Abstract
Three optimal-tuning PID controller design schemes are considered for industrial process control in this paper, which are time-domain optimal-tuning PID control, frequency-domain optimal-tuning PID control and multiobjective optimal-tuning PID control. These schemes can provide optimal PID parameters even in case where the process dynamics are time variant. They are applied to three industrial systems: a hydraulic position control system, a rotary hydraulic speed control system and a gasifier.
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