• DocumentCode
    2030927
  • Title

    Flatness based analysis of a chemical reactor pilot plant

  • Author

    Ojeda, Angel ; Delgado, Marisol

  • Author_Institution
    Departamento de Procesos y Sistemas, Univ. Simon Bolivar, Caracas, Venezuela
  • Volume
    3
  • fYear
    2000
  • fDate
    2000
  • Firstpage
    1906
  • Abstract
    In this paper, the authors present a flatness-based analysis of a continuous stirred-tank reactor (CSTR) where a saponification reaction between ethyl acetate and sodium hydroxide is taking place. A nonlinear model represents the reactor and as consequence of the flatness property we can make an explicit analysis of the reactor by formally calculating the reactor variables as functions of the flat outputs and their time derivatives. The equations that show that the reactor is a flat system are deduced in the work
  • Keywords
    chemical industry; control system analysis; nonlinear control systems; process control; chemical process control; chemical reactor pilot plant; continuous stirred-tank reactor; control simulation; ethyl acetate; flatness based analysis; nonlinear model; reactor variables; saponification reaction; sodium hydroxide; Chemical analysis; Chemical processes; Chemical reactors; Control systems; Equations; Inductors; Input variables; Linear feedback control systems; Linear systems; Linearity;
  • fLanguage
    English
  • Publisher
    ieee
  • Conference_Titel
    Industrial Electronics Society, 2000. IECON 2000. 26th Annual Confjerence of the IEEE
  • Conference_Location
    Nagoya
  • Print_ISBN
    0-7803-6456-2
  • Type

    conf

  • DOI
    10.1109/IECON.2000.972567
  • Filename
    972567