Integrated system for electrolyte recovery, product separation, and CO<sub>2</sub> capture in CO<sub>2</sub> reduction.

Wang, Peng; Pei, An; Chen, Zhaoxi; Sun, Peilin; Hu, Chengyi; Wang, Xue; Zheng, Nanfeng; Chen, Guangxu · Nat Commun · 2025

basic_science · Level V

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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.