微型反应器
硝化作用
间歇式反应器
苯甲醛
产量(工程)
批处理
化学
连续反应器
流动化学
过程(计算)
同种类的
工艺工程
化学工程
材料科学
有机化学
计算机科学
催化作用
热力学
工程类
物理
操作系统
冶金
程序设计语言
作者
Danilo Russo,Giovanna Tomaiuolo,Roberto Andreozzi,Stefano Guido,Alexei A. Lapkin,Ilaria Di Somma
标识
DOI:10.1016/j.cej.2018.11.044
摘要
Ortho- and meta-nitrobenzaldehydes are two important intermediates in the chemical industry. They are the main products of benzaldehyde nitration by mixed acid, which is a hazardous chemical process since reaction rates are very sensitive to variations of the operating conditions. In the present investigation, a previously developed kinetic model under homogeneous conditions is validated and extended for heterogeneous liquid-liquid systems. A comparison between performances of a lab-scale batch reactor and a commercial microreactor is also presented. The results show that microreactors with embedded static mixer can outperform scaled-up batch reactors, achieving the theoretical limit of conversion/yield attainable under kinetic control.
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