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dc.creatorKijevčanin, Mirjana
dc.creatorŠerbanović, Slobodan P.
dc.creatorRadović, Ivona
dc.creatorĐorđević, Bojan D.
dc.creatorTasić, Aleksandar Ž.
dc.date.accessioned2021-03-10T10:45:20Z
dc.date.available2021-03-10T10:45:20Z
dc.date.issued2007
dc.identifier.issn0378-3812
dc.identifier.urihttp://TechnoRep.tmf.bg.ac.rs/handle/123456789/1122
dc.description.abstractDensities p of the ternary system (ethanol + chloroform + benzene) and binaries (ethanol + chloroform) and (chloroform + benzene), have been measured at six temperatures (288.15, 293.15, 298.15, 303.15, 308.15, 313.15) K and pressure 101.33 kPa with an Anton Paar DMA 5000 digital vibrating tube densimeter. Excess molar volumes V-E were calculated from these densities data and fitted by the polynomial Redlich-Kister (for binary data) and Nagata and Tamura (for ternary data) equations. Radojkovic et al. equation was used for the prediction of the V-E of ternary data. The obtained results have been explained in terms of different effects between molecules of present species, taking into consideration influence of temperature on them. For the correlation of binary and prediction of ternary V-E with cubic equation of state (CEOS), the Peng-Robinson-Stryjek-Vera equation of state (PRSV CEOS) coupled with two different types of independent and temperature dependent mixing rules: (i) the composition dependent (vdW1) and (ii) CEOS with G(E) equation (CEOS/G(E)) Twu and co-workers (TCBT) model were used. For the correlation of ternary V data only Twu and co-workers (TCBT) mixing rules were used. Rhoen
dc.publisherElsevier Science Bv, Amsterdam
dc.rightsrestrictedAccess
dc.sourceFluid Phase Equilibria
dc.subjectexperimentalen
dc.subjectternary systemen
dc.subjectdensitiesen
dc.subjectexcess molar volumesen
dc.subjectcubic FOSen
dc.titleVolumetric properties of the ternary system ethanol plus chloroform plus benzene at temperature range (288.15-313.15) K: Experimental data, correlation and prediction by cubic EOSen
dc.typearticle
dc.rights.licenseARR
dc.citation.epage92
dc.citation.issue2
dc.citation.other251(2): 78-92
dc.citation.rankM21
dc.citation.spage78
dc.citation.volume251
dc.identifier.doi10.1016/j.fluid.2006.11.005
dc.identifier.rcubconv_2777
dc.identifier.scopus2-s2.0-33846160163
dc.identifier.wos000243798600002
dc.type.versionpublishedVersion


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