TY - JOUR
T1 - Direct low concentration CO2 electroreduction to multicarbon products via rate-determining step tuning
AU - Xie, Liangyiqun
AU - Cai, Yanming
AU - Jiang, Yujing
AU - Shen, Meikun
AU - Lam, Jason Chun-Ho
AU - Zhu, Jun-Jie
AU - Zhu, Wenlei
PY - 2024
Y1 - 2024
N2 - Direct converting low concentration CO2 in industrial exhaust gases to high-value multi-carbon products via renewable-energy-powered electrochemical catalysis provides a sustainable strategy for CO2 utilization with minimized CO2 separation and purification capital and energy cost. Nonetheless, the electrocatalytic conversion of dilute CO2 into value-added chemicals (C2+ products, e.g., ethylene) is frequently impeded by low CO2 conversion rate and weak carbon intermediates’ surface adsorption strength. Here, we fabricate a range of Cu catalysts comprising fine-tuned Cu(111)/Cu2O(111) interface boundary density crystal structures aimed at optimizing rate-determining step and decreasing the thermodynamic barriers of intermediates’ adsorption. Utilizing interface boundary engineering, we attain a Faradaic efficiency of (51.9 ± 2.8) % and a partial current density of (34.5 ± 6.4) mA·cm−2 for C2+ products at a dilute CO2 feed condition (5% CO2 v/v), comparing to the state-of-art low concentration CO2 electrolysis. In contrast to the prevailing belief that the CO2 activation step (CO2 + e− + ∗ →*CO2−) governs the reaction rate, we discover that, under dilute CO2 feed conditions, the rate-determining step shifts to the generation of *COOH (*CO2−+ H2O → *COOH + OH−(aq)) at the Cu0/Cu1+ interface boundary, resulting in a better C2+ production performance. © The Author(s) 2024.
AB - Direct converting low concentration CO2 in industrial exhaust gases to high-value multi-carbon products via renewable-energy-powered electrochemical catalysis provides a sustainable strategy for CO2 utilization with minimized CO2 separation and purification capital and energy cost. Nonetheless, the electrocatalytic conversion of dilute CO2 into value-added chemicals (C2+ products, e.g., ethylene) is frequently impeded by low CO2 conversion rate and weak carbon intermediates’ surface adsorption strength. Here, we fabricate a range of Cu catalysts comprising fine-tuned Cu(111)/Cu2O(111) interface boundary density crystal structures aimed at optimizing rate-determining step and decreasing the thermodynamic barriers of intermediates’ adsorption. Utilizing interface boundary engineering, we attain a Faradaic efficiency of (51.9 ± 2.8) % and a partial current density of (34.5 ± 6.4) mA·cm−2 for C2+ products at a dilute CO2 feed condition (5% CO2 v/v), comparing to the state-of-art low concentration CO2 electrolysis. In contrast to the prevailing belief that the CO2 activation step (CO2 + e− + ∗ →*CO2−) governs the reaction rate, we discover that, under dilute CO2 feed conditions, the rate-determining step shifts to the generation of *COOH (*CO2−+ H2O → *COOH + OH−(aq)) at the Cu0/Cu1+ interface boundary, resulting in a better C2+ production performance. © The Author(s) 2024.
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U2 - 10.1038/s41467-024-54590-7
DO - 10.1038/s41467-024-54590-7
M3 - RGC 21 - Publication in refereed journal
C2 - 39613736
SN - 2041-1723
VL - 15
JO - Nature Communications
JF - Nature Communications
M1 - 10386
ER -