Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Measurements and correlation of vapour liquid equilibria of 2-butanone and hydrocarbons binary systems at two different pressures

Lladosa, E.[Estela], Martinez, N. F.[Nelson F.], Monton, J. B. [Juan B.], Torre, J. d. l.[Javier de la]
Fluid Phase Equilib. 2011, 307, 1, 24-29
ABSTRACT
Consistent isobaric vapour-liquid equilibrium data have been measured for 2-butanone + n-hexane, 2- butanone + n-heptane, and 2-butanone + 2,2,4-trimethylpentane at two different pressures. All binary systems present a minimum boiling azeotrope at both pressures, and show that the azeotropic compositions are weakly dependent on pressure. The equilibrium data were correlated using the Wilson, NRTL, and UNIQUAC models for which the parameters are reported.
Compounds
# Formula Name
1 C6H14 hexane
2 C4H8O butanone
3 C7H16 heptane
4 C8H18 2,2,4-trimethylpentane
Datasets
The table above is generated from the ThermoML associated json file (link above). POMD and RXND refer to PureOrMixture and Reaction Datasets. The compound numbers are included in properties, variables, and phases, if specificied; the numbers refer to the table of compounds on the left.
Type Compound-# Property Variable Constraint Phase Method #Points
  • POMD
  • 1
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Chromatography
  • 2
  • POMD
  • 2
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Chromatography
  • 3
  • POMD
  • 3
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Chromatography
  • 2
  • POMD
  • 4
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Chromatography
  • 2
  • POMD
  • 2
  • 1
  • Azeotropic pressure, kPa ; Liquid
  • Mole fraction - 2; Liquid
  • Liquid
  • Gas
  • By X=Y
  • 2
  • POMD
  • 2
  • 1
  • Azeotropic temperature, K ; Liquid
  • Mole fraction - 2; Liquid
  • Liquid
  • Gas
  • By X=Y
  • 2
  • POMD
  • 2
  • 1
  • Mole fraction - 2 ; Liquid
  • Pressure, kPa; Gas
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Chromatography
  • 32
  • POMD
  • 2
  • 1
  • Mole fraction - 2 ; Gas
  • Pressure, kPa; Gas
  • Temperature, K; Gas
  • Gas
  • Liquid
  • Chromatography
  • 32
  • POMD
  • 2
  • 3
  • Azeotropic pressure, kPa ; Liquid
  • Mole fraction - 2; Liquid
  • Liquid
  • Gas
  • By X=Y
  • 2
  • POMD
  • 2
  • 3
  • Azeotropic temperature, K ; Liquid
  • Mole fraction - 2; Liquid
  • Liquid
  • Gas
  • By X=Y
  • 2
  • POMD
  • 2
  • 3
  • Mole fraction - 2 ; Liquid
  • Pressure, kPa; Gas
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Chromatography
  • 31
  • POMD
  • 2
  • 3
  • Mole fraction - 2 ; Gas
  • Pressure, kPa; Gas
  • Temperature, K; Gas
  • Gas
  • Liquid
  • Chromatography
  • 31
  • POMD
  • 2
  • 4
  • Azeotropic pressure, kPa ; Liquid
  • Mole fraction - 2; Liquid
  • Liquid
  • Gas
  • By X=Y
  • 2
  • POMD
  • 2
  • 4
  • Azeotropic temperature, K ; Liquid
  • Mole fraction - 2; Liquid
  • Liquid
  • Gas
  • By X=Y
  • 2
  • POMD
  • 2
  • 4
  • Mole fraction - 2 ; Gas
  • Pressure, kPa; Gas
  • Temperature, K; Gas
  • Gas
  • Liquid
  • Chromatography
  • 32
  • POMD
  • 2
  • 4
  • Mole fraction - 2 ; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Chromatography
  • 32