Microscale simulations of reaction and mass transport in cathode catalyst layer of polymer electrolyte fuel cell

被引:14
|
作者
Inoue, Gen [1 ]
Park, Kayoung [1 ]
So, Magnus [1 ]
Kimura, Naoki [1 ]
Tsuge, Yoshifumi [1 ]
机构
[1] Kyushu Univ, Fac Engn, Dept Chem Engn, Nishi Ku, 744 Motooka, Fukuoka 8190395, Japan
关键词
Polymer electrolyte fuel cells; Catalyst layer; Heterogeneous porous structure; Simulation; Carbon aggregate structure; Current density distribution; GAS-DIFFUSION LAYER; FOCUSED ION-BEAM; OXYGEN REDUCTION; OXIDE COVERAGE; CORROSION BEHAVIORS; CARBON SUPPORT; MODEL; PERFORMANCE; IONOMER; MICROSTRUCTURE;
D O I
10.1016/j.ijhydene.2022.02.021
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The resistance of the cathode oxygen reduction reaction in polymer electrolyte fuel cells must be reduced for improving the performance. Therefore, it is important to thoroughly understand the relationship between the heterogeneous structures and the cell performance. However, it is difficult to obtain such an understanding using experimental approaches and typical uniform porous simulations. In this study, numerical analysis was used to simulate a three-dimensional catalyst layer (CL) with carbon black (CB) aggregate structures and ionomer coating models, and a cathode reaction and mass transport simulation model incorporating the heterogeneous structure was developed. Moreover, the relationship between the electrode structure and the cell performance, including the reaction distribution and output performance, was examined. The current density distribution depended on the CB structure and ionomer adhesion shape. From the viewpoint of enhancing both the Pt utilization and the mass transport performance, an adequate heterogeneous pore structure in the CL is necessary. These results were used to determine the optimal material properties for the high performance cell.(c) 2022 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:12665 / 12683
页数:19
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