Vapor–Liquid Equilibria of Binary Mixtures Containing 1-Butanol and Hydrocarbons at 313.15 K

dc.contributor.authorBelabbaci, Aouichaen_US
dc.contributor.authorVillamañan, Rosa M.en_US
dc.contributor.authorNegadi, Latifaen_US
dc.contributor.authorMartin, Carmen M.en_US
dc.contributor.authorAit Kaci, Ahmeden_US
dc.contributor.authorVillamañan, Miguel A.en_US
dc.date.accessioned2013-04-09T09:31:12Zen_US
dc.date.available2013-04-09T09:31:12Zen_US
dc.date.issued2012en_US
dc.description.abstractTotal pressure measurements made at 313.15 K by the static method for five binary mixtures 1-butanol + heptane, 2,2,4-trimethylpentane, dodecane, cyclohexane, and methylbenzene are presented. Data reduction by Barker's method provides correlations for GE, using the four-parameter Margules equation; also the Wilson, nonrandom two-liquid (NRTL), and universal quasichemical activity coefficient (UNIQUAC) models have been used for fitting binary systems. The five investigated mixtures exh ibit a positive deviation from ideality. No azeotrope has been detected for 1-butanol + dodecane, and the other systems show positive azeotropy. Good results a re-obtained in the prediction of total pressure for these systems.en_US
dc.identifier.otherdoi: 10.1021/je200840een_US
dc.identifier.urihttps://dspace.univ-tlemcen.dz/handle/112/1718en_US
dc.language.isoenen_US
dc.titleVapor–Liquid Equilibria of Binary Mixtures Containing 1-Butanol and Hydrocarbons at 313.15 Ken_US
dc.typeArticleen_US

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