• DocumentCode
    487464
  • Title

    Comparison between Process Model based Controllers

  • Author

    Riggs, James B. ; Rhinehart, R. Russell

  • Author_Institution
    Department of Chemical Engineering, Texas Tech University
  • fYear
    1988
  • fDate
    15-17 June 1988
  • Firstpage
    1591
  • Lastpage
    1595
  • Abstract
    Process model based control (PMBC) refers to methods that use a nonlinear process model directly--without linearization--for process control. Nonlinear IMC and GCC have been compared on an idealized SISO CSTR. Both methods gave nearly the same performance throughout a wide range of reactor nonlinearity. A SISO heat exchanger was used to further study GMC. The CSTR was an open loop unstable, lumped parameter process without deadtime and with a large sample time to process time constant ratio. By contrast, the heat exchanger was an open loop stable, distributed parameter process with transport delay and a small sample to process time constant ratio. In spite of these differences, GMC gave robust control over a wide range of process nonlinearity while remaining relatively insensitive to process-model mismatch. Optimally tuned GMC parameters, performed equally well for both linear and nonlinear process extremes. By contrast, nonlinear IMC filter parameters must change with process nonlinearity. Additionally, it is illustrated that GMC can yield excellent results even with a steady state process model.
  • Keywords
    Chemical processes; Continuous-stirred tank reactor; Delay effects; Inductors; Integral equations; Nonlinear equations; Open loop systems; Process control; Steady-state; Temperature control;
  • fLanguage
    English
  • Publisher
    ieee
  • Conference_Titel
    American Control Conference, 1988
  • Conference_Location
    Atlanta, Ga, USA
  • Type

    conf

  • Filename
    4789975