dc.creatorRossi A.S.
dc.creatorWolf-Maciel M.R.
dc.creatorRomanielo L.L.
dc.creatorReis M.H.M.
dc.date2015
dc.date2015-06-25T12:50:49Z
dc.date2015-11-26T14:57:58Z
dc.date2015-06-25T12:50:49Z
dc.date2015-11-26T14:57:58Z
dc.date.accessioned2018-03-28T22:09:44Z
dc.date.available2018-03-28T22:09:44Z
dc.identifier
dc.identifierSeparation Science And Technology (philadelphia). Taylor And Francis Inc., v. 50, n. 4, p. 626 - 632, 2015.
dc.identifier1496395
dc.identifier10.1080/01496395.2014.957320
dc.identifierhttp://www.scopus.com/inward/record.url?eid=2-s2.0-84924070988&partnerID=40&md5=20d67a0cece7091e8ba9c4c746c580bc
dc.identifierhttp://www.repositorio.unicamp.br/handle/REPOSIP/85175
dc.identifierhttp://repositorio.unicamp.br/jspui/handle/REPOSIP/85175
dc.identifier2-s2.0-84924070988
dc.identifier.urihttp://repositorioslatinoamericanos.uchile.cl/handle/2250/1255764
dc.descriptionResidue curves are graphical tools used to understand the behavior of a mixture in a separation process and are often calculated assuming equilibrium between liquid and vapor phases. However, equilibrium assumption can lead to misleading conclusions about mixture behavior. Here the sensibility of residue curves is analyzed when efficiency values are applied to correct the equilibrium model. Efficiency values were calculated using the Barros and Wolf correlations. Results showed that residue curves are sensitive to the applied model, but singular points did not change. Residue curves did not cross distillation boundaries, since residue curves and distillation boundaries were calculated using the same model. Thus, the observed results confirm that residue curves are forbidden to cross distillation boundaries.
dc.description50
dc.description4
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dc.languageen
dc.publisherTaylor and Francis Inc.
dc.relationSeparation Science and Technology (Philadelphia)
dc.rightsfechado
dc.sourceScopus
dc.titleEffects Of Mass Transfer In Residue Curves And Analysis Of Distillation Boundary Crossing
dc.typeArtículos de revistas


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