• DocumentCode
    313176
  • Title

    Tutorial: process control through nonlinear modeling

  • Author

    Rhinehart, R. Russell

  • Author_Institution
    Dept. of Chem. Eng., Texas Tech. Univ., Lubbock, TX, USA
  • Volume
    3
  • fYear
    1997
  • fDate
    4-6 Jun 1997
  • Firstpage
    2011
  • Abstract
    Technical advances in computers make it feasible to use nonlinear process models for automatic control. One advantage over linear model-based controllers is that nonlinear controllers are functional over a wider operating range without retuning; and, where process nonlinearity is the major control problem, nonlinear controllers have demonstrated industrial success. When designed with adaptive models, tracking phenomenologically meaningful model coefficients for process diagnosis, and using the model for supervisory optimization are other advantages. Disadvantages are the required case-by-case controller design and inability to mathematically guarantee such features as convergence, stability, etc
  • Keywords
    control nonlinearities; convergence; dynamics; model reference adaptive control systems; nonlinear control systems; optimisation; process control; SISO systems; convergence; dynamics; model based control; nonlinear control; nonlinear modeling; nonlinearity; process control; process diagnosis; supervisory optimization; Automatic control; Chemical engineering; Difference equations; Industrial control; Inverse problems; Output feedback; Predictive models; Process control; Thermal variables control; Tutorial;
  • fLanguage
    English
  • Publisher
    ieee
  • Conference_Titel
    American Control Conference, 1997. Proceedings of the 1997
  • Conference_Location
    Albuquerque, NM
  • ISSN
    0743-1619
  • Print_ISBN
    0-7803-3832-4
  • Type

    conf

  • DOI
    10.1109/ACC.1997.611041
  • Filename
    611041