化学
甲酸
甲苯
格式化
催化作用
二甲苯
齿合度
无机化学
动力学同位素效应
甲醇
对二甲苯
光化学
氢
间二甲苯
药物化学
同位素标记
甲酸钠
选择性
反应机理
多相催化
作者
Jiachang Zuo,Chong Liu,Bilyu Hong,Qiongjin Jiang,Zhenyu Yang,Jia Liu,Wen Zhou,Yingjie Lai,Tom Backhouse,Linmin Ye,Yongjin Luo,Wei Zhuang,Xu Han,Youzhu Yuan
标识
DOI:10.1002/anie.202524831
摘要
Abstract The industrial methanol–toluene methylation process for xylene production faces a challenge of lowering the reaction temperature while suppressing the side reaction of methanol to hydrocarbons. This depends on the low‐temperature formation of the methoxy intermediate required for methylation. Here, we establish a route for methoxy formation in which formic acid (FA) hydrogenates via a metastable monodentate formate intermediate. With the GaZrO x –ZSM‐5 catalyst, Ga–H bonds act as a “placeholder”, enabling FA adsorption as a monodentate formate rather than a stable bridged formate. At 300 °C and 3.0 MPa, toluene conversion reaches 13.9% with 77.6% xylene selectivity, outperforming established routes. Kinetic isotope effect experiments revealed that Ga‐based catalysts show a secondary isotope effect, whereas non‐Ga catalysts exhibit an inverse isotope effect. Density functional theory calculations indicated that the monodentate formate was more susceptible to hydrogenation which then facilitated methylation. This work provides a competitive route for xylene production from toluene under mild conditions using sustainable FA and H 2 .
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