AIChE Journal · 1975 · 150 citations · 11 references
EngineeringPart IiiExperimental ThermodynamicsChemistryBinary Liquid SystemsThermodynamic ModellingFluid PropertiesMolecular ThermodynamicsNumerical SimulationTransport PhenomenaData ReductionThermodynamicsEquilibrium Thermodynamic PropertyThermodynamic EquilibriumVapor‐liquid EquilibriumPhysicsExcess Gibbs FunctionPhase EquilibriumNatural SciencesEquilibrium ThermodynamicsChemical KineticsVle Data
Abstract Through an empirical but rational appraoch to the development of equations to represent the composition dependence of the excess Gibbs function for binary liquid systems, it has been found possible to correlate VLE data precisely, even for highly nonideal systems. This makes possible the application of Barker's method to the reduction of VLE data on a routine basis. The validity of the method is demonstrated through application to several sets of data from the literature, and new experimental data are presented for six diverse binary systems in vapor‐liquid equilibrium at 50°C.
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