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  • 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 a inversion and consecutive polynomial approximation of a measured or simulated input-output data. The design of the dynamic linear part is based on approximation of nonlinear elements in the control loop by a continuous-time external linear model with parameters estimated using a corresponding delta model. 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 a inversion and consecutive polynomial approximation of a measured or simulated input-output data. The design of the dynamic linear part is based on approximation of nonlinear elements in the control loop by a continuous-time external linear model with parameters estimated using a corresponding delta model. 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. (en)
Title
  • Nonlinear Control of a Chemical Reactor
  • Nonlinear Control of a Chemical Reactor (en)
skos:prefLabel
  • Nonlinear Control of a Chemical Reactor
  • Nonlinear Control of a Chemical Reactor (en)
skos:notation
  • RIV/70883521:28610/11:43866361!RIV12-MSM-28610___
http://linked.open...avai/predkladatel
http://linked.open...avai/riv/aktivita
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  • P(ED2.1.00/03.0111), Z(MSM7088352101)
http://linked.open...vai/riv/dodaniDat
http://linked.open...aciTvurceVysledku
http://linked.open.../riv/druhVysledku
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http://linked.open...dnocenehoVysledku
  • 216223
http://linked.open...ai/riv/idVysledku
  • RIV/70883521:28610/11:43866361
http://linked.open...riv/jazykVysledku
http://linked.open.../riv/klicovaSlova
  • Chemical reactor, nonlinear process, nonlinear control, adaptive control, polynomial method (en)
http://linked.open.../riv/klicoveSlovo
http://linked.open...ontrolniKodProRIV
  • [F7B45EC512F2]
http://linked.open...v/mistoKonaniAkce
  • Tatranská Lomnica
http://linked.open...i/riv/mistoVydani
  • Bratislava
http://linked.open...i/riv/nazevZdroje
  • 18th International Conference on Process Control ´11
http://linked.open...in/vavai/riv/obor
http://linked.open...ichTvurcuVysledku
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http://linked.open...vavai/riv/projekt
http://linked.open...UplatneniVysledku
http://linked.open...iv/tvurceVysledku
  • Bobál, Vladimír
  • Dostál, Petr
  • Vojtěšek, Jiří
http://linked.open...vavai/riv/typAkce
http://linked.open.../riv/zahajeniAkce
http://linked.open...n/vavai/riv/zamer
number of pages
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  • Slovenská technická univerzita v Bratislave
https://schema.org/isbn
  • 978-80-227-3517-9
http://localhost/t...ganizacniJednotka
  • 28610
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