TY - JOUR
T1 - Microscale simulations of reaction and mass transport in cathode catalyst layer of polymer electrolyte fuel cell
AU - Inoue, Gen
AU - Park, Kayoung
AU - So, Magnus
AU - Kimura, Naoki
AU - Tsuge, Yoshifumi
N1 - Funding Information:
This research was supported by the New Energy and Industrial Technology Development Organization (NEDO) , Japan (grant number P20003-20001327-0 ). This study collaborated to MEXT “Program for Promoting Researches on the Supercomputer Fugaku” (Fugaku Battery & Fuel Cell Project) (grant number JPMXP1020200301 ).
Funding Information:
This research was supported by the New Energy and Industrial Technology Development Organization (NEDO), Japan (grant number P20003-20001327-0). This study collaborated to MEXT ?Program for Promoting Researches on the Supercomputer Fugaku? (Fugaku Battery & Fuel Cell Project) (grant number JPMXP1020200301).
Publisher Copyright:
© 2022 Hydrogen Energy Publications LLC
PY - 2022
Y1 - 2022
N2 - 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.
AB - 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.
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U2 - 10.1016/j.ijhydene.2022.02.021
DO - 10.1016/j.ijhydene.2022.02.021
M3 - Article
AN - SCOPUS:85125483091
JO - International Journal of Hydrogen Energy
JF - International Journal of Hydrogen Energy
SN - 0360-3199
ER -