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Updated: Jul 2, 2026

Synthesis and Performance Characterizations of Transition Metal Single Atom Catalyst for Electrochemical CO2 Reduction
Published on: April 10, 2018
Electrochemical processing of carbon dioxide.
1Department of Chemical and Biological Engineering, University of British Columbia, 2360 East Mall, Vancouver, B.C. V6T 1Z3, Canada. coloman@intergate.ca
Electrochemical reduction of carbon dioxide (CO(2)) to formate is feasible in continuous reactors. This technology offers a viable pathway for converting CO(2) into valuable chemicals like formate salts and formic acid.
Area of Science:
- Electrochemistry
- Chemical Engineering
- Climate Change Mitigation
Background:
- Carbon dioxide (CO(2)) emissions negatively impact the global climate.
- Developing processes to convert CO(2) into valuable products is crucial.
- Electrochemical reduction of CO(2) offers a promising route for CO(2) utilization.
Purpose of the Study:
- To assess the viability of electrosynthesis processes for formate salts and formic acid from CO(2).
- To evaluate conceptual flowsheet designs for commercial-scale CO(2) conversion.
- To examine the potential of trickle-bed continuous electrochemical reactors for CO(2) reduction.
Main Methods:
- Laboratory-scale experiments on a 100 A scale.
- Development of conceptual process flowsheets for two distinct conversion options.
- Analysis of CO(2) conversion at a rate of 100 tonnes per day.
Main Results:
- Successful reduction of CO(2) to formate (HCO(2)(-)) in a trickle-bed continuous electrochemical reactor.
- Demonstration of industrially viable conditions for CO(2) electroreduction.
- Identification of cathode stability and formate crossover as key challenges.
Conclusions:
- Trickle-bed continuous electrochemical reactors show potential for commercial CO(2) to formate production.
- Overcoming challenges in cathode stability and formate crossover is essential for commercialization.
- The proposed processes offer a viable route for converting CO(2) into formate salts and formic acid.
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