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Statements

Subject Item
n2:RIV%2F70883521%3A28140%2F10%3A63509091%21RIV11-MSM-28140___
rdf:type
n3:Vysledek skos:Concept
dcterms:description
The paper deals with the adaptive control of the nonlinear process represented by the Continuous Stirred Tank Reactor (CSTR). This type of reactor belongs to the class of systems with lumped-parameters. Mathematical model of this system consist of two nonlinear Ordinary Differential Equations (ODEs). The steady-state analysis uncovers two stable and one unstable operating points. Used adaptive approach is based on recursive identification of the system?s parameters during the control. A polynomial approach used for the controller synthesis has satisfied control requirements and moreover, it could be used for systems with negative properties such as nonlinearity, non-minimum phase etc. The goal of this work is to compare control for two stable steady-states. The paper deals with the adaptive control of the nonlinear process represented by the Continuous Stirred Tank Reactor (CSTR). This type of reactor belongs to the class of systems with lumped-parameters. Mathematical model of this system consist of two nonlinear Ordinary Differential Equations (ODEs). The steady-state analysis uncovers two stable and one unstable operating points. Used adaptive approach is based on recursive identification of the system?s parameters during the control. A polynomial approach used for the controller synthesis has satisfied control requirements and moreover, it could be used for systems with negative properties such as nonlinearity, non-minimum phase etc. The goal of this work is to compare control for two stable steady-states.
dcterms:title
Adaptive Control of Continuous-Stirred Tank Reactor in Two Stable Steady-States Adaptive Control of Continuous-Stirred Tank Reactor in Two Stable Steady-States
skos:prefLabel
Adaptive Control of Continuous-Stirred Tank Reactor in Two Stable Steady-States Adaptive Control of Continuous-Stirred Tank Reactor in Two Stable Steady-States
skos:notation
RIV/70883521:28140/10:63509091!RIV11-MSM-28140___
n4:aktivita
n5:Z
n4:aktivity
Z(MSM7088352101)
n4:dodaniDat
n9:2011
n4:domaciTvurceVysledku
n11:5552990 n11:4881885
n4:druhVysledku
n16:O
n4:duvernostUdaju
n12:S
n4:entitaPredkladatele
n14:predkladatel
n4:idSjednocenehoVysledku
245380
n4:idVysledku
RIV/70883521:28140/10:63509091
n4:jazykVysledku
n6:eng
n4:klicovaSlova
Chemical reactor; adaptive control; delta model; parameter estimation; polynomial method.
n4:klicoveSlovo
n7:polynomial%20method. n7:delta%20model n7:parameter%20estimation n7:Chemical%20reactor n7:adaptive%20control
n4:kontrolniKodProRIV
[33BF3AD9A35D]
n4:obor
n15:BC
n4:pocetDomacichTvurcuVysledku
2
n4:pocetTvurcuVysledku
2
n4:rokUplatneniVysledku
n9:2010
n4:tvurceVysledku
Dostál, Petr Vojtěšek, Jiří
n4:zamer
n17:MSM7088352101
n13:organizacniJednotka
28140