Optimal design of dispersive tubular reactors at steady-state using optimal control theory

被引：17

作者：

Logist, F. ^{[1
]}

Van Erdeghem, P. M. M. ^{[1
]}

Smets, I. Y. ^{[1
]}

Van Impe, J. F. ^{[1
]}

机构：

[1] Katholieke Univ Leuven, BioTeC, Dept Chem Engn, B-3001 Louvain, Belgium

来源：

JOURNAL OF PROCESS CONTROL | 2009年 / 19卷 / 07期

关键词：

Jacketed dispersive tubular reactor; Optimal temperature profiles; Pareto curves; JUMPING GENE ADAPTATIONS; HYPERBOLIC PDE SYSTEMS; DYNAMIC OPTIMIZATION; TEMPERATURE PROFILES; PREDICTIVE CONTROL; FEEDBACK-CONTROL; BATCH PROCESSES; ROBUST-CONTROL; OPERATION;

D O I：

10.1016/j.jprocont.2009.01.008

中图分类号：

TP [自动化技术、计算机技术];

学科分类号：

0812 ;

摘要：

This paper studies the design of optimal temperature profiles for a class of exothermic, jacketed dispersive tubular reactors under steady-state conditions and subject to maximum temperature constraints. The studied class ranges from perfectly mixed continuous stirred tank reactors to plug flow reactors. The aim is to derive the Pareto optimal set of temperature profiles for conflicting conversion and energy costs, while extracting generic features from the obtained solutions. Hereto, a four step procedure which is based on a weighted sum of both costs and which combines indirect, analytical and direct, numerical optimal control techniques, is employed. The generic features are studied (i) along the Pareto set by varying the weights and (ii) along the reactor class by adapting the dispersion level. (C) 2009 Elsevier Ltd. All rights reserved.

引用

页码：1191 / 1198

页数：8

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