• DocumentCode
    486423
  • Title

    Adaptive Control Strategies for Process Startup

  • Author

    Phillips, Susan F. ; Seborg, Dale E.

  • Author_Institution
    Department of Chemical and Nuclear Engineering, University of California, Santa Barbara, California 93106
  • fYear
    1985
  • fDate
    19-21 June 1985
  • Firstpage
    1253
  • Lastpage
    1259
  • Abstract
    In many process control problems it is desirable to startup the process by making a smooth and rapid transition to the desired operating condition with little or no overshoot. For processes with large thermal capacitances, it is especially difficult to avoid overshoot during startup unless a very conservative (i.e., slow) startup is implemented. Adaptive control strategies are a promising solution because they can be used to predict the time at which heating should be stopped and cooling begun. Simulation studies for a fluidized sandbath demonstrate the advantages of the proposed approach.
  • Keywords
    Adaptive control; Chemical engineering; Chemical processes; Error correction; Parameter estimation; Predictive models; Steady-state; Switches; Temperature; Three-term control;
  • fLanguage
    English
  • Publisher
    ieee
  • Conference_Titel
    American Control Conference, 1985
  • Conference_Location
    Boston, MA, USA
  • Type

    conf

  • Filename
    4788812