Time optimal start-up strategies for reactive distillation columns

被引:42
|
作者
Reepmeyer, F [1 ]
Repke, JU [1 ]
Wozny, G [1 ]
机构
[1] Tech Univ Berlin, Dept Proc Dynam & Operat, D-10623 Berlin, Germany
关键词
reactive distillation; start-up; dynamic simulation; ethyl acetate; transesterification;
D O I
10.1016/j.ces.2004.06.029
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this contribution, a rigorous process model to simulate the start-up of a cold and empty reactive distillation (RD) column is developed and experimentally validated with a transesterification process. Strategies for time optimal start-up of an RD column are presented. The mostly used strategy for conventional distillation of total reflux for RD is only recommendable with limitations. New, alternative strategies, like the recycling of the off-spec bottom and top product or the initial charging with product, to minimize the necessary start-up time are presented. Suitable strategies can save up to 82% of the needed time for the column start-up. (C) 2004 Elsevier Ltd. All rights reserved.
引用
收藏
页码:4339 / 4347
页数:9
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