2017
DOI: 10.1016/j.isatra.2016.11.010
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Improved PI-PD control design using predictive functional optimization for temperature model of a fluidized catalytic cracking unit

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Cited by 23 publications
(21 citation statements)
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“…Although it has been proved by many previous researchers that the combined PFC-PID controller can keep good performance when the predictive model changes in a certain scale [22][23][24][25], it is a fact that the mismatched model would make the control performance deteriorate if the predictive model deviates far from the designed condition [37,39,46]. For the marine main engine, the load condition varies more extensively.…”
Section: Adaptive Open-loop Gain Associated Mmpfc-pid Controllermentioning
confidence: 99%
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“…Although it has been proved by many previous researchers that the combined PFC-PID controller can keep good performance when the predictive model changes in a certain scale [22][23][24][25], it is a fact that the mismatched model would make the control performance deteriorate if the predictive model deviates far from the designed condition [37,39,46]. For the marine main engine, the load condition varies more extensively.…”
Section: Adaptive Open-loop Gain Associated Mmpfc-pid Controllermentioning
confidence: 99%
“…They were also never illustrated in the similar applications in other different fields [22][23][24][25]27]. …”
Section: Speed Tracking Performance Undermentioning
confidence: 99%
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“…As stated previously, although PID controllers are frequently used in process control applications, they are suitable for small time delay systems [30]. Nonlinearities, uncertainties, and large time delays exist widely in industrial processes, which leads to great difficulty in classical PID control [31].…”
Section: Introductionmentioning
confidence: 99%
“…Nonlinearities, uncertainties, and large time delays exist widely in industrial processes, which leads to great difficulty in classical PID control [31]. Thus, when systems with time delays that are too large are encountered, the PID controller may not provide the desired performance specifications [30]. In addition, it is well known that getting good closed-loop step responses with a PID controller for processes having integrators and unstable poles is difficult [32].…”
Section: Introductionmentioning
confidence: 99%