dc.creator | Radović, Ivona | |
dc.creator | Kijevčanin, Mirjana | |
dc.creator | Šerbanović, Slobodan P. | |
dc.creator | Đorđević, Bojan D. | |
dc.date.accessioned | 2021-03-10T11:24:51Z | |
dc.date.available | 2021-03-10T11:24:51Z | |
dc.date.issued | 2010 | |
dc.identifier.issn | 0378-3812 | |
dc.identifier.uri | http://TechnoRep.tmf.bg.ac.rs/handle/123456789/1728 | |
dc.description.abstract | Densities rho of the ternary system 1-butanol + hexylamine + n-heptane and binaries: 1-butanol + hexylamine and hexylamine + n-heptane within the temperature range (288.15-323.15K) and atmospheric pressure are reported. Excess molar volumes V-E were calculated from the density data and fitted by the Redlich-Kister and Nagata and Tamura equations. The results are analyzed in terms of the molecular interactions between the components of mixtures. Several empirical relationships (Radojkovic, Kohler, Jacob-Fitzner, Colinet,Tsao-Smith,Toop, Scatchard and Rastogi) were applied for prediction of V-E data of the ternary system from the corresponding binary data. For the correlation of binary V-E, the Peng-Robinson-Stryjek-Vera cubic equation of state (PRSV CEOS) coupled with the van der Waals (vcIW1) and CEOS/G(E) mixing rule introduced by Twu et al. (TCBT) were chosen. Prediction of V-E of ternary system was performed by the same vdW1 and TCBT models. For the correlation of the V-E of ternary data only TCBT mixing rules were used. | en |
dc.publisher | Elsevier Science Bv, Amsterdam | |
dc.relation | Ministry of Science and Environmental Protection, Serbia | |
dc.relation | info:eu-repo/grantAgreement/MESTD/MPN2006-2010/142064/RS// | |
dc.rights | restrictedAccess | |
dc.source | Fluid Phase Equilibria | |
dc.subject | Experimental determination | en |
dc.subject | Densities | en |
dc.subject | Excess molar volumes | en |
dc.subject | Ternary system | en |
dc.subject | Cubic EOS | en |
dc.title | 1-Butanol + hexylamine plus n-heptane at temperature range (288.15-323.15 K): Experimental density data, excess molar volumes determination and modeling with cubic EOS | en |
dc.type | article | |
dc.rights.license | ARR | |
dc.citation.epage | 130 | |
dc.citation.issue | 1 | |
dc.citation.other | 298(1): 117-130 | |
dc.citation.rank | aM21 | |
dc.citation.spage | 117 | |
dc.citation.volume | 298 | |
dc.identifier.doi | 10.1016/j.fluid.2010.07.011 | |
dc.identifier.scopus | 2-s2.0-84755160731 | |
dc.identifier.wos | 000283023700016 | |
dc.type.version | publishedVersion | |