Process Control and Optimization Consortium

 Updated: 06/27/05 06:19 PM     

 

 Multiple Model Adaptive Control Design for a MIMO Chemical Reactor

Authors:

Ramakrishnan Gundala¹ and Karlene A. Hoo*
¹Department of Chemical Engineering, University of South Carolina
*Department of Chemical Engineering, Texas Tech University

ABSTRACT

Multiple adaptive and nonadaptive models are used to represent the behavior of processes that are known to transition to unknown regimes in the operating space. The adaptive models investigated are of two types, free-running and re-initializable, that differ in the initialization of their parameters. Using these models and their companion controllers in a model reference adaptive structure, it is shown that this mixed model set can provide satisfactory control of a nonlinear, interactive, multiple-input multiple-output chemical reactor with active constraints.

Publication Information: Download Manuscript - PDF format
Industrial & Engineering Chemistry Research, Vol. 39, pp 1554-1563, 2000.
Corresponding Author:    Karlene A. Hoo

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