Synthesis of n-hexyl acetate by reactive distillation

被引:45
作者
Schmitt, M
Hasse, H
Althaus, K
Schoenmakers, H
Götze, L
Moritz, P
机构
[1] Univ Stuttgart, Inst Thermodynam & Thermal Proc Engn, D-70569 Stuttgart, Germany
[2] BASF AG, Proc Engn, D-6700 Ludwigshafen, Germany
[3] Sulzer Chemtech Ltd, Winterthur, Switzerland
关键词
reactive distillation experiments; hexyl acetate; catalytic packing; scale-up; modeling and simulation;
D O I
10.1016/S0255-2701(03)00124-7
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Comprehensive studies on the n-hexyl acetate synthesis by heterogeneously catalyzed reactive distillation are presented. Reactive distillation experiments were carried out both in laboratory and semi-industrial scale with different catalytic packings. Several variants of a basic column set-up and the influence of the most important process parameters were studied. Additionally, phase and chemical equilibria and reaction kinetics were measured. Predictions from stage models of different complexity are compared to the results of experiments. It is shown, that, based on a sound knowledge on reaction kinetics and thermodynamic properties it is possible to successfully describe the studied reactive distillation process. (C) 2003 Elsevier B.V. All rights reserved.
引用
收藏
页码:397 / 409
页数:13
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