Thermodynamics Research Center / ThermoML | Journal of Chemical and Engineering Data

Vapor Liquid Equilibrium between (278.15 and 323.15) K and Excess Functions at T = 298.15 K for 1-Bromobutane with 2-Methyl-1-propanol or 2-Butanol

Martinez, S.[Santiago], Garriga, R.[Rosa], Perez, P.[Pascual], Gracia, M.[Mariano]
J. Chem. Eng. Data 2003, 48, 2, 294-301
ABSTRACT
Vapor pressures of (1-bromobutane + 2-methyl-1-propanol or 2-butanol) at 10 temperatures between (278.15 and 323.15) K were measured by a static method. Excess molar enthalpies and volumes were also measured at 298.15 K. The reduction of the vapor pressures to obtain activity coefficients and excess molar Gibbs energies was carried out by fitting the vapor pressure data to the Wilson equation according to Barker's method. Azeotropic mixtures with a minimum boiling temperature were observed over the whole temperature range.
Compounds
# Formula Name
1 C4H9Br 1-bromobutane
2 C4H10O butan-2-ol
3 C4H10O 2-methyl-1-propanol
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
  • CCELL:dPV:0.01
  • 10
  • POMD
  • 2
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • CCELL:dPV:0.01
  • 10
  • POMD
  • 3
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • CCELL:dPV:0.01
  • 10
  • POMD
  • 3
  • 1
  • Excess molar enthalpy (molar enthalpy of mixing), kJ/mol ; Liquid
  • Mole fraction - 3; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Flow calorimetry
  • 13
  • POMD
  • 3
  • 1
  • Azeotropic pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • By P(X) extreme
  • 10
  • POMD
  • 3
  • 1
  • Excess molar volume, m3/mol ; Liquid
  • Mole fraction - 3; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Calculated with densities of this investigation
  • 16
  • POMD
  • 3
  • 1
  • Azeotropic composition: mole fraction - 3 ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • By T or P extreme
  • 10
  • POMD
  • 3
  • 1
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 3; Liquid
  • Liquid
  • Gas
  • CCELL:UFactor:2
  • 110
  • POMD
  • 2
  • 1
  • Excess molar enthalpy (molar enthalpy of mixing), kJ/mol ; Liquid
  • Mole fraction - 2; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Flow calorimetry
  • 13
  • POMD
  • 2
  • 1
  • Azeotropic pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • By P(X) extreme
  • 10
  • POMD
  • 2
  • 1
  • Excess molar volume, m3/mol ; Liquid
  • Mole fraction - 2; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Calculated with densities of this investigation
  • 18
  • POMD
  • 2
  • 1
  • Azeotropic composition: mole fraction - 2 ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • By T or P extreme
  • 10
  • POMD
  • 2
  • 1
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 2; Liquid
  • Liquid
  • Gas
  • CCELL:UFactor:2
  • 120