By International Federation of Automatic Control, Heinz Unbehauen
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Additional info for Adaptive Control of Chemical Processes 1985
The example reactor studied in this paper is operating around a steady state which is highly sensitive to upstream disturbances. The necessary specifications for MIMOSC include selection of the structure of the discrete time model, selection of measurements, control inputs, and a statement of the control objective. These specifications are inferred from basic chemical engineering knowledge of the process and from open loop responses. The parameters of the selected model structure are estimated on line and used to calculate the control gains.
L. S. Kershenbaum, and R. W. H. Sargent (1982). Theory and Application of a Robust Self-tuning Regulator. Report of Dept. of Chem. Eng. & Chem. , Imperial College. Copyright © IFAC Adaptive Control of Chemical Processes, Frankfurt am Main, 1985 ADAPTIVE CONTROL OF A RECYCLE REACTOR G. E. Bortolotto and S. Bay j0rgensen Instituttet for Kemiteknik, Danmarks Tekniske H0jskole, 2800 Lyngby, Denmark Abstract. A MIMO self tuning controller (MIMOSC) with an explicit model structure is applied to control a fixed bed chemical reactor with recirculation of unconverted reactants.
Adaptive control of Chemical Engineering Processes. IFAC Workshop on Adaptive Control, San Francisco, June 20-22. B. (1984). Multivariable adaptive identification and control of a distributed chemical reactor. Large Scale systems, ^, 323-336. Hallager, L. D. thesis (1984). Instituttet for Kemiteknik. Technical University of Denmark, Denmark. , and Hallager, L. (1985). Sparse process modelling for robust multivariable adaptive chemical process control. 7'th IFAC/IF0RS Symposium on Identification and System Parameter Estimation.
Adaptive Control of Chemical Processes 1985 by International Federation of Automatic Control, Heinz Unbehauen