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dc.contributor.authorDwivedi, Deeptanshu
dc.contributor.authorHalvorsen, Ivar j.
dc.contributor.authorSkogestad, Sigurd
dc.date.accessioned2017-08-18T08:07:55Z
dc.date.available2017-08-18T08:07:55Z
dc.date.created2012-01-11T11:10:11Z
dc.date.issued2011
dc.identifier.urihttp://hdl.handle.net/11250/2451091
dc.description.abstractControl and operation of energy efficient complex distillation arrangements like Kaibel and Petlyuk columns can be challenging. This paper discusses the control structure design for stabilizing and operation of aforesaid systems for separating a 4-component feed namely methanol, ethanol, propanol and n-butanol as an example. The works carried out on the Kaibel column include experimental studies while the work on the Petlyuk column comprises only the simulation studies. The work demonstrates validation of proposed control structure for these two systems. Hence, provides the suggestions for operation of these designs as well as future works.nb_NO
dc.language.isoengnb_NO
dc.titleControl Structure Design for Optimal Oparation of 4-Product Thermally Coupled Columnsnb_NO
dc.typeLecturenb_NO
dc.identifier.cristin882088
dc.description.localcodeCopyright: 2011: Authorsnb_NO
cristin.unitcode194,66,30,0
cristin.unitnameInstitutt for kjemisk prosessteknologi
cristin.ispublishedtrue
cristin.fulltextpostprint


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