Author
Listed:
- Jinqiang Zhang
(University of Toronto
University of Toronto
University of Technology Sydney)
- Yufei Cao
(University of Toronto
Tsinghua University)
- Pengfei Ou
(University of Toronto)
- Geonhui Lee
(University of Toronto
Seoul National University)
- Yufei Zhao
(University of Toronto
University of Technology Sydney)
- Shijie Liu
(University of Toronto)
- Erfan Shirzadi
(University of Toronto)
- Roham Dorakhan
(University of Toronto)
- Ke Xie
(University of Toronto)
- Cong Tian
(University of Toronto)
- Yuanjun Chen
(University of Toronto)
- Xiaoyan Li
(University of Toronto)
- Yurou Celine Xiao
(University of Toronto)
- Ali Shayesteh Zeraati
(University of Toronto)
- Rui Kai Miao
(University of Toronto)
- Sungjin Park
(University of Toronto)
- Colin P. O’Brien
(University of Toronto)
- Jun Ge
(Tsinghua University)
- Xin Zhou
(South China University of Technology)
- David Sinton
(University of Toronto)
- Edward H. Sargent
(University of Toronto)
Abstract
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.
Suggested Citation
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 Z, 2025.
"A redox-active polymeric network facilitates electrified reactive-capture electrosynthesis to multi-carbon products from dilute CO2-containing streams,"
Nature Communications, Nature, vol. 16(1), pages 1-9, December.
Handle:
RePEc:nat:natcom:v:16:y:2025:i:1:d:10.1038_s41467-025-58756-9
DOI: 10.1038/s41467-025-58756-9
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