Article ID Journal Published Year Pages File Type
9626027 Fluid Phase Equilibria 2005 7 Pages PDF
Abstract
Isobaric vapor-liquid equilibrium data have been experimentally determined at 101.3 kPa for the binary systems ethanol + ethyl lactate, isopropanol + isopropyl lactate and n-butanol + n-butyl lactate. No azeotrope was found in any of the systems. All the experimental data reported were thermodynamically consistent according to the point-to-point method of Fredenslund. The activity coefficients were correlated with the NRTL and UNIQUAC liquid-phase equations and the corresponding binary interaction parameters are reported. The densities and derived excess volumes for the three mixtures are also reported at 298.15 K.
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Physical Sciences and Engineering Chemical Engineering Chemical Engineering (General)
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