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Ammoximation of Cyclohexanone to Cyclohexanone Oxime Catalyzed by Titanium Silicalite-I Zeolite in Three-phase System

机译:钛硅沸石-I型沸石三相体系催化环己酮氨化为环己酮肟

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摘要

An innovative green process of producing ε-caprolactam was proposed by integrating ammoximation and Beckmann rearrangement effectively. As a first part of the new process, TS-1 molecular sieve-catalyzed synthesis of cyclohexanone oxime from cyclohexanone, ammonia and hydrogen peroxide was carried out in a batch plant. Cyclohexane was used as the solvent in the three-phase reaction system. The influences of essential process parameters on ammoximation were investigated. Under the reaction conditions as catalyst content of 2.5% (by mass); H 2 O 2 /yclohexanone molar ratio of 1.10; NH 3 /cyclohexanone molar ratio of 2.20; reaction temperature of 343 K; reaction time of 5 h, high conversion of cyclohexanone and selectivity to oxime (both〉99%) were obtained. Thus, the three-phase ammoximation process showed equal catalytic activity as TS-1 but much more convenient and simpler for the separation of catalyst in comparison to the industrial two-phase system with t-butanol used as solvent.
机译:通过有效结合氨肟化和贝克曼重排,提出了一种创新的绿色生产ε-己内酰胺的方法。作为新工艺的第一部分,在间歇式工厂中,由环己酮,氨和过氧化氢进行TS-1分子筛催化合成环己酮肟。在三相反应体系中,使用环己烷作为溶剂。研究了基本工艺参数对氨氧化反应的影响。在反应条件下作为催化剂的含量为2.5%(质量); H 2 O 2 /环己酮摩尔比为1.10; NH 3 /环己酮的摩尔比为2.20;反应温度为343K;反应时间为5小时,环己酮的转化率高,对肟的选择性(均> 99%)。因此,与使用叔丁醇作为溶剂的工业两相系统相比,三相氨化过程显示出与TS-1相同的催化活性,但分离催化剂更加方便和简单。

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