Lattice Boltzmann simulation of oxygen diffusion and electrochemical reaction inside catalyst layer of PEM fuel cells

被引:31
作者
Deng, Hao [1 ]
Hou, Yuze [1 ]
Chen, Wenmiao [2 ]
Pan, Fengwen [2 ]
Jiao, Kui [1 ]
机构
[1] Tianjin Univ, State Key Lab Engines, 135 Yaguan Rd, Tianjin 300350, Peoples R China
[2] Weichai Power Co Ltd, 197A Fushou St E, Weifang 261016, Peoples R China
基金
中国国家自然科学基金;
关键词
Catalyst layer; Oxygen transport; Electrochemical reaction; Lattice Boltzmann; Stochastic algorithm; EFFECTIVE TRANSPORT-PROPERTIES; LIQUID WATER TRANSPORT; REDUCTION REACTION; MASS-TRANSPORT; CATHODE; RECONSTRUCTION; MODEL; FLOW; PERFORMANCE; ELECTRODE;
D O I
10.1016/j.ijheatmasstransfer.2019.118538
中图分类号
O414.1 [热力学];
学科分类号
摘要
An in-depth understanding of pore-scale transport process and electrode reaction kinetics is critical to ease the sluggish oxygen reduction reaction of proton exchange membrane fuel cells. In this study, the effects of catalyst layer microstructure on the oxygen diffusion and electrochemical reaction consumption are analyzed, based on the developed 3D single-phase lattice Boltzmann model and optimized stochastic reconstruction algorithm. The results suggest that increasing the ionomer content and platinum loading are beneficial to increasing the active sites, while the oxygen transport along the thickness direction becomes more difficult due to the narrowed pores, so the platinum particles in the back region have less participation in the reaction, which causes the significant catalyst waste and limits the further cost reduction and improvement of power density. Improving the carbon particle diameter ensures the enlarged pores and more effective Pt particles covered by ionomer, thus enhances the oxygen supply and electrochemical reaction rate. (C) 2019 Elsevier Ltd. All rights reserved.
引用
收藏
页数:16
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