Transport modelling of packed-tube reactors - IV: Steady-state modelling with intraparticle gradients

被引:0
|
作者
Kasab, JJ [1 ]
Mehta, S [1 ]
Stewart, WE [1 ]
机构
[1] Univ Wisconsin, Dept Chem Engn, Madison, WI 53706 USA
基金
美国国家科学基金会;
关键词
modelling; multiphase reactors; numerical analysis; packed bed; simulation;
D O I
10.1016/S0009-2509(00)00188-3
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A data-based model of surface states in packed tubes is joined with an intraparticle diffusion-reaction model to describe reactors with significant intraparticle gradients. This modelling approach is demonstrated with steady-state simulations of the partial oxidation of n-butane to maleic anhydride in a packed-tube reactor with spherical particles and a tube/particle diameter ratio of 2.02. The simulation is based on a correlation of heat transport experiments performed in a unique packed-tube gas flow apparatus, and on a kinetic model taken from the literature. An orthogonal collocation scheme, using rounded Hahn polynomial zeros as axial nodes and Jacobi zeros as intraparticle nodes, allows efficient solution of the resulting detailed reactor model. (C) 2000 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:5783 / 5792
页数:10
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