Thermodynamics Research Center / ThermoML | Journal of Chemical Thermodynamics

Excess molar enthalpies and volumes of binary mixtures of nonafluorobutylmethylether with ethylene glycol ethers at T = 298.15 K

Minamihonoki, T.[Takashi], Ogawa, H.[Hideo], Murakami, S.[Sachio], Nomura, H.[Hiroyasu]
J. Chem. Thermodyn. 2005, 37, 11, 1186-1195
ABSTRACT
Excess molar enthalpies, HEm and volumes, VEm were reported for binary mixtures of {nonafluorobutylmethylether, (NFBME-C4F9-O-CH3)} + [five ethylene glycol ethers, EGEn,m-R, {CmH2m + 1-(OCH2CH2)n-R, n = 1 and 2, m = 1 to 4, R = OH andOCH3}] at 298.15 K. Results of excess molar enthalpies and volumes were positive over whole range of concentrations for all the mixtures. The magnitude was in order: EGE1,4-OH > EGE1,3-OH > EGE1,2-OH> EGE1,1-OH > EGE2,1-OH > EGE2,1-OCH3 for HEm and EGE2,1-OCH3 > EGE1,4-OH>EGE1,3-OH> EGE1,2-OH > EGE1,1-OH > EGE2,1-OH for V Em at the maximum point. The curves of HEm and V Em for the EGE2,1-OH system were depressed in the middle mole fraction of NFBME, x1 suggesting a quasi-stable state in the solution. We observed occurrences of the stable emulsification state in solutions in concentrations range of 0.35 < x1 < 0.55. From these results, excess partial molar enthalpies, HE;1 m;2, and volumes, V E;1 m;2 , of EGEn,m-R at infinite dilution, apparent molar enthalpies of solvation, DsolvH2, of the EGEn,m-R in NFBME were evaluated. The dependence of these thermodynamic quantities on the number of carbon atoms in the alkyl group, m, the number of the ethylene oxide group, n, and the difference of R group were discussed in consideration of various kinds of intermolecular interactions in pure component liquids and solutions.
Compounds
# Formula Name
1 C5H3F9O 1-methoxy-nonafluorobutane
2 C3H8O2 2-methoxyethan-1-ol
3 C4H10O2 2-ethoxyethan-1-ol
4 C6H14O2 2-butoxyethan-1-ol
5 C5H12O3 2-(2-methoxyethoxy)ethanol
6 C6H14O3 2,5,8-trioxanonane
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
  • 2
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:4
  • 1
  • POMD
  • 3
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB::UFactor:4
  • 1
  • POMD
  • 4
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB::UFactor:4
  • 1
  • POMD
  • 5
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB::UFactor:4
  • 1
  • POMD
  • 6
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:4
  • 1
  • POMD
  • 2
  • 1
  • Excess molar enthalpy (molar enthalpy of mixing), kJ/mol ; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • FLOW:UFactor:2
  • 16
  • POMD
  • 2
  • 1
  • Mass density, kg/m3 ; Liquid
  • Mole fraction - 1; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:4
  • 31
  • POMD
  • 3
  • 1
  • Excess molar enthalpy (molar enthalpy of mixing), kJ/mol ; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • FLOW:UFactor:2
  • 17
  • POMD
  • 3
  • 1
  • Mass density, kg/m3 ; Liquid
  • Mole fraction - 1; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:4
  • 31
  • POMD
  • 4
  • 1
  • Excess molar enthalpy (molar enthalpy of mixing), kJ/mol ; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • FLOW:UFactor:2
  • 16
  • POMD
  • 4
  • 1
  • Mass density, kg/m3 ; Liquid
  • Mole fraction - 1; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:4
  • 23
  • POMD
  • 5
  • 1
  • Excess molar enthalpy (molar enthalpy of mixing), kJ/mol ; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • FLOW:UFactor:2
  • 14
  • POMD
  • 5
  • 1
  • Mass density, kg/m3 ; Liquid
  • Mole fraction - 1; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:4
  • 19
  • POMD
  • 6
  • 1
  • Excess molar enthalpy (molar enthalpy of mixing), kJ/mol ; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • FLOW:UFactor:2
  • 14
  • POMD
  • 6
  • 1
  • Mass density, kg/m3 ; Liquid
  • Mole fraction - 1; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:4
  • 23