Insights into the Low Overpotential Electroreduction of CO2 to CO on a Supported Gold Catalyst in an Alkaline Flow Electrolyzer
Abstract
Cost competitive electroreduction of CO 2 to CO requires electrochemical systems that exhibit partial current density ( j CO ) exceeding 150 mA cm –2 at cell overpotentials (|η cell |) less than 1 V. However, achieving such benchmarks remains difficult. Here, we report the electroreduction of CO 2 on a supported gold catalyst in an alkaline flow electrolyzer with performance levels close to the economic viability criteria. Onset of CO production occurred at cell and cathode overpotentials of just −0.25 and −0.02 V, respectively. High j CO (∼99, 158 mA cm –2 ) was obtained at low |η cell | (∼0.70, 0.94 V) and high CO energetic efficiency (∼63.8, 49.4%). The performance was stable for at least 8 h. Additionally, the onset cathode potentials, kinetic isotope effect, and Tafel slopes indicate the low overpotential production of CO in alkaline media to be the result of a pH-independent rate-determining step (i.e., electron transfer) in contrast to a pH-dependent overall process.
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For catalysts producing CO (Au, Ag, etc.) or formate (Sn, Pb, etc.), elevated pressures do not greatly influence selectivity, but reduce cathodic overpotentials.
“For catalysts producing CO (Au, Ag, etc.) or formate (Sn, Pb, etc.), elevated pressures do not greatly influence selectivity, [139,143,202,220,221,[223][224][225][226] but reduce cathodic overpotentials.[131,143,221,224,225]”
From Electrochemical CO <sub>2</sub> Reduction into Chemical Feedstocks: From Mechanistic Electrocatalysis Models to System Design (2019) · cites this paper as [143]
Some catalysts (Fe, Co, Rh, Ni, Pd, Pt, and C) with predominantly H2 selectivity at 1 atm can generate CO or HCOOH when pressurized.
“In addition, some catalysts (Fe, Co, Rh, Ni, Pd, Pt, and C) with predominantly H2 selectivity at 1 atm can generate CO or HCOOH when pressurized.[140,141,143,223,[227][228][229]”
From Electrochemical CO <sub>2</sub> Reduction into Chemical Feedstocks: From Mechanistic Electrocatalysis Models to System Design (2019) · cites this paper as [143]
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- Authors
- Verma, S., Hamasaki, Y., Kim, C., Huang, W., Lu, S., Jhong, H.-R. M., Gewirth, A. A., Fujigaya, T., Nakashima, N., & Kenis, P. J. A.
- Affiliations
- Kyushu University (JP)
- University of Illinois Urbana-Champaign (US)
- Corresponding author
- Fujigaya, Tsuyohiko
- Nakashima, Naotoshi
- Kenis, Paul J. A.
- ORCID
- Venue
- ACS Energy Letters
- Publisher
- American Chemical Society (ACS)
- Published
- 2017-12-18
- Volume
- 3
- Issue
- 1
- Pages
- 193-198
- ISSN
- 2380-8195 (ISSN-L)
- OpenAlex
- W2776913936
- Cited by
- 521
- References
- 52
- Citations by year
- 2026: 44 · 2025: 44 · 2024: 56 · 2023: 69 · 2022: 76 · 2021: 83 · 2020: 71 · 2019: 61 · 2018: 17
- FWCI
- 10.90
- Type
- journal article
- Language
- en
- Open access
- closed
- Locations
- ACS Energy Letters (publishedVersion)
- Funders
- Ministry of Education, Culture, Sports, Science and Technology
- Dow Chemical Company
- Topics
- Physical Sciences › Energy › Renewable Energy, Sustainability and the Environment › CO2 Reduction Techniques and Catalysts
- Physical Sciences › Energy › Renewable Energy, Sustainability and the Environment › Electrocatalysts for Energy Conversion
- Physical Sciences › Chemical Engineering › Catalysis › Catalysts for Methane Reforming
- Keywords
- electrochemical CO2 reduction, co-production, supported gold catalysts, low overpotential, kinetic isotope effects, Tafel slope, rate-determining step, electron transfer, energy efficiency, electrocatalyst stability
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