Optimal Design of a Reactive Distillation Column

被引：3

作者：

Zondervan, Edwin ^{[1
]}

Shah, Mayank ^{[1
]}

de Haan, Andre B. ^{[1
]}

机构：

[1] Eindhoven Univ Technol, Dept Chem & Chem Engn, NL-5600 MB Eindhoven, Netherlands

来源：

ICHEAP-10: 10TH INTERNATIONAL CONFERENCE ON CHEMICAL AND PROCESS ENGINEERING, PTS 1-3 | 2011年 / 24卷

关键词：

Reactive distillation; Design; Optimization; MINLP;

D O I：

10.3303/CET1124050

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

In this work we develop a MINLP model that can be used to optimize the design of reactive distillation column. MINLP model is formulated in GAMS in such a way that it can be solved locally and globally. In the RD column a component A is converted into product B while vapour and liquid are assumed to be in equilibrium. The objective is to find a design for this process that minimizes the total costs (consisting of capital and operational costs). The design variables of interest are the total number of stages, the number of reactive stages, the location of the reactive stages, the feed tray location and the reflux ratio.

引用

页码：295 / 300

页数：6

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