2018 IEEE International Conference on Automation/Xxiii Congress of the Chilean Association of Automatic Control (ICA-ACCA) 2018
DOI: 10.1109/ica-acca.2018.8609727
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Improving the control energy use for first order plus time delay plants with fractional proportional integral controllers: a preliminary analysis

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Cited by 5 publications
(4 citation statements)
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“…The work of the closed-loop control system based on the proposed combined PID/PI/I controller ( Figure 2 ) was analysed with the plants, the dynamics of which are described by the first-order plus dead-time (FOPDT) transfer function. Such a model of the plant was chosen because it describes the dynamics of many real industrial processes [ 32 , 33 , 34 , 35 , 36 , 37 ]. The response delay (dead-time) values were chosen based on the literature [ 32 , 33 , 34 , 35 , 36 , 37 ], as well as from the practice of application of control systems.…”
Section: Combined Pid/pi/i Controllermentioning
confidence: 99%
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“…The work of the closed-loop control system based on the proposed combined PID/PI/I controller ( Figure 2 ) was analysed with the plants, the dynamics of which are described by the first-order plus dead-time (FOPDT) transfer function. Such a model of the plant was chosen because it describes the dynamics of many real industrial processes [ 32 , 33 , 34 , 35 , 36 , 37 ]. The response delay (dead-time) values were chosen based on the literature [ 32 , 33 , 34 , 35 , 36 , 37 ], as well as from the practice of application of control systems.…”
Section: Combined Pid/pi/i Controllermentioning
confidence: 99%
“…Such a model of the plant was chosen because it describes the dynamics of many real industrial processes [ 32 , 33 , 34 , 35 , 36 , 37 ]. The response delay (dead-time) values were chosen based on the literature [ 32 , 33 , 34 , 35 , 36 , 37 ], as well as from the practice of application of control systems. For example, the water supply systems for which this controller was developed had such response delay values, and their dynamics corresponded to the FOPDT transfer function.…”
Section: Combined Pid/pi/i Controllermentioning
confidence: 99%
See 1 more Smart Citation
“…To demonstrate this, the simulation of the set-point unit-pulse and unit-load-disturbance response of the control system based on the PI controller with the classical Smith predictor of the plants described by the first- and second-order transfer functions with the asymmetric response delay was performed. Such plants were chosen for analysis because the dynamics of many real controlled plants can be described by the first- or second-order transfer function plus the response delay [ 26 , 27 , 28 , 29 , 30 ]. The obtained results are presented in Figure 4 and Figure 5 .…”
Section: Problem Formulationmentioning
confidence: 99%