Pore-scale study of liquid water transport in gas diffusion layers with in-plane non-uniform distributed pore size of polymer electrolyte membrane fuel cell

被引:0
|
作者
Lai, Tao [1 ]
Qu, Zhiguo [1 ]
Zhang, Jianfei [1 ]
机构
[1] Xi An Jiao Tong Univ, Sch Energy & Power Engn, Key Lab Thermo Fluid Sci & Engn MOE, Xian 710049, Shaanxi, Peoples R China
基金
美国国家科学基金会;
关键词
Gas diffusion layer; Liquid water directional flow; Lattice Boltzmann method; In-plane distributed pore size; Effective gas diffusion coefficient; PERFORMANCE; GDL; SIMULATION; PRESSURE; MODEL;
D O I
10.1016/j.apenergy.2024.124933
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
Timely removal of liquid water and the supply of the reaction gas in the gas diffusion layer (GDL) plays a critical role in improving the performance of polymer electrolyte membrane fuel cells (PEMFCs). Modifying the design of the GDL structure is an effective strategy for regulating the percolation process of liquid water and the supply of reaction gas. In this study, several GDLs with in-plane nonuniformly distributed pore sizes were designed to construct an ordered liquid water transport pathway. Two pore-size patterns with a "V" shape and an inverted "V" shape were designed through the orientation control of fiber distribution. In the inverted V-shaped pattern, the pore size exhibited a wave crest distribution along the in-plane direction, whereas, in the V-shaped pattern structure, the pore size was troughed along the in-plane direction. The three-dimensional (3D) multiphase Lattice Boltzmann method (LBM) and 3D diffusion LBM were used to investigate the liquid water percolation process and the reaction gas transport process in the GDL, respectively. The numerical results indicated that liquid water tends to concentrate in layers with macropores in the nonuniform GDL. Compared with the uniformly distributed GDL, these two pore size patterns can accelerate the drainage velocity and lower the water content. The reversed V-shaped pattern was further optimized to obtain the optimal width of the layers with macrospores. The results showed that a length of 96 mu m is recommended to balance the concentrated effect and low-concentration areas. Under dry conditions, the gas transport capacity was insensitive to pore size distribution, whereas, under partially saturated conditions, both the V-shaped and inverted V-shaped structures of a nonuniform design weakened the impeding effect of liquid water on the gas supply. Moreover, the effective gas diffusion coefficient of the nonuniform study can reach up to 3.85 times of the uniform structure. This work promotes the understanding of different in-plane distributed pore size styles on the water percolation behavior in the GDL, thereby contributing to the optimal design of the GDL and PEMFCs.
引用
收藏
页数:20
相关论文
共 50 条
  • [21] Pore-scale modeling of gas diffusion layers: Investigation of gas-liquid two-phase transport properties
    Zhang, Ning
    Chen, Wenshang
    Zhou, Haoran
    Deng, Qihao
    Chen, Ben
    INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2024, 230
  • [22] Pore-scale flow and mass transport in gas diffusion layer of proton exchange membrane fuel cell with interdigitated flow fields
    Chen, Li
    Luan, Hui-Bao
    He, Ya-Ling
    Tao, Wen-Quan
    INTERNATIONAL JOURNAL OF THERMAL SCIENCES, 2012, 51 : 132 - 144
  • [23] Degradation Characteristics of Electrospun Gas Diffusion Layers with Custom Pore Structures for Polymer Electrolyte Membrane Fuel Cells
    Balakrishnan, Manojkumar
    Shrestha, Pranay
    Lee, ChungHyuk
    Ge, Nan
    Fahy, Kieran F.
    Messerschmidt, Matthias
    Scholta, Joachim
    Eifert, Laszlo
    Maibach, Julia
    Zeis, Roswitha
    Hatton, Benjamin D.
    Bazylak, Aimy
    ACS APPLIED MATERIALS & INTERFACES, 2021, 13 (02) : 2414 - 2427
  • [24] Degradation Characteristics of Electrospun Gas Diffusion Layers with Custom Pore Structures for Polymer Electrolyte Membrane Fuel Cells
    Balakrishnan, Manojkumar
    Shrestha, Pranay
    Lee, Chunghyuk
    Ge, Nan
    Fahy, Kieran F.
    Messerschmidt, Matthias
    Scholta, Joachim
    Eifert, László
    Maibach, Julia
    Zeis, Roswitha
    Hatton, Benjamin D.
    Bazylak, Aimy
    ACS Applied Materials and Interfaces, 2021, 13 (02): : 2414 - 2427
  • [25] Effects of water dynamic behavior on oxygen transport in catalyst layers: A pore-scale study of proton exchange membrane fuel cells
    Zou, Guofu
    Chen, Wenshang
    Shen, Jun
    Yang, Tianqi
    Chen, Ben
    INTERNATIONAL COMMUNICATIONS IN HEAT AND MASS TRANSFER, 2025, 164
  • [26] Pore-Scale Modeling of Air-Water Two Phase Flow and Oxygen Transport in Gas Diffusion Layer of Proton Exchange Membrane Fuel Cell
    Zhou, Chongbo
    Guo, Lingyi
    Chen, Li
    Tian, Xin
    He, Tiefeng
    Yang, Qinghua
    ENERGIES, 2021, 14 (13)
  • [27] NUMERICAL SIMULATION OF NON-UNIFORM GAS DIFFUSION LAYER POROSITY EFFECT ON POLYMER ELECTROLYTE MEMBRANE FUEL CELL PERFORMANCE
    Roshandel, R.
    Farhanieh, B.
    INTERNATIONAL JOURNAL OF ENGINEERING, 2007, 20 (02): : 179 - 192
  • [28] Lattice Boltzmann simulation of liquid water transport in microporous and gas diffusion layers of polymer electrolyte membrane fuel cells
    Kim, Kwang Nam
    Kang, Jung Ho
    Lee, Sang Gun
    Nam, Jin Hyun
    Kim, Charn-Jung
    JOURNAL OF POWER SOURCES, 2015, 278 : 703 - 717
  • [29] Pore network modelling to enhance liquid water transport through porous transport layers for polymer electrolyte membrane electrolyzers
    Lee, J. K.
    Lee, Ch.
    Bazylak, A.
    JOURNAL OF POWER SOURCES, 2019, 437
  • [30] Investigation of the effect of pore diameter of gas diffusion layers on cold start behavior and cell performance of polymer electrolyte membrane fuel cells
    Hirakata, Satoki
    Mochizuki, Takashi
    Uchida, Makoto
    Uchida, Hiroyuki
    Watanabe, Masahiro
    ELECTROCHIMICA ACTA, 2013, 108 : 304 - 312