About: Simulation of nonlinear adaptive control of a tubular chemical reactor

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rdf:type	skos:Concept http://linked.opendata.cz/ontology/domain/vavai/Vysledek
Description	The paper deals with continuous-time adaptive control of a tubular chemical reactor with the countercurrent cooling as a nonlinear single input – single output process. The mean reactant temperature and the output reactant temperature are chosen as the controlled outputs, and, the coolant flow rate as the control input. The nonlinear model of the reactor is approximated by an external linear model with a structure chosen on the basis of controlled outputs step responses. Its parameters are estimated via corresponding delta model. The control system structure with two feedback controllers is considered. The resulting controllers are derived using polynomial approach. The method is tested on a mathematical model of the tubular chemical reactor. The paper deals with continuous-time adaptive control of a tubular chemical reactor with the countercurrent cooling as a nonlinear single input – single output process. The mean reactant temperature and the output reactant temperature are chosen as the controlled outputs, and, the coolant flow rate as the control input. The nonlinear model of the reactor is approximated by an external linear model with a structure chosen on the basis of controlled outputs step responses. Its parameters are estimated via corresponding delta model. The control system structure with two feedback controllers is considered. The resulting controllers are derived using polynomial approach. The method is tested on a mathematical model of the tubular chemical reactor. (en)
Title	Simulation of nonlinear adaptive control of a tubular chemical reactor Simulation of nonlinear adaptive control of a tubular chemical reactor (en)
skos:prefLabel	Simulation of nonlinear adaptive control of a tubular chemical reactor Simulation of nonlinear adaptive control of a tubular chemical reactor (en)
skos:notation	RIV/70883521:28140/12:43868900!RIV13-MSM-28140___
http://linked.open...avai/predkladatel	Fakulta aplikované informatiky
http://linked.open...avai/riv/aktivita	P
http://linked.open...avai/riv/aktivity	P(ED2.1.00/03.0111)
http://linked.open...vai/riv/dodaniDat	2013
http://linked.open...aciTvurceVysledku	Bobál, Vladimír Dostál, Petr Vojtěšek, Jiří
http://linked.open.../riv/druhVysledku	D - Článek ve sborníku
http://linked.open...iv/duvernostUdaju	S - Úplné a pravdivé údaje nepodléhající ochraně podle zvláštních právních předpisů
http://linked.open...titaPredkladatele	Univerzita Tomáše Bati ve Zlíně / Fakulta aplikované informatiky
http://linked.open...dnocenehoVysledku	168020
http://linked.open...ai/riv/idVysledku	RIV/70883521:28140/12:43868900
http://linked.open...riv/jazykVysledku	eng - angličtina
http://linked.open.../riv/klicovaSlova	Nonlinear system, tubular chemical reactor, approximate linear model, parameter identification, polynomial approach, pole assignment. (en)
http://linked.open.../riv/klicoveSlovo	parameter identification approximate linear model polynomial approach tubular chemical reactor Nonlinear system pole assignment.
http://linked.open...ontrolniKodProRIV	[ECE481062BC0]
http://linked.open...v/mistoKonaniAkce	Řím
http://linked.open...i/riv/mistoVydani	Řím
http://linked.open...i/riv/nazevZdroje	Proceedings of The Interntional Workshop on Applied Modeling and Simulation, 2012
http://linked.open...in/vavai/riv/obor	CI
http://linked.open...ichTvurcuVysledku	3 (xsd:int)
http://linked.open...cetTvurcuVysledku	3 (xsd:int)
http://linked.open...vavai/riv/projekt	Centre of Polymer Systems
http://linked.open...UplatneniVysledku	2012
http://linked.open...iv/tvurceVysledku	Bobál, Vladimír Dostál, Petr Vojtěšek, Jiří
http://linked.open...vavai/riv/typAkce	WRD - Světová
http://linked.open.../riv/zahajeniAkce	2012-09-24 (xsd:date)
number of pages	6 (xsd:int)
http://purl.org/ne...btex#hasPublisher	IEEE
https://schema.org/isbn	978-88-97999-07-2
http://localhost/t...ganizacniJednotka	28140
is http://linked.open...avai/riv/vysledek of	Simulation of nonlinear adaptive control of a tubular chemical reactor

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