Control of a Multivariable System Using Optimal Control Pairs: A Quadruple-Tank Process

This paper deals with one of the possible ways to control multivariable (MIMO) control loops. The suggested control design procedure uses the so-called primary controllers, auxiliary controllers, and also correction members. Parameters of the primary controllers are determined for the optimal contro...

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Main Authors: Pavel Navratil, Libor Pekar, Radek Matusu
Format: Article
Language:English
Published: IEEE 2020-01-01
Series:IEEE Access
Subjects:
Online Access:https://ieeexplore.ieee.org/document/8945360/
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spelling doaj-664dd8d318534c6a8b0123b46b061abd2021-03-30T01:10:35ZengIEEEIEEE Access2169-35362020-01-0182537256310.1109/ACCESS.2019.29623028945360Control of a Multivariable System Using Optimal Control Pairs: A Quadruple-Tank ProcessPavel Navratil0Libor Pekar1https://orcid.org/0000-0002-2401-5886Radek Matusu2https://orcid.org/0000-0002-5242-7781Department of Automation and Control Engineering, Faculty of Applied Informatics, Tomas Bata University in Zlín, Zlín, Czech RepublicDepartment of Automation and Control Engineering, Faculty of Applied Informatics, Tomas Bata University in Zlín, Zlín, Czech RepublicDepartment of Automation and Control Engineering, Faculty of Applied Informatics, Tomas Bata University in Zlín, Zlín, Czech RepublicThis paper deals with one of the possible ways to control multivariable (MIMO) control loops. The suggested control design procedure uses the so-called primary controllers, auxiliary controllers, and also correction members. Parameters of the primary controllers are determined for the optimal control pairs using arbitrary single-variable synthesis methods; namely, the modulus optimum method, the balanced tuning method, and the desired model method. The optimal control pairs are determined using the so-called relative gain array tool or the relative normalized gain array tool combined with other tools, as the condition number or the Niederlinski index. The auxiliary feedback controllers serve for ensuring a control loop decoupling. Invariance to load disturbance of a control loop is realized by using the correction members. The novelty lies especially in the combination of the original inverted decoupling with disturbance rejection and provided tuning methods. The proposed control design for a MIMO loop is verified by simulation for the two-variable controlled plant of a quadruple-tank process and evaluated by using various criteria. Moreover, a numerical comparison to some other methods is given to the reader.https://ieeexplore.ieee.org/document/8945360/Control loop decoupling and invariancemultivariable controloptimal control pairsquadruple-tank processsimulation
collection DOAJ
language English
format Article
sources DOAJ
author Pavel Navratil
Libor Pekar
Radek Matusu
spellingShingle Pavel Navratil
Libor Pekar
Radek Matusu
Control of a Multivariable System Using Optimal Control Pairs: A Quadruple-Tank Process
IEEE Access
Control loop decoupling and invariance
multivariable control
optimal control pairs
quadruple-tank process
simulation
author_facet Pavel Navratil
Libor Pekar
Radek Matusu
author_sort Pavel Navratil
title Control of a Multivariable System Using Optimal Control Pairs: A Quadruple-Tank Process
title_short Control of a Multivariable System Using Optimal Control Pairs: A Quadruple-Tank Process
title_full Control of a Multivariable System Using Optimal Control Pairs: A Quadruple-Tank Process
title_fullStr Control of a Multivariable System Using Optimal Control Pairs: A Quadruple-Tank Process
title_full_unstemmed Control of a Multivariable System Using Optimal Control Pairs: A Quadruple-Tank Process
title_sort control of a multivariable system using optimal control pairs: a quadruple-tank process
publisher IEEE
series IEEE Access
issn 2169-3536
publishDate 2020-01-01
description This paper deals with one of the possible ways to control multivariable (MIMO) control loops. The suggested control design procedure uses the so-called primary controllers, auxiliary controllers, and also correction members. Parameters of the primary controllers are determined for the optimal control pairs using arbitrary single-variable synthesis methods; namely, the modulus optimum method, the balanced tuning method, and the desired model method. The optimal control pairs are determined using the so-called relative gain array tool or the relative normalized gain array tool combined with other tools, as the condition number or the Niederlinski index. The auxiliary feedback controllers serve for ensuring a control loop decoupling. Invariance to load disturbance of a control loop is realized by using the correction members. The novelty lies especially in the combination of the original inverted decoupling with disturbance rejection and provided tuning methods. The proposed control design for a MIMO loop is verified by simulation for the two-variable controlled plant of a quadruple-tank process and evaluated by using various criteria. Moreover, a numerical comparison to some other methods is given to the reader.
topic Control loop decoupling and invariance
multivariable control
optimal control pairs
quadruple-tank process
simulation
url https://ieeexplore.ieee.org/document/8945360/
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AT radekmatusu controlofamultivariablesystemusingoptimalcontrolpairsaquadrupletankprocess
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