SIMULATION OF ADAPTIVE CONTROL OF A TUBULAR CHEMICAL REACTOR

被引：1

作者：

Dostal, Petr ^{[1
]}

Vojtesek, Jiri ^{[1
]}

Bobal, Vladimir ^{[1
]}

机构：

[1] Tomas Bata Univ Zlin, Ctr Polymer Syst, Dept Proc Control, Nam TG Masaryka 5555, Zlin 76001, Czech Republic

来源：

PROCEEDINGS 26TH EUROPEAN CONFERENCE ON MODELLING AND SIMULATION ECMS 2012 | 2012年

关键词：

Tubular chemical reactor; Nonlinear model; External linear model; Parameter identification; Polynomial approach; Pole assignment;

D O I：

10.7148/2012-0419-0425

中图分类号：

TP [自动化技术、计算机技术];

学科分类号：

0812 ;

摘要：

The paper deals with continuous-time adaptive control of a tubular chemical reactor with the countercurrent cooling as a nonlinear single input - single output process. The nonlinear model of the reactor is approximated by an external linear model with parameters estimated via corresponding delta model. The control system structure with two feedback controllers is considered. The resulting controllers are derived using the polynomial approach. The method is tested on a mathematical model of the tubular chemical reactor.

引用

页码：419 / +

页数：2

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