Groupe 2. A vinyl-acetate polymerization reactor is operated at an open-loop unstable point, and has the following input
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Groupe 2. A vinyl-acetate polymerization reactor is operated at an open-loop unstable point, and has the following input
Groupe 2. A vinyl-acetate polymerization reactor is operated at an open-loop unstable point, and has the following input-output -2.5 (-10s +1)(2s +1) Design the IMC-based PID controller for this system. Implement an antiwindup control strategy for the obtained IMC-based PID Š, (s) =
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