Приказ основних података о документу

dc.creatorJaćimović, Branislav M.
dc.creatorGenić, Srbislav
dc.date.accessioned2022-09-19T16:10:29Z
dc.date.available2022-09-19T16:10:29Z
dc.date.issued2008
dc.identifier.issn0263-8762
dc.identifier.urihttps://machinery.mas.bg.ac.rs/handle/123456789/811
dc.description.abstractThe paper deals with the tray-to-tray method for determining the required number of trays in gas-liquid columns in case of intensive entrainment. The equations for estimation of the tray efficiency are derived for top, bottom and intermediate trays, and they incorporate the number of gas and liquid phases transfer units, stripping factor, Peclet number of mixing and fractional entrainment. These equations can be simplified to the well-known one-parametric diffusion model explained in Bubble Tray Design Manual (1958) [Bubble Tray Design Manual, 1958, AIChE, New York] for case of negligible entrainment. The algorithm of tray-to-tray method is based on tray efficiency calculated for each tray separately and it enables the calculation of the number of required trays, starting from the bottom tray. Given example shows how the excessive entrainment decreases of the driving force of the process.en
dc.publisherInst Chemical Engineers, Rugby
dc.rightsrestrictedAccess
dc.sourceChemical Engineering Research & Design
dc.subjecttray efficiencyen
dc.subjectnumber of traysen
dc.subjectentrainmenten
dc.titleTray-to-tray method for estimation of the number of trays in gas-liquid columns in case of intensive entrainmenten
dc.typearticle
dc.rights.licenseARR
dc.citation.epage434
dc.citation.issue5A
dc.citation.other86(5A): 427-434
dc.citation.rankM22
dc.citation.spage427
dc.citation.volume86
dc.identifier.doi10.1016/j.cherd.2007.12.006
dc.identifier.scopus2-s2.0-46149118477
dc.identifier.wos000256240000001
dc.type.versionpublishedVersion


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Приказ основних података о документу