Dec 4, 2024
4:15pm - 4:30pm
Hynes, Level 3, Room 307
Jeong Hyun Kim1,Junho Jang1,Youngin Cho1,Ki Tae Nam1
Seoul National University1
Electrochemical methods are promising for CO
2 mitigation due to their potential for high energy efficiency, adaptability to decentralized operations, and alignment with renewable energy sources. Among the two main approaches for electrochemical CO
2 mitigation—electrochemical CO
2 capture and electrochemical CO
2 reduction—the extended concept of redox-flow batteries often adopts the CO
2 capture approach. In these systems, cathode reactions generate alkaline species capable of capturing CO
2. Diluted CO
2 streams are treated by contact with an electrolyte containing these species, followed by oxidation reactions that facilitate CO
2 release, ultimately separating CO
2 from the feed gas. To achieve an energy-efficient capture process, research focuses on developing cell components, primarily redox-active species with high reversibility and facile reaction kinetics, such as quinones, bipyridines, and transition metal complexes.
While the use of separated CO
2 gas is addressed in other fields, integrating CO
2 capture and utilization processes can significantly reduce overall energy requirements. Thus, electrochemical systems that simultaneously generate bases and reduce CO
2 are under development. In these systems, electrons are introduced to chemisorbed CO
2 species such as carbamates and carbonates, yielding CO
2 reduction products and bases.
In this study, we propose a redox-flow system that captures CO
2 and subsequently converts it into cyclic carbonates. Our system integrates CO
2 capture and conversion through a series of domino reactions triggered by the electrochemical generation of organic bases. Unlike other redox flow systems that use redox-active species targeting highly reversible redox reactions for CO
2 capture, our system utilizes vicinal halohydrin molecules as precursors of alkaline species, which spontaneously undergo intramolecular cyclization reactions after capturing CO
2 and yield cyclic carbonates. Our method achieves a Faradaic efficiency of up to 100% for ethylene carbonate production, demonstrating highly selective sequential capture and conversion reactions. Additionally, it is expandable to the synthesis of various cyclic carbonates directly from diluted CO
2 sources.