Numerical simulation of mass transfer in a liquid-liquid membrane contactor for laminar flow conditions

被引:35
作者
Kieffer, Roland [1 ]
Charcosset, Catherine [1 ]
Puel, Francois [1 ]
Mangin, Denis [1 ]
机构
[1] UCBLyon 1, CNRS, UMR 5007, Lab Automat & Genie Procedes,ESCPE Lyon, F-69622 Villeurbanne, France
关键词
computational fluid dynamics; membrane contactor; membrane reactor; micromixing; microreactor; mixing;
D O I
10.1016/j.compchemeng.2007.06.013
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
Liquid-liquid phase membrane contactors are increasingly being used for mixing and reaction. The principle is the following: component A flows through the membrane device inlet to mix/react with component B which comes from the membrane pores. This study presents a numerical simulation using computational fluid dynamics (CFD) of momentum and mass transfer in a tubular membrane contactor for laminar flow conditions. The velocity and concentration profiles of components A-C are obtained by resolution of the Navier-Stokes and convection-diffusion equations. The numerical simulations show that mixing between A and B is obtained by diffusion along the streamlines separating both components. The mixing/reaction zone width is within the region of a few hundred of microns, and depends on the diffusion coefficients of A and B. Hollow fiber membrane devices are found to be of particular interest because their inner diameter is close to the mixing zone width. (C) 2007 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1325 / 1333
页数:9
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