TY - JOUR
T1 - Carbon- and energy-efficient ethanol electrosynthesis via interfacial cation enrichment
AU - Shayesteh Zeraati, Ali
AU - Li, Feng
AU - Alkayyali, Tartela
AU - Dorakhan, Roham
AU - Shirzadi, Erfan
AU - Arabyarmohammadi, Fatemeh
AU - O’Brien, Colin P.
AU - Gabardo, Christine M.
AU - Kong, Jonathan
AU - Ozden, Adnan
AU - Zargartalebi, Mohammad
AU - Zhao, Yong
AU - Fan, Lizhou
AU - Papangelakis, Panagiotis
AU - Kim, Dongha
AU - Park, Sungjin
AU - Miao, Rui Kai
AU - Edwards, Jonathan P.
AU - Young, Daniel
AU - Ip, Alexander H.
AU - Sargent, Edward H.
AU - Sinton, David
N1 - Publisher Copyright:
© The Author(s), under exclusive licence to Springer Nature Limited 2024.
PY - 2025/1
Y1 - 2025/1
N2 - The use of acidic electrolytes in CO2 reduction avoids costly carbonate loss. However, the energy efficiency of acid-fed electrolysers has been limited by high hydrogen production and operating potentials. We find that these stem from the lack of alkali cations at the catalyst surface, limiting CO2 and CO adsorption. In acid-fed membrane electrode assembly systems, the incorporation of these cations is challenging as there is no flowing catholyte. Here an interfacial cation matrix (ICM)–catalyst heterojunction is designed that directly attaches to the catalyst layer. The negatively charged nature of the ICM enriches the alkali cation concentration near the cathode surface, trapping generated hydroxide ions. This increases the local electric field and pH, increasing multi-carbon production. Integrating the ICM strategy with a tailored copper–silver catalyst enables selective ethanol production through a proton-spillover mechanism. We report a 45% CO2-to-ethanol Faradaic efficiency at 200 mA cm−2, carbon efficiency of 63%, full-cell ethanol energy efficiency of 15% (3-fold improvement over the best previous acidic CO2 reduction value) and energy cost of 260 GJ per tonne ethanol, the lowest among reported ethanol-producing CO2 electrolysers. (Figure presented.)
AB - The use of acidic electrolytes in CO2 reduction avoids costly carbonate loss. However, the energy efficiency of acid-fed electrolysers has been limited by high hydrogen production and operating potentials. We find that these stem from the lack of alkali cations at the catalyst surface, limiting CO2 and CO adsorption. In acid-fed membrane electrode assembly systems, the incorporation of these cations is challenging as there is no flowing catholyte. Here an interfacial cation matrix (ICM)–catalyst heterojunction is designed that directly attaches to the catalyst layer. The negatively charged nature of the ICM enriches the alkali cation concentration near the cathode surface, trapping generated hydroxide ions. This increases the local electric field and pH, increasing multi-carbon production. Integrating the ICM strategy with a tailored copper–silver catalyst enables selective ethanol production through a proton-spillover mechanism. We report a 45% CO2-to-ethanol Faradaic efficiency at 200 mA cm−2, carbon efficiency of 63%, full-cell ethanol energy efficiency of 15% (3-fold improvement over the best previous acidic CO2 reduction value) and energy cost of 260 GJ per tonne ethanol, the lowest among reported ethanol-producing CO2 electrolysers. (Figure presented.)
UR - https://www.scopus.com/pages/publications/85205561675
U2 - 10.1038/s44160-024-00662-x
DO - 10.1038/s44160-024-00662-x
M3 - Article
AN - SCOPUS:85205561675
VL - 4
SP - 75
EP - 83
JO - Nature Synthesis
JF - Nature Synthesis
IS - 1
M1 - 2101334
ER -