DocumentCode
1962083
Title
Adaptive generalized predictive control and model reference adaptive control for CSTR Reactor
Author
Delbari, Mahboobeh ; Salahshoor, Karim ; Moshiri, Behzad
Author_Institution
South Tehran Branch, Islamic Azad Univ., Tehran, Iran
fYear
2010
fDate
13-15 Aug. 2010
Firstpage
165
Lastpage
169
Abstract
Large numbers of industrial chemical process have nonlinear and time varying behavior, so to achieve good control properties it´s necessary to use a powerful identification method that can track these variations properly. In this paper, an on- line recursive least square identification method based on ARX is used to have good knowledge about dynamic behavior of system, then for control goals two adaptive method is present: indirect adaptive control based pole placement and adaptive general predict control(GPC). The advantages of the methodologies are demonstrated on nonlinear Continuous Stirred Tank Reactor (CSTR) simulations. desired control properties is reached with a good parameter estimation and achieved results show the successful identifications and control methodologies. Result of two control strategy are compared together and advantages of Adaptive GPC is shown for time varying systems like CSTR.
Keywords
autoregressive processes; chemical reactors; least squares approximations; model reference adaptive control systems; nonlinear control systems; pole assignment; predictive control; process control; recursive estimation; time-varying systems; ARX; CSTR reactor; CSTR simulations; GPC; adaptive general predict control; adaptive generalized predictive control; control methodology; control property; dynamic system behavior; indirect adaptive control based pole placement; industrial chemical process; model reference adaptive control; nonlinear continuous stirred tank reactor simulations; nonlinear varying behavior; online recursive least square identification method; parameter estimation; powerful identification method; time varying behavior; time varying systems; Adaptation model; Adaptive control; Chemical reactors; Inductors; Mathematical model; Parameter estimation; Process control;
fLanguage
English
Publisher
ieee
Conference_Titel
Intelligent Control and Information Processing (ICICIP), 2010 International Conference on
Conference_Location
Dalian
Print_ISBN
978-1-4244-7047-1
Type
conf
DOI
10.1109/ICICIP.2010.5565238
Filename
5565238
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