催化作用
甲醛
产量(工程)
化学
选择性
密度泛函理论
化学工程
氧气
动能
过程(计算)
活化能
电荷密度
电荷(物理)
无机化学
多相催化
有机化学
作者
Rui Wang,Guihua Yang,Wanting Li,Siyu Nie,Wei Zhang,Bingbing Gong
摘要
Abstract The synthesis of 1,4‐butynediol via formaldehyde ethynylation is a process of considerable industrial importance. Herein, Cu‐Bi catalysts were synthesized via a co‐precipitation method. The optimized Cu‐Bi catalyst with 10 wt% Bi loading (denoted as CuO/10Bi 2 O 3 ) delivered outstanding performance, providing a 1,4‐butynediol yield of 74% at 94% selectivity. Remarkably, it maintained a 60% yield with 94% selectivity after 100 h of continuous operation, demonstrating stability on par with that of the commercial RK catalyst. Kinetic studies determined an activation energy of only 28.64 kJ/mol for CuO/10Bi 2 O 3 , significantly lower than the 64.88 kJ/mol measured for the RK catalyst. Furthermore, combined structural characterizations, density functional theory calculations, and Bader charge analyses reveal that the Cu‐Bi electronic synergy and abundant oxygen vacancies in CuO/10Bi 2 O 3 stabilize Cu + sites, suppress their over‐reduction, and further stabilize the Cu 2 C 2 active center, ultimately endowing the catalyst with high activity and long lifetime.
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