氧还原反应
氧气
电极
动力学
氧还原
克拉克电极
化学
图层(电子)
电化学
薄层
还原(数学)
无机化学
材料科学
化学工程
物理化学
电解质
有机化学
物理
几何学
数学
量子力学
工程类
作者
Eva Marra,Henrik Grimler,Gerard Montserrat-Sisó,Rakel Wreland Lindström,Björn Wickman,Göran Lindbergh,Carina Lagergren
标识
DOI:10.1016/j.electacta.2022.141376
摘要
• ORR kinetics is studied in an AEMFC using the thin-film Pt/GDL electrode • Above 0.8 V a Tafel slope of 60 mV dec −1 was obtained at 30°C and 100 % RH • The reaction order decreases from close to 2 at 0.85 V to 1 at 0.65 V • The setup with the double-MEA restricts the H 2 crossover and enables CO stripping The study of the catalytic activity in a fuel cell is challenging, as mass transport, gas crossover and the counter electrode are generally interfering. In this study, a Pt electrode consisting of a thin film deposited on the gas diffusion layer was employed to study the oxygen reduction reaction (ORR) in an operating Anion Exchange Membrane Fuel Cell (AEMFC). The 2D Pt electrode was assembled together with a conventional porous Pt/C counter electrode and an extra Pt/C layer and membrane to reduce the H 2 crossover. Polarization curves at different oxygen partial pressures were recorded and the resulting reproducible ORR activities were normalized with respect to the active surface area (ECSA), obtained by CO stripping. As expected, decreasing the oxygen partial pressure results in a negative shift in open circuit voltage (OCV), cell voltage and maximum attainable current density. For cell voltages above 0.8 V a fairly constant Tafel slope of 60 mV dec −1 was recorded but at lower voltages the slope increases rapidly. The observed Tafel slope can be explained by a theoretical model with an associative mechanism where charge- and proton-transfer steps are decoupled, and the proton transfer is the rate-determining step. A reaction order of 1 with respect to O 2 was obtained at 0.65 V which corresponds well with the mechanism suggested above. Based on the obtained catalyst activities, the electrode performance is comparable to good porous electrodes found in the field. The methodology presented in this study is expected to be useful in future kinetic studies of other catalysts for AEMFC.
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