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
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