2018
DOI: 10.1504/ijris.2018.096204
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Real time implementation of multivariable centralised FOPID controller for TITO process

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Cited by 4 publications
(9 citation statements)
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“…Further, the tracking performance and robustness studies are conducted for uncertain parametric conditions. The following interacting tank systems are considered: (i) coupled conical tank system (CCTS) [ 41 ], (ii) coupled spherical tank system (CSTS) [ 29 ] and (iii) quadruple tank system (QTS) [ 42 ]. As presented in [ 43 ], the ideal range for gain and phase margin are between 2–5 and 30–60 respectively.…”
Section: Resultsmentioning
confidence: 99%
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“…Further, the tracking performance and robustness studies are conducted for uncertain parametric conditions. The following interacting tank systems are considered: (i) coupled conical tank system (CCTS) [ 41 ], (ii) coupled spherical tank system (CSTS) [ 29 ] and (iii) quadruple tank system (QTS) [ 42 ]. As presented in [ 43 ], the ideal range for gain and phase margin are between 2–5 and 30–60 respectively.…”
Section: Resultsmentioning
confidence: 99%
“…As reported in [ 41 ], the height of the tank is 50 cm, and the tank is operated around 20–25 cm by regulating the input flow rate. The TITO FOPDT process model is obtained at the operating points = 24.5 cm, = 25.6 cm.…”
Section: Resultsmentioning
confidence: 99%
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“…The original non-linear model of the system, as described in Ref. 53, presents a comprehensive understanding of the system dynamics under standard operating conditions. Figure 9 provides a comparative analysis between the original system in Ref.…”
Section: Coupled Conical Tank Systemmentioning
confidence: 99%
“…Figure 9 provides a comparative analysis between the original system in Ref. 53 and the reduced FOPDT models in Equations ( 47) and (48). The reduced FOPDT model was able to capture the system behavior.…”
Section: Coupled Conical Tank Systemmentioning
confidence: 99%