A redox-active polymeric network facilitates electrified reactive-capture electrosynthesis to multi-carbon products from dilute CO<sub>2</sub>-containing streams.
basic_science · Level V
Where this comes from
- Record sourced from PubMed, PMID 40229285.
- Also identified by DOI 10.1038/s41467-025-58756-9 and PMC identifier 11997176.
- Licence recorded as CC BY-NC-ND.
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Abstract
Reactive capture - the integration of CO<sub>2</sub> capture with electrochemical upgrade - offers the prospect of improving overall energy efficiency in captured-CO<sub>2</sub>-to-fuels by eliminating the gas-phase CO<sub>2</sub> desorption step, and by further offering a CO<sub>2</sub>-free gas product stream. Two related challenges limit the potential impact of electrified reactive capture today: its propensity to produce lower-value C<sub>1</sub> products (carbon products containing one carbon atom per molecule); and its failure to retain performance when fed dilute streams (e.g. ~1-10% CO<sub>2</sub>). We posit that these could be addressed using catalysts that locally concentrate and activate in-situ generated CO<sub>2</sub>: we integrate a redox-active polymeric network whose polymer fragments undergo reversible reduction during the electrochemical conversion process, enabling electron transfer to CO<sub>2</sub> molecules generated in-situ from carbonate capture liquid. We report as a result a 55 ± 5% C<sub>2+</sub> (carbon products containing two or more carbon atoms per molecule) Faradaic efficiency (FE) at 300 mA/cm<sup>2</sup> in an electrochemical reactive capture system in which the electrolysis stage is fed with 1 M K<sub>2</sub>CO<sub>3</sub>. We obtain 56 ± 4 wt% C<sub>2</sub>H<sub>4</sub> in the product gas stream. When we use a dilute stream consisting of 1% CO<sub>2</sub> in N<sub>2</sub> at the KOH capture stage, we retain the C<sub>2+</sub> FE to within 85% (relative) of its value achieved in the case of pure CO<sub>2</sub>.