微型反应器
塞流
丙烯腈
推流式反应器模型
丙酮
连续反应器
化学
间歇式反应器
动能
动力学
停留时间(流体动力学)
化学工程
热力学
连续搅拌釜式反应器
催化作用
物理化学
有机化学
聚合物
共聚物
量子力学
岩土工程
工程类
物理
作者
Hui‐Long Wei,Xi‐Bao Zhang,Zheng‐Hong Luo
标识
DOI:10.1021/acs.iecr.2c02917
摘要
Synthesis experiments of 5-oxohexanenitrile through the addition of acetone to acrylonitrile at the temperature range of 200–230 °C were carried out in a microreactor. Based on the experimental data, a semiempirical kinetic model was established and validated. According to the developed kinetic model, the effects of the molar ratio of acetone to acrylonitrile, the concentration of N-propylamine, and the initial water content were further investigated. By coupling the semiempirical kinetics with the plug flow reactor model, studies on the effect of the reactor diameter, the residence time, and the reaction temperature were performed to shed some light on the design and optimization of the industrial tubular reactors for the production of 5-oxohexanenitrile.
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