A novel method for transition control of nonlinear processes is presented. Gain scheduling is implemented to ensure stability and desired output behavior over the operating region of interest while transition between the initial and the final steady state is achieved by predictive reference control (or reference governor). In this framework, the search of a feasible reference input sequence is performed so that the closed-loop system moves along an optimal curve of steady states. This curve is constructed off-line so that its points lie far from the border of the process constraint set and correspond to satisfactory controllability properties of the uncontrolled plant. Moreover, bifurcation analysis of the closed-loop system is performed by varying the reference signal according to the selected curve. In this way, regions of state multiplicity and/or instability are identified enabling the choice of the controller parameters values preventing transitions to undesired solution regimes. The method is validated on a simulated problem of start-up control of a jacketed continuous stirred tank reactor. © 2009 American Chemical Society.

Optimal reference trajectory shaping and robust gain-scheduling for transition control of nonlinear processes / Altimari, Pietro; Lucia, Russo; Erasmo, Mancusi; Mario Di, Bernardo; Crescitelli, Silvestro. - In: INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH. - ISSN 0888-5885. - STAMPA. - 48:20(2009), pp. 9128-9140. [10.1021/ie9001553]

Optimal reference trajectory shaping and robust gain-scheduling for transition control of nonlinear processes

ALTIMARI, PIETRO;
2009

Abstract

A novel method for transition control of nonlinear processes is presented. Gain scheduling is implemented to ensure stability and desired output behavior over the operating region of interest while transition between the initial and the final steady state is achieved by predictive reference control (or reference governor). In this framework, the search of a feasible reference input sequence is performed so that the closed-loop system moves along an optimal curve of steady states. This curve is constructed off-line so that its points lie far from the border of the process constraint set and correspond to satisfactory controllability properties of the uncontrolled plant. Moreover, bifurcation analysis of the closed-loop system is performed by varying the reference signal according to the selected curve. In this way, regions of state multiplicity and/or instability are identified enabling the choice of the controller parameters values preventing transitions to undesired solution regimes. The method is validated on a simulated problem of start-up control of a jacketed continuous stirred tank reactor. © 2009 American Chemical Society.
2009
01 Pubblicazione su rivista::01a Articolo in rivista
Optimal reference trajectory shaping and robust gain-scheduling for transition control of nonlinear processes / Altimari, Pietro; Lucia, Russo; Erasmo, Mancusi; Mario Di, Bernardo; Crescitelli, Silvestro. - In: INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH. - ISSN 0888-5885. - STAMPA. - 48:20(2009), pp. 9128-9140. [10.1021/ie9001553]
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/11573/476508
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