Integrated system for electrolyte recovery, product separation, and CO<sub>2</sub> capture in CO<sub>2</sub> reduction.
basic_science · Level V
Where this comes from
- Record sourced from PubMed, PMID 39820283.
- Also identified by DOI 10.1038/s41467-025-56111-6 and PMC identifier 11739585.
- Licence recorded as CC BY-NC-ND.
- Because redistribution is not established, this page shows the abstract only. Follow the links below for the full text.
Abstract
Challenges in CO<sub>2</sub> capture, CO<sub>2</sub> crossover, product separation, and electrolyte recovery hinder electrocatalytic CO<sub>2</sub> reduction (CO<sub>2</sub>R). Here, we present an integrated electrochemical recovery and separation system (ERSS) with an ion separation module (ISM) between the anode and cathode of a water electrolysis system. During ERSS operation, protons from the anolyte flow through the anodic cation exchange membrane (CEM) into the ISM, acidifying the CO<sub>2</sub>R effluent electrolyte. Cations like K<sup>+</sup> in the ISM flow through the cathodic CEM into the catholyte to balance the OH<sup>-</sup> ions from hydrogen evolution. ERSS recycles electrolyte-adsorbed CO<sub>2</sub>, recovers KOH with a 94.0% K<sup>+</sup> yield, and achieves an 86.2% separation efficiency for CO<sub>2</sub>R products. The recovered KOH can capture CO<sub>2</sub> from air or flue gas or be utilized as a CO<sub>2</sub>R electrolyte, closing the CO<sub>2</sub> capture, conversion, and utilization loop. Compared to the conventional acid-base neutralization process, ERSS saves $119.76 per ton of KOH recovered and is applicable to other aqueous alkaline electrosynthesis reactions.