Author/Authors :
S. J. Norquay، نويسنده , , A. Palazoglu and J. A. Romagnoli، نويسنده ,
Latin Abstract :
Dual composition control of a high-purity distillation column is recognized as an industrially important, yet notoriously dicult
control problem. It is proposed, however, that Wiener models, consisting of a linear dynamic element followed in series by a static
nonlinear element, are ideal for representing this and several other nonlinear processes. They are relatively simple models requiring
little more eort in development than a standard linear step response model, yet oer superior characterization of systems with
highly nonlinear gains. Wiener models may be incorporated into MPC schemes in a unique way that eectively removes the non-
linearity from the control problem, preserving many of the favorable properties of linear MPC, especially in the analysis of stability.
In this paper, Wiener model predictive control is applied to an industrial C2-splitter at the Orica Ole®nes plant with promising
results.
NaturalLanguageKeyword :
distillation control , Nonlinear systems , Wiener model. , Predictive control
