Internal Model Control: Robust Digital Controller Synthesis for Multivariable Open-Loop Stable or Unstable Processes

dc.contributor.authorZafiriou, E.en_US
dc.contributor.authorMorari, M.en_US
dc.contributor.departmentISRen_US
dc.date.accessioned2007-05-23T09:46:03Z
dc.date.available2007-05-23T09:46:03Z
dc.date.issued1990en_US
dc.description.abstractThe two-step Internal Model Control (IMC) procedure is presented for the synthesis of multivariable discrete controllers. This paper adds the following features to the IMC design methodology: (i) Extension to open-loop unstable plants. (ii) Design of the first-step (no model error) IMC controller so that the L2-error (sum of squared errors) is minimized for every setpoint or disturbance vector in a designer-specified set and their linear combinations. (iii) The second-step (model-plant mismatch) multivariable low-pass filter is designed for robust stability and performance by minimizing a non-conservative robustness measure, the Structured Singular Value. (iv) The potential problem in intersample rippling is avoided by introducing a modification in the first-step controller and formulating the robust performance objective for the continuous plant output.en_US
dc.format.extent1724992 bytes
dc.format.mimetypeapplication/pdf
dc.identifier.urihttp://hdl.handle.net/1903/4996
dc.language.isoen_USen_US
dc.relation.ispartofseriesISR; TR 1990-48en_US
dc.subjectchemical process controlen_US
dc.subjectdistillation controlen_US
dc.subjectpredictive controlen_US
dc.subjectlinear systemsen_US
dc.subjectoptimal controlen_US
dc.subjectrobust controlen_US
dc.subjectChemical Process Systemsen_US
dc.titleInternal Model Control: Robust Digital Controller Synthesis for Multivariable Open-Loop Stable or Unstable Processesen_US
dc.typeTechnical Reporten_US

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