A membrane reactor intensifying micromixing: Effects of parameters on segregation index

被引：20

作者：

Jia, ZQ ^{[1
]}

Zhao, YQ

Liu, LQ

He, F

Liu, ZZ

机构：

[1] Beijing Normal Univ, Dept Chem, Beijing 100875, Peoples R China

[2] Chinese Acad Sci, Res Ctr Ecoenvironm Sci, Beijing, Peoples R China

来源：

JOURNAL OF MEMBRANE SCIENCE | 2006年 / 276卷 / 1-2期

基金：

中国国家自然科学基金;

关键词：

micromixing; membrane reactor; segregation index; controlled addition;

D O I：

10.1016/j.memsci.2005.10.003

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

In this paper, the micromixing efficiency in a membrane reactor was studied by employing competing parallel reactions. In the membrane reactor, one liquid is added gradually into another one through the nano-scaled micropores of ultrafiltration membranes. The effects of molecular weight cut-off (MWCO) of membranes, permeation fluxes, Reynolds number and reactants concentrations on the segregation index:were investigated. The results show that the decreasing membranes MWCO and the increasing Reynolds number favor the enhancement of micromixing efficiency. Compared with the other reactors (e.g. stirring tank, ultrasound, static mixer, Coutte flow reactor), the membrane reactor exhibits more excellent effects in intensifying micromixing. (c) 2005 Elsevier B.V. All rights reserved.

引用

页码：295 / 300

页数：6

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