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Nonlinear gain scheduled controller for a sphere liquid tank

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dc.title Nonlinear gain scheduled controller for a sphere liquid tank en
dc.contributor.author Krhovják, Adam
dc.contributor.author Dostál, Petr
dc.contributor.author Talaš, Stanislav
dc.contributor.author Rušar, Lukáš
dc.relation.ispartof Proceedings - 29th European Conference on Modelling and Simulation, ECMS 2015
dc.identifier.isbn 9780993244001
dc.date.issued 2015
dc.citation.spage 327
dc.citation.epage 332
dc.event.title 29th European Conference on Modelling and Simulation, ECMS 2015
dc.event.location Varna
utb.event.state-en Bulgaria
utb.event.state-cs Bulharsko
dc.event.sdate 2015-05-26
dc.event.edate 2015-05-29
dc.type conferenceObject
dc.language.iso en
dc.publisher European Council for Modelling and Simulation (ECMS)
dc.identifier.doi 10.7148/2015-0327
dc.relation.uri http://www.scs-europe.net/dlib/2015/2015-0327.htm
dc.relation.uri http://www.scs-europe.net/dlib/2015/ecms2015acceptedpapers/0327-mct_ECMS2015_0019.pdf
dc.subject Continuous-time model en
dc.subject Gain scheduled controller en
dc.subject Nonlinear model en
dc.subject Parametrized linear model en
dc.subject Polynomial method en
dc.subject Scheduling variable en
dc.subject Sphere liquid tank en
dc.description.abstract In this paper, we develop a gain-scheduled controller for a nonlinear plant of the sphere liquid tank. The proposed strategy is based on linearization of the nonlinear state equation around selected operating points. This methodology allows to apply any linear control design method. In particular, we discuss a polynomial method to achieve desired stability and performance requirements. Following this idea, both 1DOF and 2DOF control configurations are considered. The linear design methods are applied at each operating point in order to arrive at a set of linear control laws. Additionally, the parameters of the resulting family of linear controllers are scheduled as functions of reference variable, resulting in a single controller. Nonlocal performance of gain scheduled controller for the nonlinear model is checked by mathematical simulation. © ECMS Valeri M. Mladenov, Petia Georgieva, Grisha Spasov, Galidiya Petrova (Editors). en
utb.faculty University Institute
utb.faculty Faculty of Applied Informatics
dc.identifier.uri http://hdl.handle.net/10563/1005303
utb.identifier.obdid 43873425
utb.identifier.scopus 2-s2.0-84938723206
utb.source d-scopus
dc.date.accessioned 2015-09-09T15:16:32Z
dc.date.available 2015-09-09T15:16:32Z
utb.ou Centre of Polymer Systems
utb.contributor.internalauthor Krhovják, Adam
utb.contributor.internalauthor Dostál, Petr
utb.contributor.internalauthor Talaš, Stanislav
utb.contributor.internalauthor Rušar, Lukáš
utb.fulltext.affiliation Adam Krhovják 2, Petr Dostál 1,2, Stanislav Talaš 2, Lukáš Rušar 2 1 Centre of Polymer Systems, University Institute, Tomas Bata University in Zlín, Nad Ovčírnou 3685, 760 01 Zlín, Czech Republic. 2 Department of Process Control, Faculty of Applied Informatics, Tomas Bata University in Zlín, Nad Stráněmi 4511, 760 05 Zlín, Czech Republic {krhovjak;dostalp;talas; rusar}@fai.utb.cz
utb.fulltext.dates -
utb.fulltext.faculty Faculty of Applied Informatics
utb.fulltext.faculty University Institute
utb.fulltext.faculty Faculty of Applied Informatics
utb.fulltext.faculty Faculty of Applied Informatics
utb.fulltext.faculty Faculty of Applied Informatics
utb.fulltext.ou Department of Process Control
utb.fulltext.ou Centre of Polymer Systems
utb.fulltext.ou Department of Process Control
utb.fulltext.ou Department of Process Control
utb.fulltext.ou Department of Process Control
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