Приказ основних података о документу

dc.creatorJaćimović, Branislav M.
dc.creatorGenić, Srbislav
dc.creatorJacimović, Nikola B.
dc.date.accessioned2022-09-19T16:54:52Z
dc.date.available2022-09-19T16:54:52Z
dc.date.issued2012
dc.identifier.issn0888-5885
dc.identifier.urihttps://machinery.mas.bg.ac.rs/handle/123456789/1457
dc.description.abstractReboilers are essential for the proper work of distillation and stripping columns. Hereby the intensity of axial mixing along the reboiler (Peclet number) is used for the reboiler separation efficiency modeling and estimation for binary systems. Two fully worked examples show that the separation (Murphree) efficiency varies significantly depending on the adopted reboiler flow model. Murphree efficiency ranges between 1.40 and 0.663 in example 1, and between 1.962 and 1 in example 2. The general conclusion is that the reboiler performance must be considered carefully in the case of design of the new plants,as well as in the case of "brown field" projects.en
dc.publisherAmer Chemical Soc, Washington
dc.relationMinistry of Science and Technological Development of Serbia
dc.rightsrestrictedAccess
dc.sourceIndustrial & Engineering Chemistry Research
dc.titleReboiler Separation Efficiencies for Binary Systemsen
dc.typearticle
dc.rights.licenseARR
dc.citation.epage5804
dc.citation.issue16
dc.citation.other51(16): 5793-5804
dc.citation.rankM21
dc.citation.spage5793
dc.citation.volume51
dc.identifier.doi10.1021/ie202193m
dc.identifier.scopus2-s2.0-84860372545
dc.identifier.wos000303139300018
dc.type.versionpublishedVersion


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Приказ основних података о документу