Reactive and catalytic distillation from an industrial perspective

被引:54
作者
Schoenmakers, HG [1 ]
Bessling, B
机构
[1] BASF AG, Dept ZAT, Proc Engn, D-67056 Ludwigshafen, Germany
[2] BASF Corp, Dept NP R, Wyandotte, MI USA
关键词
distillation; validation; reactive distillation; simulation; methyl acetate;
D O I
10.1016/S0255-2701(02)00085-5
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
Reactive and catalytic distillation has attracted growing interest, both in industry and in scientific research. This contribution gives an overview will of the tools that are available today and the methods that have now been introduced into the industrial practice in a large chemical company. A process synthesis gives good qualitative reference points. Simulation tools have been developed which are mainly equilibrium-based. However, further steps are necessary on the way to implementation in an industrial plant. The scale-up from the miniplant used for the experimental validation of a new process is well known for conventional distillation, but complicated by several facts for reactive distillation specifically in the case of heterogeneous catalysis. To overcome these problems reference plant experience on an industrial scale is necessary or-if not available-will require future research. Other options both for homogeneous and heterogeneous catalysis are possible and will be discussed in the contribution. Attention is drawn to the fact that a combination of reaction and distillation does not necessarily have to be operated in a column. For slower reactions a broad range of equipment not necessarily containing columns can be used. (C) 2003 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:145 / 155
页数:11
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