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

Excess Gibbs Energies of the Ternary System 2-Methoxyethanol + Tetrahydrofuran + Cyclohexane and Other Relevant Binaries at 298.15 K

Matteoli, E.[Enrico], Gianni, P.[Paolo], Lepori, L.[Luciano]
J. Chem. Eng. Data 2010, 55, 12, 5441-5448
ABSTRACT
Vapor-liquid equilibria for the ternary system 2-methoxyethanol + tetrahydrofuran + cyclohexane and for the constituent binary mixtures containing 2-methoxyethanol have been determined at 298.15 K. In addition, for a better understanding of the phenomenology, the binary mixtures 2-methoxyethanol + ethanol and 2-ethoxyethanol + cyclohexane were also investigated. Vapor-liquid equilibrium data were collected by headspace gas chromatographic analysis of the vapor phase directly withdrawn from an equilibrium apparatus. Molar excess Gibbs energies GE and activity coefficients were calculated therefrom. All binaries display positive GE deviations from ideality, the largest being observed for the binary 2-methoxyethanol + cyclohexane, as well as the ternary mixtures over the whole mole fraction range, indicating that interactions in the pure liquids are not compensated for by new interactions in the mixtures. A positive sign is also displayed by HE and VE of the ternary system, while the entropy contribution to GE, -TSE, is positive in the region rich in the binary 2-methoxyethanol + cyclohexane and negative in the region rich in tetrahydrofuran + cyclohexane. The analysis of activity coefficients allows us to point out the role of hydrogen bonds in the cross-association of alcohols with polar molecules and the self-association both in pure liquid alcohol and in mixtures with hydrocarbons.
Compounds
# Formula Name
1 C3H8O2 2-methoxyethan-1-ol
2 C2H6O ethanol
3 C4H10O2 2-ethoxyethan-1-ol
4 C4H8O tetrahydrofuran
5 C6H12 cyclohexane
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
  • Molar volume, m3/mol ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:4
  • 1
  • POMD
  • 2
  • Molar volume, m3/mol ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:4
  • 1
  • POMD
  • 3
  • Molar volume, m3/mol ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:4
  • 1
  • POMD
  • 4
  • Molar volume, m3/mol ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:4
  • 1
  • POMD
  • 5
  • Molar volume, m3/mol ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:4
  • 1
  • POMD
  • 1
  • 4
  • Mole fraction - 1 ; Gas
  • Mole fraction - 1; Liquid
  • Temperature, K; Gas
  • Gas
  • Liquid
  • CHROM:UFactor:8
  • 12
  • POMD
  • 1
  • 5
  • Mole fraction - 1 ; Gas
  • Mole fraction - 1; Liquid
  • Temperature, K; Gas
  • Gas
  • Liquid
  • CHROM:UFactor:8
  • 35
  • POMD
  • 2
  • 1
  • Mole fraction - 1 ; Gas
  • Mole fraction - 1; Liquid
  • Temperature, K; Gas
  • Gas
  • Liquid
  • CHROM:UFactor:8
  • 17
  • POMD
  • 3
  • 5
  • Mole fraction - 3 ; Gas
  • Mole fraction - 3; Liquid
  • Temperature, K; Gas
  • Gas
  • Liquid
  • CHROM:UFactor:8
  • 25
  • POMD
  • 1
  • 4
  • 5
  • Mole fraction - 1 ; Gas
  • Mole fraction - 1; Liquid
  • Mole fraction - 4; Gas
  • Temperature, K; Gas
  • Gas
  • Liquid
  • CHROM:UFactor:8
  • 56
  • POMD
  • 1
  • 4
  • 5
  • Mole fraction - 4 ; Gas
  • Mole fraction - 1; Liquid
  • Mole fraction - 4; Liquid
  • Temperature, K; Gas
  • Gas
  • Liquid
  • CHROM:UFactor:8
  • 56