• DocumentCode
    486698
  • Title

    The Value of Simple Multivariable and Nonlinear Models in Process Control

  • Author

    Georgakis, Chilstos

  • Author_Institution
    Department of Chemical Engineering and Chemical Process Modeling and Control Research Center, Lehigh University, Bethlehem, PA 18018
  • fYear
    1986
  • fDate
    18-20 June 1986
  • Firstpage
    1199
  • Lastpage
    1203
  • Abstract
    Simple conceptual or mathematical models have always been used in design of linear SISO process controllers. On the other hand the design of nonlinear or MIMO controllers has always been perceived as requiring a detailed dynamic model. This communication aims to show that, the use of simple models, can drastically affect the design of such controllers by suggesting a design framework that centers around the extensive variable of the process instead of the intensive one that are usually measured.
  • Keywords
    Chemical engineering; Chemical processes; Chemical reactors; Communication system control; Inductors; Mathematical model; Polyethylene; Polymers; Process control; Tellurium;
  • fLanguage
    English
  • Publisher
    ieee
  • Conference_Titel
    American Control Conference, 1986
  • Conference_Location
    Seattle, WA, USA
  • Type

    conf

  • Filename
    4789116