Simulation of OH- and oxygen transport in the air-cathode catalyst layer of microbial fuel cells

被引:3
作者
Cai, Wenfang [1 ]
Geng, Jiafeng [4 ]
Zhao, Shifeng [2 ]
Zhu, Yucheng [3 ]
Wang, Yunhai [3 ]
Chen, Qingyun [2 ]
Guo, Kun [1 ]
机构
[1] Xi An Jiao Tong Univ, Sch Chem Engn & Technol, Xian 710049, Peoples R China
[2] Xi An Jiao Tong Univ, State Key Lab Multiphase Flow Power Engn, Xian 710049, Peoples R China
[3] Xi An Jiao Tong Univ, Dept Environm Sci & Engn, Xian 710049, Peoples R China
[4] Changan Univ, Sch Water & Environm, Dept Chem Engn, Xian 710054, Peoples R China
基金
中国国家自然科学基金; 中国博士后科学基金;
关键词
Air-cathode MFC; Catalyst layer; Mass transfer; OH-; transport; REDUCTION REACTION; CARBON; PERFORMANCE; THICKNESS; MODEL;
D O I
10.1016/j.elecom.2023.107494
中图分类号
O646 [电化学、电解、磁化学];
学科分类号
081704 ;
摘要
The mass transfer of OH- and oxygen within an air-cathode is critical for the performance of microbial fuel cells (MFCs). Improving the understanding of this complex transportation mechanism could help guide the design of air-cathodes to enhance the power density of MFCs. Herein, a 2D-agglomerate model is developed to study OH- and O2 transfer, and electrochemical performance within an air-cathode MFC. The effects of key variables (binder volume fraction, and Pt/carbon mass ratio) on OH- and oxygen transport behavior have been investi-gated. Simulation results reveal that the OH- and oxygen concentrations within the catalyst layer are closely related to the catalyst layer structure. A lower volume fraction of Nafion (R) binder is beneficial to OH- and oxygen transfer, while the Pt/carbon mass ratio has complex effects on OH- and oxygen transfer and reactions. This work aims to improve our understanding of OH- and oxygen mass transfer and offers an effective approach to con-structing high-performance air-cathode MFCs.
引用
收藏
页数:7
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