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High Resolution Image Download MS PowerPoint Slide This study represents a first step toward integrating CO 2 capture and electrochemical conversion by investigating the use of 0.5 M monoethanolamine (MEA)─a widely used industrial CO 2 absorbent─in a nonaqueous electrolyte composed of choline chloride and ethylene glycol (1:4 mole ratio). This electrolyte was selected to enhance the CO 2 solubility and catalytic performance while minimizing the water content and suppressing hydrogen evolution. This electrolyte was tested in a compact two-compartment H-cell electrolyzer operating at 65 °C─a temperature reflecting industrially relevant conditions. To further improve the stability and selectivity of the CO 2 RR to CO, pulsed electrolysis was employed. This approach effectively addressed key drawbacks of static electrolysis by modulating the electric field, enhancing mass transport, and inducing electrode surface restructuring. Additionally, ethylenediaminetetraacetic acid (EDTA) was introduced to chelate trace metal impurities and further stabilize the process. The combined use of EDTA and pulsed electrolysis (pulse potential of 0 V vs. Ag/AgCl for 20 s) effectively restructured the electrode surface, resulting in improved current stability and a notable increase in faradaic efficiency for CO up to 60%. Overall, our findings demonstrate the potential of pulsed electrolysis and EDTA in overcoming the limitations of static electrolysis and provide a foundational framework for integrated CO 2 capture and conversion processes using multifunctional nonaqueous electrolytes.
Farahmandazad et al. (Tue,) studied this question.
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