硝基苯
串联
苯胺
催化作用
化学
选择性
甲醇
组合化学
胺气处理
化学反应工程
连续流动
化学工程
甲醛
有机化学
级联反应
均相催化
流动化学
协同催化
微型反应器
工作(物理)
多相催化
酒
推流式反应器模型
反应机理
过程(计算)
作者
Junhua Zhang,Jinxin He,S K Wang,Shirui Cui,Ying Zhang,Jun Yuan,Junqi Tian,Zhongyang Liu,XC Wu,Jianian Cheng,Changxin He,Zelong Li,Can Li
摘要
ABSTRACT Integrated tandem catalysis within a continuous fixed‐bed reactor represents a promising yet underexplored strategy for process intensification in advanced amine synthesis via CO 2 utilization. Here, we demonstrate the direct conversion of nitrobenzene and CO 2 with H 2 into N‐methylaniline in a continuous fixed‐bed reactor over a CuZnZrO x catalyst, achieving 99% conversion and 95% selectivity with stable operation exceeding 100 h. Mechanistic studies identify Cu‐ZnO interfaces in the form of Cu + ‐O v ‐Zn 2‐δ serve as active sites for CO 2 hydrogenation to key intermediate formaldehyde (CH 2 O*), which couples the CO 2 hydrogenation and methylation of aniline derived from nitrobenzene hydrogenation in kinetics. The tandem configuration provides intrinsic heat‐management benefits, recovering 0.341 kg of steam (1.5 MPa, 201°C) per mole of nitrobenzene—far superior to the methanol consumption characteristic of the conventional three‐step route. This work highlights tandem catalysis as an effective reactor‐level strategy that bridges atomic‐scale active‐site engineering with kinetic synergies, advancing continuous‐flow CO 2 valorization toward higher‐value amines.
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