CFD and kinetic methods for mass transfer determination in a mesh microreactor

被引:25
作者
Abdallah, Radwan [1 ]
Magnico, Pierre [1 ]
Fumey, Bruno [1 ]
de Bellefon, Claude [1 ]
机构
[1] ESCPE Lyon, CNRS, Lab Genie Procedes Catalyt, F-69616 Villeurbanne, France
关键词
mass transfer; catalysis; gas-liquid-solid; microstructured reactor; CFD; hydrogenation;
D O I
10.1002/aic.10822
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The global gas-liquid-solid volumetric mass-transfer coefficient K(L)a of a catalytic multiphase microstructured film contactor, featuring 5 mu m dimensions, a 155 mu m liquid film thickness, and a 15 mu m thin catalytic layer is determined, using the very fast hydrogenation of a-methylstyrene with a Pd/gamma-alumina catalyst. The volumetric mass-transfer coefficients measured experimentally fall in the range 0.8-1.6 s(-1) above that predicted by the film model and those obtained from a CFD (3-D model) simulation, and from an analytical solution. (c) 2006 American Institute of Chemical Engineers
引用
收藏
页码:2230 / 2237
页数:8
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