shahad
    [J]. PROCEEDINGS OF THE INSTITUTION OF MECHANICAL ENGINEERS PART A-JOURNAL OF POWER AND ENERGY, 2007, 221 (A7) : 931 - 939
  • [3] Two phase flow simulation in a channel of a polymer electrolyte membrane fuel cell using the lattice Boltzmann method
    Ben Salah, Yasser
    Tabe, Yutaka
    Chikahisa, Takemi
    [J]. JOURNAL OF POWER SOURCES, 2012, 199 : 85 - 93
  • [4] A 3D, multiphase, multicomponent model of the cathode and anode of a PEM fuel cell
    Berning, T
    Djilali, N
    [J]. JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 2003, 150 (12) : A1589 - A1598
  • [5] Two-phase transport in the cathode gas diffusion layer of PEM fuel cell with a gradient in porosity
    Chen, Falin
    Chang, Min-Hsing
    Hsieh, Ping-Tso
    [J]. INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2008, 33 (10) : 2525 - 2529
  • [6] Chen L, 2010, FRONT HEAT MASS TRAN, P1
  • [7] A critical review of the pseudopotential multiphase lattice Boltzmann model: Methods and applications
    Chen, Li
    Kang, Qinjun
    Mu, Yutong
    He, Ya-Ling
    Tao, Wen-Quan
    [J]. INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2014, 76 : 210 - 236
  • [8] Multi-scale modeling of proton exchange membrane fuel cell by coupling finite volume method and lattice Boltzmann method
    Chen, Li
    Feng, Yong-Liang
    Song, Chen-Xi
    Chen, Lei
    He, Ya-Ling
    Tao, Wen-Quan
    [J]. INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2013, 63 : 268 - 283
  • [9] Numerical investigation of liquid water transport and distribution in porous gas diffusion layer of a proton exchange membrane fuel cell using lattice Boltzmann method
    Chen, Li
    Luan, Hui-Bao
    He, Ya-Ling
    Tao, Wen-Quan
    [J]. RUSSIAN JOURNAL OF ELECTROCHEMISTRY, 2012, 48 (07) : 712 - 726
  • [10] Experimental characterization of in-plane permeability of gas diffusion layers
    Feser, J. P.
    Prasad, A. K.
    Advani, S. G.
    [J]. JOURNAL OF POWER SOURCES, 2006, 162 (02) : 1226 - 1231