Effect of Humidity on C1, C2 Product Selectivity for CO2 Reduction in a Hybrid Gas/Liquid Electrochemical Reactor

被引:2
|
作者
Lee, Seung-Hoon [1 ]
Song, Yang [2 ]
Iglesias, Brandon [2 ]
Everitt, Henry O. [3 ,4 ]
Liu, Jie [1 ]
机构
[1] Duke Univ, Dept Chem, Durham, NC 27708 USA
[2] Reactwell LLC, New Orleans, LA 70112 USA
[3] Rice Univ, US Army DEVCOM Army Res Lab South, Houston, TX 77005 USA
[4] Duke Univ, Dept Phys, Durham, NC 27708 USA
基金
美国国家科学基金会;
关键词
electrochemical flow reactor; hybrid gas/liquid reactor; CO2 reduction reaction; hydrogen evolution reaction product selectivity; three-phase interface; ELECTROCATALYTIC REDUCTION; CARBON-DIOXIDE; ELECTROREDUCTION; MECHANISMS; CONVERSION; CATALYST; DESIGN;
D O I
10.1021/acsaem.2c02226
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
Hybrid gas/liquid-fed electrochemical flow reactors may become attractive alternatives for chemical synthesis once it is understood how catalytic product selectivity may be optimized through the control of gas phase reactants. Using a constant pH basic electrolyte to suppress the hydrogen evolution reaction, we explore how protonation by water vapor added to the flowing CO2 supply affects the CO(2)reduction reaction. Although H2 remains the dominant product, supplying dry CO2 gas selectively produces more C-2 products than C-1. However, adding protons through water vapor changes selectivity toward C-1 products, increasing the overall faradaic efficiency of hydrocarbon production while reducing H-2 production.
引用
收藏
页码:9309 / 9314
页数:6
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