Micro-mixing in chemical reactors: A perspective

被引:48
作者
Mao, Zaisha [1 ]
Yang, Chao
机构
[1] Chinese Acad Sci, Inst Proc Engn, Key Lab Green Proc & Engn, Beijing 100190, Peoples R China
基金
中国国家自然科学基金;
关键词
Chemical reactor; Mixing; Micro-mixing; Micro-mixing model; Numerical simulation; BARIUM-SULFATE PRECIPITATION; STIRRED-TANK REACTORS; NUMERICAL-SIMULATION; TURBULENT PRECIPITATION; IODIDE-IODATE; MODEL; CFD; COMPLEX;
D O I
10.1016/j.cjche.2016.09.012
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Micro-mixing is an important mechanism, which works simultaneously with macro-mixing in chemical reactors in process industries, for achieving the best selectivity with respect to desired products. In about a half century, a huge amount of data and knowledge has been accumulated from theoretical and experimental studies on micro-mixing. Nevertheless, those results are mostly composites of simplified theoretical and empirical models, and the true nature of interactions of flow inhomogeneity and micro-mixing with chemical reaction has not been fully unveiled. This article reviews the progress in micro-mixing study in chemical reactors to date. A few important topics related to the nature, experimental evaluation, and numerical simulation of micro-mixing are addressed. Some suggestions are given hopefully to motivate more chemical engineers to devote their efforts to better understanding of micro-mixing in chemical reactors. (C) 2016 The Chemical Industry and Engineering Society of China, and Chemical Industry Press. All rights reserved.
引用
收藏
页码:381 / 390
页数:10
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