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Please use this identifier to cite or link to this item: http://dspace.bits-pilani.ac.in:8080/jspui/handle/123456789/2658
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dc.contributor.authorJain, Amit
dc.date.accessioned2021-10-08T09:06:22Z
dc.date.available2021-10-08T09:06:22Z
dc.date.issued2014
dc.identifier.urihttps://www.readcube.com/articles/10.1007%2F978-81-322-1602-5_48
dc.identifier.urihttp://dspace.bits-pilani.ac.in:8080/xmlui/handle/123456789/2658
dc.description.abstractThe aim of this paper is to gain insights into how process dynamics can affect control configuration decision based on relative gain array (RGA) analysis in the face of model uncertainty. Analytical expressions for worst-case bounds of uncertainty in steady-state and dynamic RGA are derived for two inputs two outputs (TITO) plant models. A simulation example which has been used in several prior studies is considered here to demonstrate the results. The obtained bounds of uncer- tainty in RGA provide valuable information pertaining to the necessity of robustness and accuracy in the model of decentralized multivariable systems.en_US
dc.language.isoenen_US
dc.publisherSpringeren_US
dc.subjectChemical Engineeringen_US
dc.subjectRelative gain arrayen_US
dc.subjectParametric uncertaintyen_US
dc.subjectControl configuration selectionen_US
dc.titleRGA Analysis of Dynamic Process ModelsUnder Uncertaintyen_US
dc.typeBook Chapteren_US
Appears in Collections:Department of Chemical Engineering

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