• DocumentCode
    2197779
  • Title

    A comparison of fundamental model-based and multiple model predictive control

  • Author

    Aufderheide, Brian ; Prasad, Vinay ; Bequette, B. Wayne

  • Author_Institution
    Isermann Dept. of Chem. Eng., Rensselaer Polytech. Inst., Troy, NY, USA
  • Volume
    5
  • fYear
    2001
  • fDate
    2001
  • Firstpage
    4863
  • Abstract
    A multiple model strategy is implemented in a model predictive control framework. The model bank design requires minimal plant knowledge based on the ranges of gains, dominant time constants and time delays. The application example is the isothermal Van de Vusse reaction in a continuous stirred tank reactor, which exhibits challenging input multiplicity behavior. Disturbances include additive input and output noises and changes in system parameters. Results are compared with an extended Kalman filter (EKF)-based model predictive controller that uses a fundamental model with a disturbance parameter estimated online. The multiple model predictive controller performance is comparable to that demonstrated by the EKF-based model predictive controller
  • Keywords
    Kalman filters; chemical industry; noise; optimisation; parameter estimation; predictive control; process control; step response; Kalman filter; continuous stirred tank reactor; disturbance parameter estimation; isothermal Van de Vusse reaction; multiple model predictive control; noises; optimization; step response; Additive noise; Continuous-stirred tank reactor; Delay effects; Fluid flow control; Isothermal processes; Nonlinear dynamical systems; Optimal control; Predictive control; Predictive models; Steady-state;
  • fLanguage
    English
  • Publisher
    ieee
  • Conference_Titel
    Decision and Control, 2001. Proceedings of the 40th IEEE Conference on
  • Conference_Location
    Orlando, FL
  • Print_ISBN
    0-7803-7061-9
  • Type

    conf

  • DOI
    10.1109/.2001.980977
  • Filename
    980977