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Mesostructure‐Specific Configuration of *CO Adsorption for Selective CO<sub>2</sub> Electroreduction to C<sub>2+</sub> Products

Zaiqi Li, Bin Sun, Difei Xiao, Hongli Liu, Zeyan Wang, Yuanyuan Liu, Zhaoke Zheng, Peng Wang, Ying Dai, Baibiao Huang, Baibiao Huang, Hefeng Cheng

2024Angewandte Chemie International Edition33 citationsDOI

Abstract

Abstract The multi‐carbon (C 2+ ) alcohols produced by electrochemical CO 2 reduction, such as ethanol and n ‐propanol, are considered as indispensable liquid energy carriers. In most C−C coupling cases, however, the concomitant gaseous C 2 H 4 product results in the low selectivity of C 2+ alcohols. Here, we report rational construction of mesostructured CuO electrocatalysts, specifically mesoporous CuO (m‐CuO) and cylindrical CuO (c‐CuO), enables selective distribution of C 2+ products. The m‐CuO and c‐CuO show similar selectivity towards total C 2+ products (≥76 %), but the corresponding predominant products are C 2+ alcohols (55 %) and C 2 H 4 (52 %), respectively. The ordered mesostructure not only induces the surface hydrophobicity, but selectively tailors the adsorption configuration of *CO intermediate: m‐CuO prefers bridged adsorption, whereas c‐CuO favors top adsorption as revealed by in situ spectroscopies. Computational calculations unravel that bridged *CO adsorbate is prone to deep protonation into *OCH 3 intermediate, thus accelerating the coupling of *CO and *OCH 3 intermediates to generate C 2+ alcohols; by contrast, top *CO adsorbate is apt to undergo conventional C−C coupling process to produce C 2 H 4 . This work illustrates selective C 2+ products distribution via mesostructure manipulation, and paves a new path into the design of efficient electrocatalysts with tunable adsorption configuration of key intermediates for targeted products.

Topics & Concepts

AdsorptionChemistryMaterials scienceChemical engineeringCombinatorial chemistryPhysical chemistryEngineeringCO2 Reduction Techniques and CatalystsIonic liquids properties and applicationsCarbon dioxide utilization in catalysis