Thermodynamics Research Center / ThermoML | Journal of Chemical Thermodynamics

Excess molar enthalpies and volumes of binary mixtures of nonafluorobutylmethylether with ketones at T = 298.15 K

Minamihonoki, T.[Takashi], Ogawa, H.[Hideo], Murakami, S.[Sachio], Nomura, H.[Hiroyasu]
J. Chem. Thermodyn. 2006, 38, 11, 1254-1259
ABSTRACT
Excess molar enthalpies, HE m, and volumes, V E m, were reported for binary mixtures of {nonafluorobutylmethylether, (FBME, C4F9OCH3) + 2-propanone, or + 2-butanone, or + 3-pentanone} at 298.15 K. Results of HE m and V E m were positive over a whole range of concentrations for all the mixtures. The magnitude was in order: 2-propanone > 3-pentanone > 2-butanone for HE m and 3-pentanone > 2-butanone = 2-propanone for V E m at the maximum point. However, the difference in the maximum values of HE m and V E m by the increase in the number of carbon atoms in the ketones, nC is not so large. From these results, partial molar quantities oHE;1 m;i ; V E;1 m;i ; and V1m ;iP of the i component at infinite dilution, and apparent molar enthalpies of solvation, DsolvHi of the i component were evaluated. The dependence of these thermodynamic quantities on the nC were discussed in consideration of various kinds of intermolecular interactions in pure component liquids and solutions.
Compounds
# Formula Name
1 C5H3F9O methyl nonafluoroisobutyl ether
2 C5H3F9O 1-methoxy-nonafluorobutane
3 C3H6O acetone
4 C4H8O butanone
5 C5H10O pentan-3-one
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
  • 3
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:2
  • 1
  • POMD
  • 4
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:2
  • 1
  • POMD
  • 5
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:2
  • 1
  • POMD
  • 2
  • 1
  • Mass density, kg/m3 ; Liquid
  • Mole fraction - 1; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:4
  • 1
  • POMD
  • 4
  • 2
  • 1
  • Excess molar enthalpy (molar enthalpy of mixing), kJ/mol ; Liquid
  • Mole fraction - 4; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Solvent: Mole fraction - 1; Liquid
  • Liquid
  • FLOW:UFactor:2
  • 33
  • POMD
  • 4
  • 2
  • 1
  • Mass density, kg/m3 ; Liquid
  • Mole fraction - 4; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Solvent: Mole fraction - 1; Liquid
  • Liquid
  • VIBTUB:UFactor:2
  • 21
  • POMD
  • 5
  • 2
  • 1
  • Excess molar enthalpy (molar enthalpy of mixing), kJ/mol ; Liquid
  • Mole fraction - 5; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Solvent: Mole fraction - 1; Liquid
  • Liquid
  • FLOW:UFactor:3
  • 33
  • POMD
  • 5
  • 2
  • 1
  • Mass density, kg/m3 ; Liquid
  • Mole fraction - 5; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Solvent: Mole fraction - 1; Liquid
  • Liquid
  • VIBTUB:UFactor:2
  • 26
  • POMD
  • 3
  • 2
  • 1
  • Excess molar enthalpy (molar enthalpy of mixing), kJ/mol ; Liquid
  • Mole fraction - 3; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Solvent: Mole fraction - 1; Liquid
  • Liquid
  • FLOW:UFactor:2
  • 33
  • POMD
  • 3
  • 2
  • 1
  • Mass density, kg/m3 ; Liquid
  • Mole fraction - 3; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Solvent: Mole fraction - 1; Liquid
  • Liquid
  • VIBTUB:UFactor:2
  • 28