A concept for multi-scale modeling of bubble columns and loop reactors

被引:57
作者
Bauer, M [1 ]
Eigenberger, G [1 ]
机构
[1] Univ Stuttgart, Inst Chem Verfahrenstech, D-70199 Stuttgart, Germany
关键词
modeling; bubble column; multi-scale modeling; reaction; bubble size; simplified hydrodynamics;
D O I
10.1016/S0009-2509(99)00264-X
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A concept for an iterative multi-scale modeling and simulation of gas/liquid bubble column reactors with or without recycle has been developed and discussed for a specific example. It is based upon the interplay of the two-phase mass transfer and reaction with the detailed (unsteady state) hydrodynamics. A "zone model" contains one-dimensional mass balances for the gas and the liquid phase and balance equations which are necessary to describe the change of the mean bubble diameter of the bubble size distribution. Energy balances can also be added. Detailed information of the liquid and gas flow pattern is provided to the zone model by the hydrodynamic model, while the hydrodynamic model gets its required information about local mean bubble sizes and the local mass flux between gas and liquid from the zone model. (C) 1999 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:5109 / 5117
页数:9
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