Please use this identifier to cite or link to this item: http://hdl.handle.net/2080/1917
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dc.contributor.authorMishra, R K-
dc.contributor.authorDan, T K-
dc.date.accessioned2013-04-12T08:39:45Z-
dc.date.available2013-04-12T08:39:45Z-
dc.date.issued2013-04-
dc.identifier.citationIEEE International Conference on Emerging Trends in Computing, Communication and Nanotechnology, ICE-CCN-2013,Tuticorin, Tamilnadu,India March. 25 – 26, 2013en
dc.identifier.urihttp://hdl.handle.net/2080/1917-
dc.descriptionCopyright belongs to IEEEen
dc.description.abstractThe prime objective of any industrial process is to perform efficiently with variable cost reduction. Internal Model Control (IMC) is a commonly used technique that provides a transparent mode for the designing and tuning of various types of control architecture. In this paper, we have designed the internal model control for binary distillation column for SISO process. The transfer function has been taken from Wood and Berry model. The internal model control has been designed considering three strategies namely, process perfect, process mismatch with disturbances and process model with disturbance only. It has also been tried to reduce the disturbance created in the system by varying tuning parameter (λ)en
dc.format.extent237278 bytes-
dc.format.mimetypeapplication/pdf-
dc.language.isoen-
dc.publisherIEEEen
dc.subjectInternal Model Controlen
dc.subjectBinary Distillation Columnen
dc.subjectSISOen
dc.subjectDisturbanceen
dc.subjectWood and Berryen
dc.titleDesign of an Internal Model Control for SISO Binary Distillation Columnen
dc.typeArticleen
Appears in Collections:Conference Papers

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