Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Temperature dependence of the excess molar volume of 1-hexanol + 1-alkene systems in terms of an association and equation of state model

Treszczanowicz, A.[Andrzej], Pawlowski, T. S.[Tomasz S.], Treszczanowicz, T.[Teresa]
Fluid Phase Equilib. 2010, 295, 2, 155-162
ABSTRACT
Excess molar volumes VE measured at 288.15 and 308.15 K for (1-hexanol + 1-hexene), (1-hexanol + 1-octene) and (1-hexanol + 1-decene) systems are reported. The data and the measurements reported before at 298.15 K for this series of mixtures were used to estimate the excess molar isobaric thermal expansion and the partial molar excess isobaric thermal expansions of the components at 298.15 K. The excess molar isobaric thermal expansion as a function of concentration, changes from positive negative for the systems formed by short-chain 1-alkenes like 1-hexene to positive for 1-decene over the whole concentration range. The modified Treszczanowicz and Benson model (TB) is applied to interpret and to predict changes in the size and shape of the excess molar isobaric thermal expansion and partial molar excess isobaric thermal expansions curves. The model predicts qualitatively well the changes of the excess molar isobaric thermal expansion and partial molar excess isobaric thermal expansions values in the series of mixtures as a superposition of the contributions due to self-association of alkanol, free volume, OH...pi interactions and residual van der Waals interactions. These contributions to the properties investigated are estimated and discussed in the series of mixtures. The results obtained are compared with those for 1-alkanol + n-alkane systems.
Compounds
# Formula Name
1 C6H14O hexan-1-ol
2 C6H12 hex-1-ene
3 C8H16 oct-1-ene
4 C10H20 1-decene
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
  • 2
  • Excess molar volume, m3/mol ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Calculated with densities of this investigation
  • 32
  • POMD
  • 1
  • 3
  • Excess molar volume, m3/mol ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Calculated with densities of this investigation
  • 35
  • POMD
  • 1
  • 4
  • Excess molar volume, m3/mol ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Calculated with densities of this investigation
  • 32