过电位
塔菲尔方程
电解
阴极
电化学
催化作用
化学
电催化剂
无机化学
电解质
化学工程
电极
物理化学
生物化学
工程类
作者
Sumit Verma,Yuki Hamasaki,Chaerin Kim,Wenxin Huang,Shawn Lu,Huei-Ru Molly Jhong,Andrew A. Gewirth,Tsuyohiko Fujigaya,Naotoshi Nakashima,Paul J. A. Kenis
出处
期刊:ACS energy letters
[American Chemical Society]
日期:2017-12-18
卷期号:3 (1): 193-198
被引量:493
标识
DOI:10.1021/acsenergylett.7b01096
摘要
Cost competitive electroreduction of CO2 to CO requires electrochemical systems that exhibit partial current density (jCO) exceeding 150 mA cm–2 at cell overpotentials (|ηcell|) less than 1 V. However, achieving such benchmarks remains difficult. Here, we report the electroreduction of CO2 on a supported gold catalyst in an alkaline flow electrolyzer with performance levels close to the economic viability criteria. Onset of CO production occurred at cell and cathode overpotentials of just −0.25 and −0.02 V, respectively. High jCO (∼99, 158 mA cm–2) was obtained at low |ηcell| (∼0.70, 0.94 V) and high CO energetic efficiency (∼63.8, 49.4%). The performance was stable for at least 8 h. Additionally, the onset cathode potentials, kinetic isotope effect, and Tafel slopes indicate the low overpotential production of CO in alkaline media to be the result of a pH-independent rate-determining step (i.e., electron transfer) in contrast to a pH-dependent overall process.
科研通智能强力驱动
Strongly Powered by AbleSci AI