Robust model predictive control of a pilot plant distillation column

被引：25

作者：

Martin, Paulo A. ^{[1
]}

Odloak, Darci ^{[2
]}

Kassab, Fuad ^{[3
]}

机构：

[1] Maua Sch Engn, BR-01095307 Praca Maua, Sao Caetano Do, Brazil

[2] Univ Sao Paulo, Dept Chem Engn, BR-05508900 Sao Paulo, Brazil

[3] Univ Sao Paulo, Dept Elect Engn, BR-05508900 Sao Paulo, Brazil

来源：

CONTROL ENGINEERING PRACTICE | 2013年 / 21卷 / 03期

关键词：

Distillation column; Model predictive control; Multi-model systems; Robust stability; Process control; MPC;

D O I：

10.1016/j.conengprac.2012.10.004

中图分类号：

TP [自动化技术、计算机技术];

学科分类号：

0812 ;

摘要：

In this paper, the development and application of a robust MPC to a pilot plant ethanol-water distillation column is described. It is shown through experimental tests in the pilot plant, how the linear model can change depending on the operating point. The obtained model has time delays and repeated poles. For this kind of system, the development of an MPC, based on the step response model that is robust to multi-model uncertainty, is presented. The experimental results that confirm the good performance of the proposed controller are also shown. (C) 2012 Elsevier Ltd. All rights reserved.

引用

页码：231 / 241

页数：11

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