2020
DOI: 10.1016/j.jcou.2019.10.016
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Two-step electrochemical reduction of CO2 towards multi-carbon products at high current densities

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Cited by 59 publications
(65 citation statements)
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“…The gas product stream was then fed to the cathode chamber of the CO electrolyser, which contains a commercial copper catalyst for CO reduction, 1 M KOH as the anolyte and a NiFeO x anode. This design is similar to a tandem system previously reported by Romero Cuellar et al 23 . By maximizing the conversion of the first and second electrolysers, as well as specifically targeting acetate over other multi-carbon products, this system was able to achieve a single-pass conversion of CO 2 to acetate of 25%, a large improvement over the <1% conversion previously reported (Supplementary Table 1).…”
Section: Resultssupporting
confidence: 67%
“…The gas product stream was then fed to the cathode chamber of the CO electrolyser, which contains a commercial copper catalyst for CO reduction, 1 M KOH as the anolyte and a NiFeO x anode. This design is similar to a tandem system previously reported by Romero Cuellar et al 23 . By maximizing the conversion of the first and second electrolysers, as well as specifically targeting acetate over other multi-carbon products, this system was able to achieve a single-pass conversion of CO 2 to acetate of 25%, a large improvement over the <1% conversion previously reported (Supplementary Table 1).…”
Section: Resultssupporting
confidence: 67%
“…The CO 2 /CO mixture from the first electrolyzer can in principle directly be fed to the second electrolyzer, but initial experimental results show that the presence of large amounts of CO 2 in the mixture has a detrimental effect on the product distribution. 46 …”
Section: Process Design and Modelingmentioning
confidence: 99%
“…The feasibility of two-step tandem CO 2 electrolysis has been demonstrated experimentally by Romero Cuellar and coworkers, who reported a total CO 2 reduction current density of 300 mA/ cm 2 with a cumulative Faradaic efficiency of 62% toward C 2+ products. 10 While this is an excellent proof of concept, the system is far from optimized when compared to standalone CO 2 and CO electrolysis technologies. Low CO 2 conversion in the first reactor led to a scrubber being necessary to remove excess CO 2 before the CO electrolyzer, vastly reducing the conversion of fed CO 2 to C 2+ products.…”
Section: Two-step Tandem Co 2 Electrolysis Processmentioning
confidence: 99%