A pore scale model for the transport phenomena in the catalyst layer of a PEM fuel cell

被引:0
|
作者
Sui, P. C. [1 ]
Djilali, N. [1 ]
Wang, Qianpu
机构
[1] Univ Victoria, Inst Integrated Energy Syst, Victoria, BC, Canada
关键词
D O I
暂无
中图分类号
TH [机械、仪表工业];
学科分类号
0802 ;
摘要
In a proton exchange membrane fuel cell (PEMFC), the catalyst layer is a porous medium made of carbon-supported catalysts and solid electrolyte, and has a thickness in the order of 10 mu m. Within this layer, complex transport phenomena take place: transport of charged species (H(+), electrons and ionic radicals), non-charged species (gaseous H(2)O, O(2), H(2), N(2) and liquid water) and heat transfer occur in their own pathways. Furthermore, phase change of water and physiochemical/electrochemical reactions also take place on phase boundaries. These transport process take place in an intertwined network of materials having characteristic length scale ranging from nano-meters to micro-meters. The objective of the present study is two-fold, i.e., to develop a rigorous theoretical framework based on which the transport in the micro-structural level can be modelled, and to construct a pore scale model that resolves the geometry of the phases (carbon, ionomer and gas pores) for which direct numerical simulation can be performed. The theoretical framework is developed by employing the volume-averaging techniques for multi-phase porous media. The complete set of the conservation equations for all species in all phases are derived and every interfacial transport is accounted. The problem of model closure on the terms in the transport equations is addressed by the pore-scale model reported in the present study. A 3-D pore-scale model is constructed by a solid model that consists of packing spherical carbon particles and simulated ionomer coating on these carbon aggregates. The index system of the pore-scale model allows easy identification of volumetric pathway, interfaces and triple phase boundaries. The transport of charged and non-charged species is simulated by solving the equations based on first principle in the entire representative element volume (REV) domain. The computational domain contains typically several million cells and a parallelized, iterative solver, GMRES, is employed to solve the coupled transport with complex geometries. Computational results based on the pore-scale model show that the effective transport properties of the species are strongly affected by the micro-structure, e.g. morphology and phase-connectivity. Further simulations and investigation on the coupling effects of the transport are underway. Combination of the proposed theoretical framework and pore-scale model will lay a foundation for the construction of multi-scale modelling of the PEMFC catalyst layer. On the one hand, the pore-scale model helps close the macroscopic volume-averaged equations in the framework. On the other hand, the pore-scale model provides a platform to include microscopic or atomistic simulations.
引用
下载
收藏
页码:1325 / 1332
页数:8
相关论文
共 50 条
  • [41] PEM Fuel Cell Catalyst Layer Structure Degradation During Carbon Corrosion
    Borup, Rodney L.
    Mukundan, Rangachary
    Fairweather, Joseph
    Spernjak, Dusan
    Langlois, David
    Davey, John
    More, Karren
    Artyushkova, Kateryna
    POLYMER ELECTROLYTE FUEL CELLS 13 (PEFC 13), 2013, 58 (01): : 945 - 952
  • [42] Ionic resistance of the catalyst layer after the PEM fuel cell suffered freeze
    Hou, Junbo
    Song, Wei
    Yu, Hongmei
    Fu, Yu
    Hao, Lixing
    Shao, Zhigang
    Yi, Baolian
    JOURNAL OF POWER SOURCES, 2008, 176 (01) : 118 - 121
  • [43] Transient behavior of CO poisoning of the anode catalyst layer of a PEM fuel cell
    Chu, H. S.
    Wang, C. P.
    Liao, W. C.
    Yan, W. M.
    JOURNAL OF POWER SOURCES, 2006, 159 (02) : 1071 - 1077
  • [44] Pore scale modelling of a cathode catalyst layer in fuel cell environment: agglomerate reconstruction and variables optimization
    T. Sousa
    C. M. Rangel
    Journal of Solid State Electrochemistry, 2016, 20 : 541 - 554
  • [45] Pore scale modelling of a cathode catalyst layer in fuel cell environment: agglomerate reconstruction and variables optimization
    Sousa, T.
    Rangel, C. M.
    JOURNAL OF SOLID STATE ELECTROCHEMISTRY, 2016, 20 (02) : 541 - 554
  • [46] A pseudo-homogeneous model for cathode catalyst layer of PEM fuel cells
    You, Lixin
    Liu, Hongtan
    American Society of Mechanical Engineers, Heat Transfer Division, (Publication) HTD, 2000, 366 : 51 - 59
  • [47] A Multiscale Method for Multiphase Pore-Scale Simulation of the Polymer Electrolyte Fuel Cell Catalyst Layer
    Zheng, Weibo
    Kim, Seung Hyun
    MULTISCALE MODELING, SIMULATION AND DESIGN - FROM CONVENTIONAL METHODS TO THE LATEST IN DATA SCIENCE, 2018, 85 (05): : 77 - 86
  • [48] PEM fuel cell cathode catalyst layer durability: An electrochemical spectroscopic investigation
    Shaneeth, M.
    Basu, Suddhasatwa
    Aravamuthan, S.
    CHEMICAL ENGINEERING SCIENCE, 2016, 154 : 72 - 80
  • [49] Modeling the catalyst layer of a PEM fuel cell cathode using a dimensionless approach
    Jeng, KT
    Kuo, CP
    Lee, SF
    JOURNAL OF POWER SOURCES, 2004, 128 (02) : 145 - 151
  • [50] A mathematical model and optimization of the cathode catalyst layer structure in PEM fuel cells
    Wang, QP
    Song, DT
    Navessin, T
    Holdcroft, S
    Liu, ZS
    ELECTROCHIMICA ACTA, 2004, 50 (2-3) : 725 - 730