Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Excess Gibbs energies and volumes of the ternary system ethanol + dimethylformamide + tetrahydrofuran at 298.15K

Gianni, P., Lepori, L., Matteoli, E., Righetti, M. C.
Fluid Phase Equilib. 2013, 356, 157-167
ABSTRACT
Density measurements have been carried out by means of a vibrating tube densimeter for the ternary system ethanol (EtOH) + dimethylformamide (DMF) + tetrahydrofuran (THF) and for the binary mixturescontaining DMF. For the same ternary system and for the binary DMF + THF vapour-liquid equilibrium data have been collected by head-space gas-chromatographic analysis of the vapour phase directly withdrawn from an equilibration apparatus. All experiments have been conducted at 298.15 K. Molar excess Gibbs energies GE and volumes VE, as well as activity coefficients gamma_i and excess apparent molar volumes of the components, have been obtained from the measured quantities. Both binaries involving THF show positive deviations from ideality for GE, while slightly negative deviations are exhibited by EtOH + DMF. The GE's and ln (gamma_i) of the ternary system are positive almost throughout due to destruction upon mixing of H-bonding in EtOH and dipolar interactions in DMF and THF pure liquids. Feeble negative VE's are displayed by the binaries involving DMF, whereas EtOH + THF shows an S-shaped curve with very small VE values. As a consequence, the VE's and excess apparent molar volumes of the ternary system, differently from GEand ln (gamma_i),are negative nearly over the whole composition domain suggesting a more ordered structure in solution,namely that EtOH-DMF association prevails on EtOH and DMF self-association.
Compounds
# Formula Name
1 C3H7NO dimethylformamide
2 C4H8O tetrahydrofuran
3 C2H6O ethanol
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
  • Mole fraction - 1 ; Gas
  • Mole fraction - 1; Liquid
  • Temperature, K; Liquid
  • Gas
  • Liquid
  • Chromatography
  • 19
  • POMD
  • 1
  • 2
  • Excess molar volume, m3/mol ; Liquid
  • Mole fraction - 1; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Calculated with densities of this investigation
  • 12
  • POMD
  • 3
  • 1
  • 2
  • Mole fraction - 3 ; Gas
  • Mole fraction - 3; Liquid
  • Mole fraction - 1; Liquid
  • Temperature, K; Gas
  • Gas
  • Liquid
  • Chromatography
  • 39
  • POMD
  • 3
  • 1
  • 2
  • Mole fraction - 1 ; Gas
  • Mole fraction - 3; Liquid
  • Mole fraction - 1; Liquid
  • Temperature, K; Gas
  • Gas
  • Liquid
  • Chromatography
  • 39
  • POMD
  • 3
  • 1
  • Excess molar volume, m3/mol ; Liquid
  • Volume fraction - 3; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Calculated with densities of this investigation
  • 15