Output Constraint Softening for SISO Model Predictive Control

dc.contributor.authorZafiriou, Evanghelosen_US
dc.contributor.authorChiou, Hung-Wenen_US
dc.contributor.departmentISRen_US
dc.date.accessioned2007-05-23T09:53:28Z
dc.date.available2007-05-23T09:53:28Z
dc.date.issued1993en_US
dc.description.abstractThe presence of constraints in the on-line optimization problem solved by model predictive Control algorithms results in a nonlinear control system, even if the plant and model dynamics are linear. This is the case both for physical constraints, like saturation constraints, as well for performance or safety constraints on outputs or other variables of the process. Performance constraints can usually be softened by allowing violation if necessary. This is advisable, as hard constraints can lead to stability problems. The determination of the necessary degree of softening is usually a trial-and-error matter. This paper utilizes a theoretical framework that allows to relate hard as well as soft constraints to closed-loop stability. We focus on the special case of output constraints for single-input single-output systems and develop a non- conservative condition. This condition allows the determination of the appropriate amount of softening either numerically or via a suitable Nyquist plot.en_US
dc.format.extent360426 bytes
dc.format.mimetypeapplication/pdf
dc.identifier.urihttp://hdl.handle.net/1903/5360
dc.language.isoen_USen_US
dc.relation.ispartofseriesISR; TR 1993-13en_US
dc.subjectoptimal controlen_US
dc.subjectstabilityen_US
dc.subjectChemical Process Systemsen_US
dc.titleOutput Constraint Softening for SISO Model Predictive Controlen_US
dc.typeTechnical Reporten_US

Files

Original bundle

Now showing 1 - 1 of 1
Loading...
Thumbnail Image
Name:
TR_93-13.pdf
Size:
351.98 KB
Format:
Adobe Portable Document Format