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Statements

Subject Item
n2:RIV%2F70883521%3A28140%2F11%3A43866530%21RIV12-MSM-28140___
rdf:type
n16:Vysledek skos:Concept
dcterms:description
The paper deals with continuous-time nonlinear adaptive control of a continuous stirred tank reactor. The control strategy is based on an application of the controller consisting of a linear and nonlinear part. The static nonlinear part is derived in the way of an inversion and exponential approximation of measured or simulated input-output data. The design of the two degrees of freedom (2DOF) dynamic linear part is based on approximation of nonlinear elements in the control loop by a continuous-time external linear model with directly estimated parameters. In the control design procedure, the polynomial approach with the pole assignment method is used. The nonlinear adaptive control is tested by simulations on the nonlinear model of the CSTR with a consecutive exothermic reaction. The paper deals with continuous-time nonlinear adaptive control of a continuous stirred tank reactor. The control strategy is based on an application of the controller consisting of a linear and nonlinear part. The static nonlinear part is derived in the way of an inversion and exponential approximation of measured or simulated input-output data. The design of the two degrees of freedom (2DOF) dynamic linear part is based on approximation of nonlinear elements in the control loop by a continuous-time external linear model with directly estimated parameters. In the control design procedure, the polynomial approach with the pole assignment method is used. The nonlinear adaptive control is tested by simulations on the nonlinear model of the CSTR with a consecutive exothermic reaction.
dcterms:title
Simulation of the 2DOF nonlinear adaptive control of a chemical reactor Simulation of the 2DOF nonlinear adaptive control of a chemical reactor
skos:prefLabel
Simulation of the 2DOF nonlinear adaptive control of a chemical reactor Simulation of the 2DOF nonlinear adaptive control of a chemical reactor
skos:notation
RIV/70883521:28140/11:43866530!RIV12-MSM-28140___
n16:predkladatel
n20:orjk%3A28140
n3:aktivita
n4:Z n4:P
n3:aktivity
P(ED2.1.00/03.0111), Z(MSM7088352101)
n3:dodaniDat
n17:2012
n3:domaciTvurceVysledku
n5:5552990 n5:4881885 n5:1846787
n3:druhVysledku
n11:D
n3:duvernostUdaju
n23:S
n3:entitaPredkladatele
n13:predkladatel
n3:idSjednocenehoVysledku
229480
n3:idVysledku
RIV/70883521:28140/11:43866530
n3:jazykVysledku
n9:eng
n3:klicovaSlova
Chemical reactor, external linear model, nonlinear control, parameter estimation, control simulation.
n3:klicoveSlovo
n8:nonlinear%20control n8:Chemical%20reactor n8:control%20simulation. n8:external%20linear%20model n8:parameter%20estimation
n3:kontrolniKodProRIV
[21DC71D47F9B]
n3:mistoKonaniAkce
Krakow
n3:mistoVydani
Nicosia
n3:nazevZdroje
Proceedings 25th European Conference on Modelling and Simulation ECMS 2011
n3:obor
n19:BC
n3:pocetDomacichTvurcuVysledku
3
n3:pocetTvurcuVysledku
3
n3:projekt
n22:ED2.1.00%2F03.0111
n3:rokUplatneniVysledku
n17:2011
n3:tvurceVysledku
Vojtěšek, Jiří Dostál, Petr Bobál, Vladimír
n3:typAkce
n12:EUR
n3:zahajeniAkce
2011-06-07+02:00
n3:zamer
n15:MSM7088352101
s:numberOfPages
7
n14:hasPublisher
ECMS
n10:isbn
978-0-9564944-2-9
n21:organizacniJednotka
28140