Practical development of a nonlinear controller for an industrial-scale batch polymerization reactor
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abstract
A batch polymerization process is described along with some examples of linear control of the process for two different batch lengths. A means of estimating on-line the heat release profile of the reactor contents, and the overall heat transfer coefficient of the reactor, is developed. A gray-box model of the polymerization proces is presented and the fit of this model to the estimated heat release and heat transfer coefficient profiles is shown. A nonlinear controller is developed based on the gray-box model and the result of using the nonlinear controller is presented.
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Proceedings of the 1997 American Control Conference (Cat. No.97CH36041)