The Canadian Journal of Chemical Engineering · 1994 · 14 citations · 15 references
Natural SciencesChemical EngineeringChemistryAnalytical ChemistryPhysical ChemistryThermodynamicsEquilibrium ThermodynamicsPhase EquilibriumTemperature MeasurementExperimental Data CollectionLiquid-vapor EquilibriaLiquid-vapor EquilibriumTotal PressureVapor - Liquid EquilibriumVapor PressureVapor-liquid EquilibriaVapor-liquid Equilibrium
Abstract Isothermal vapor‐liquid equilibria were measured using a still with the aid of a computer for control of the temperature and measurement of the total pressure. The measurements were made with circulation of both the vapor and liquid phases in a still of the Rogalski and Malanowski type (1980). The isobaric vapor‐liquid equilibria were measured for the benzene + 2‐propanol system at 101.3 kPa in order to test the consistency of results obtained with this still. Isothermal vapor‐liquid equilibria were measured for the 2,3‐dimethylbutane + methanol system at 313.15 K. The experimental data were correlated with the Wilson (1964) equation.
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