Proceedings of the 41st SICE Annual Conference. SICE 2002.
DOI: 10.1109/sice.2002.1195842
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A model driven PID control system and its application to chemical processes

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“…Alternate between incrementing GCU and GCE until there is overshoot followed by undershoot. 6. Alternate between incrementing GU and decrementing GCE until achieving the best rise time, minimum overshoot and no undershoot.…”
Section: Controllers Tuning Proceduresmentioning
confidence: 99%
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“…Alternate between incrementing GCU and GCE until there is overshoot followed by undershoot. 6. Alternate between incrementing GU and decrementing GCE until achieving the best rise time, minimum overshoot and no undershoot.…”
Section: Controllers Tuning Proceduresmentioning
confidence: 99%
“…PID is a linear-type controller and hence is only efficient for a limited operating range when used to control non-linear processes [5]. But most of the industrial processes exhibit nonlinear characteristics and inherit long dead-time such as flow, pH and temperature [5,6]. Moreover, parameters tuning is sensitive and has to be changed with changing process conditions and requires expertise in order to be tuned properly [7].…”
Section: Introductionmentioning
confidence: 99%