电合成
氧化还原
溪流
化学
碳纤维
化学工程
计算机科学
电化学
无机化学
电极
算法
计算机网络
复合数
工程类
物理化学
作者
Jinqiang Zhang,Yufei Cao,Pengfei Ou,Geonhui Lee,Yufei Zhao,Shijie Liu,Erfan Shirzadi,Roham Dorakhan,Ke Xie,Cong Tian,Yuanjun Chen,Xiaoyan Li,Yurou Celine Xiao,Ali Shayesteh Zeraati,Rui Kai Miao,Sungjin Park,Colin P. O’Brien,Jun Ge,Xin Zhou,David Sinton
标识
DOI:10.1038/s41467-025-58756-9
摘要
Reactive capture - the integration of CO2 capture with electrochemical upgrade - offers the prospect of improving overall energy efficiency in captured-CO2-to-fuels by eliminating the gas-phase CO2 desorption step, and by further offering a CO2-free gas product stream. Two related challenges limit the potential impact of electrified reactive capture today: its propensity to produce lower-value C1 products (carbon products containing one carbon atom per molecule); and its failure to retain performance when fed dilute streams (e.g. ~1-10% CO2). We posit that these could be addressed using catalysts that locally concentrate and activate in-situ generated CO2: we integrate a redox-active polymeric network whose polymer fragments undergo reversible reduction during the electrochemical conversion process, enabling electron transfer to CO2 molecules generated in-situ from carbonate capture liquid. We report as a result a 55 ± 5% C2+ (carbon products containing two or more carbon atoms per molecule) Faradaic efficiency (FE) at 300 mA/cm2 in an electrochemical reactive capture system in which the electrolysis stage is fed with 1 M K2CO3. We obtain 56 ± 4 wt% C2H4 in the product gas stream. When we use a dilute stream consisting of 1% CO2 in N2 at the KOH capture stage, we retain the C2+ FE to within 85% (relative) of its value achieved in the case of pure CO2.
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