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 50 条
  • [41] Effective transport properties for polymer electrolyte membrane fuel cells - With a focus on the gas diffusion layer
    Zamel, Nada
    Li, Xianguo
    PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2013, 39 (01) : 111 - 146
  • [42] Performance of Pd Cathode Catalyst Electrodeposited on Gas Diffusion Layer in Polymer Electrolyte Membrane Fuel Cells
    Sujin Gok
    Youngkwang Kim
    Taeho Lim
    Hyun-Jong Kim
    Oh Joong Kwon
    Electrocatalysis, 2018, 9 : 59 - 66
  • [43] Performance of Pd Cathode Catalyst Electrodeposited on Gas Diffusion Layer in Polymer Electrolyte Membrane Fuel Cells
    Gok, Sujin
    Kim, Youngkwang
    Lim, Taeho
    Kim, Hyun-Jong
    Kwon, Oh Joong
    ELECTROCATALYSIS, 2018, 9 (01) : 59 - 66
  • [44] Phase separation modeling of water transport in polymer electrolyte membrane fuel cells using the Multiple-Relaxation-Time lattice Boltzmann method
    Park, Sungjea
    Kim, Myong-Hwan
    Um, Sukkee
    CHEMICAL ENGINEERING JOURNAL, 2024, 495
  • [45] Influence of local carbon fibre orientation on the water transport in the gas diffusion layer of polymer electrolyte membrane fuel cells
    Markoetter, Henning
    Dittrnann, Katja
    Haussmann, Jan
    Alink, Robert
    Gerteisen, Dietmar
    Riesemeier, Heinrich
    Scholta, Joachim
    Banhart, John
    Manke, Ingo
    ELECTROCHEMISTRY COMMUNICATIONS, 2015, 51 : 133 - 136
  • [46] Effect of diffusion-layer porosity on the performance of polymer electrolyte fuel cells
    G. Selvarani
    A. K. Sahu
    P. Sridhar
    S. Pitchumani
    A. K. Shukla
    Journal of Applied Electrochemistry, 2008, 38 : 357 - 362
  • [47] Effect of diffusion-layer porosity on the performance of polymer electrolyte fuel cells
    Selvarani, G.
    Sahu, A. K.
    Sridhar, P.
    Pitchumani, S.
    Shukla, A. K.
    JOURNAL OF APPLIED ELECTROCHEMISTRY, 2008, 38 (03) : 357 - 362
  • [48] Effect of porosity heterogeneity on the permeability and tortuosity of gas diffusion layers in polymer electrolyte membrane fuel cells
    Nabovati, Aydin
    Hinebaugh, James
    Bazylak, Aimy
    Amon, Cristina H.
    JOURNAL OF POWER SOURCES, 2014, 248 : 83 - 90
  • [49] Effects of cathode gas diffusion layer design on polymer electrolyte membrane fuel cell water management and performance
    Yau, Tak Cheung
    Cimenti, Massimiliano
    Bi, Xiaotao
    Stumper, Juergen
    JOURNAL OF POWER SOURCES, 2011, 196 (22) : 9437 - 9444
  • [50] Liquid water transport in a mixed-wet gas diffusion layer of a polymer electrolyte fuel cell
    Sinha, Puneet K.
    Wang, Chao-Yang
    CHEMICAL ENGINEERING SCIENCE, 2008, 63 (04) : 1081 - 1091