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Adaptive control of nonlinear processes: Continuous-time versus delta model parameter estimation

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dc.title Adaptive control of nonlinear processes: Continuous-time versus delta model parameter estimation en
dc.contributor.author Dostál, Petr
dc.contributor.author Bobál, Vladimír
dc.contributor.author Gazdoš, František
dc.relation.ispartof IFAC Proceedings Volumes (IFAC-PapersOnline)
dc.identifier.issn 1474-6670 Scopus Sources, Sherpa/RoMEO, JCR
dc.date.issued 2004
utb.relation.volume 37
utb.relation.issue 12
dc.citation.spage 273
dc.citation.epage 278
dc.event.title 2004 IFAC Workshop on Adaptation and Learning in Control and Signal Processing, ALCOSP 2004 and IFAC Workshop on Periodic Control Systems, PSYCO 2004
dc.event.location Yokohama
utb.event.state-en Japan
utb.event.state-cs Japonsko
dc.event.sdate 2004-08-30
dc.event.edate 2004-09-01
dc.type conferenceObject
dc.language.iso en
dc.publisher International Federation of Automatic Control (IFAC)
dc.identifier.doi 10.1016/S1474-6670(17)31480-5
dc.relation.uri https://www.sciencedirect.com/science/article/pii/S1474667017314805
dc.subject Adaptive control en
dc.subject Continuous-time model en
dc.subject Delta model en
dc.subject Parameter estimation en
dc.subject Polynomial method en
dc.description.abstract The paper deals with continous-time adaptive control of nonlinear processes. A nonlinear model of the process is approximated by a continuous-time external linear model. the parameters of the CT external linear model of the process are estimated in two ways. In the first case, direct estimation of the CT model is used. In the second case, the parameters of a corresponding delta model are recursively estimated. the 2DOF control system configuration is considered. the controller design is based on the polynomial approach. the resulting proper controller ensures stability of the control system as well as asymptotic tracking of the step reference and step load disturbance attenuation. the adaptive control is tested on the nonlinear system represented by a model of two spheric liquid tanks in series. Copyright © 2004 IFAC en
utb.faculty Faculty of Technology
dc.identifier.uri http://hdl.handle.net/10563/1008636
utb.identifier.rivid RIV/70883521:28110/04:63502302!RIV05-GA0-28110___
utb.identifier.obdid 12052656
utb.identifier.scopus 2-s2.0-85014885319
utb.source d-scopus
dc.date.accessioned 2019-07-08T11:59:59Z
dc.date.available 2019-07-08T11:59:59Z
utb.contributor.internalauthor Dostál, Petr
utb.contributor.internalauthor Bobál, Vladimír
utb.contributor.internalauthor Gazdoš, František
utb.fulltext.affiliation Petr Dostál, Vladimír Bobál, František Gazdoš Department of Process Control, Faculty of Technology, Tomas Bata University in Zlín, Nám. T. G. Masaryka 275, 762 72 Zlín Czech Republic Phone: +420 57 6033217; Fax: +420 57 6033333; E-mail: [email protected]
utb.fulltext.dates -
utb.scopus.affiliation Department of Process Control, Faculty of Technology, Tomas Bata University in Zlín, Nám. T. G. Masaryka 275, Zlín, 762 72, Czech Republic
utb.fulltext.faculty Faculty of Technology
utb.fulltext.faculty Faculty of Technology
utb.fulltext.faculty Faculty of Technology
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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