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

Excess Enthalpy and Vapor-Liquid Equilibrium at Atmospheric Pressure for the Binary Systems 2-Methyl-2-propanol + 2,4,4-Trimethyl-1-pentene and 2-Butanol + 2,4,4-Trimethyl-1-pentene

Kim, Y.[Younghun], Pokki, J. -P.[Juha-Pekka], Rehak, K.[Karel], Matous, J.[Jaroslav], Aittamaa, J.[Juhani]
J. Chem. Eng. Data 2004, 49, 2, 246-250
ABSTRACT
Excess molar enthalpies were measured for the binary systems 2-methyl-2-propanol + 2,4,4-trimethyl- 1-pentene at 300 K and for 2-butanol + 2,4,4-trimethyl-1-pentene at 298 K. Vapor-liquid equilibria were also measured for the same systems at atmospheric pressure with a circulation still, and the liquid and condensed vapor phase samples were analyzed with a gas chromatograph. The experimental data were correlated with a Wilson activity coefficient model. Experimental results and the fitted model were also compared with the predictive activity coefficient model UNIFAC (Dortmund).
Compounds
# Formula Name
1 C8H16 2,4,4-trimethyl-1-pentene
2 C4H10O butan-2-ol
3 C4H10O 2-methylpropan-2-ol
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
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:4
  • 1
  • POMD
  • 1
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:8
  • 2
  • POMD
  • 2
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:4
  • 1
  • POMD
  • 2
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:8
  • 1
  • POMD
  • 3
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:4
  • 1
  • POMD
  • 3
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:8
  • 1
  • POMD
  • 3
  • 1
  • Excess molar enthalpy (molar enthalpy of mixing), kJ/mol ; Liquid
  • Mole fraction - 3; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Flow calorimetry
  • 22
  • POMD
  • 3
  • 1
  • Azeotropic composition: mole fraction - 3 ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • By X=Y
  • 1
  • POMD
  • 3
  • 1
  • Azeotropic composition: mole fraction - 3 ; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • By X=Y
  • 1
  • POMD
  • 3
  • 1
  • Boiling temperature at pressure P, K ; Liquid
  • Mole fraction - 3; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:8
  • 24
  • POMD
  • 3
  • 1
  • Mole fraction - 3 ; Gas
  • Mole fraction - 3; Liquid
  • Pressure, kPa; Liquid
  • Gas
  • Liquid
  • CHROM:UFactor:2
  • 24
  • POMD
  • 2
  • 1
  • Excess molar enthalpy (molar enthalpy of mixing), kJ/mol ; Liquid
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Flow calorimetry
  • 20
  • POMD
  • 2
  • 1
  • Azeotropic composition: mole fraction - 2 ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • By X=Y
  • 1
  • POMD
  • 2
  • 1
  • Azeotropic composition: mole fraction - 2 ; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • By X=Y
  • 1
  • POMD
  • 2
  • 1
  • Boiling temperature at pressure P, K ; Liquid
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:8
  • 29
  • POMD
  • 2
  • 1
  • Mole fraction - 2 ; Gas
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Gas
  • Liquid
  • CHROM:UFactor:2
  • 29