DocumentCode
490505
Title
The Use of Approximate Models and Exact Linearization for Control of Nonlinear Processes
Author
Ouarti, H. ; Edgar, T.F.
Author_Institution
Department of Chemical Engineering, The University of Texas at Austin, Austin, Texas 78712
fYear
1993
fDate
2-4 June 1993
Firstpage
2268
Lastpage
2273
Abstract
Nonlinear control techniques such as global linearization can be advantageous, especially when process characteristics vary with the operating point. Differential geometric control techniques exactly linearize nonlinear systems so that linear feedback control can be applied. However, this requires that a nonlinear model of the process be available. This paper focuses on developing an empirical input-linear model for nonlinear processes by approximating transformations. As a simplification, we assume that process nonlinearities are essentially imbedded in the steady state relationships and steady-state input-output gains can be fitted by algebraic equations. This type of model can be linearized exactly using input-output transformations, leading to a simple control law based on linear system theory. Three linearization methods are proposed in this paper and compared to the previously developed Hammerstein and Wiener series compensation techniques, using a simulation model of a heat exchanger.
Keywords
Chemical processes; Control nonlinearities; Feedback control; Linear feedback control systems; Linear systems; Nonlinear control systems; Nonlinear systems; Process control; Solid modeling; Steady-state;
fLanguage
English
Publisher
ieee
Conference_Titel
American Control Conference, 1993
Conference_Location
San Francisco, CA, USA
Print_ISBN
0-7803-0860-3
Type
conf
Filename
4793290
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