Journal of Chemical & Engineering Data · 1998 · 29 citations · 7 references
Natural SciencesChemistryPhase TransformationsPhysical ChemistryThermodynamicsEquilibrium ThermodynamicsHigh-pressure ThermodynamicsPhase DiagramsPhase EquilibriaPhase EquilibriumThermodynamics Of Phase EquilibriaBinary Phase EquilibriaEquilibrium Vapor PressurePhase Equilibria At High PressureVapor - Liquid EquilibriumVapor PressureVapor-liquid EquilibriaVapor-liquid EquilibriumVapour-liquid Equilibrium
Pure-component vapor pressures and vapor−liquid equilibrium data at 94 kPa have been determined for the binary systems methyl 1,1-dimethylethyl ether + benzene and methyl 1,1-dimethylethyl ether + toluene. The systems exhibit regular behavior and a slight positive deviation from ideality, and no azeotrope is present. The data were correlated by the Wisniak−Tamir equation, and the appropriate parameters are reported.
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