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

Excess Molar Enthalpies for the Binary Systems of Benzene or Cyclohexane with 1,1-Diethoxyethane at 323.15 K or with 2,2-Dimethoxybutane at 303.15 K and Infinite Dilution Activity Coefficients in 1,1-Diethoxyethane

Teodorescu, M.[Mariana], Krummen, M.[Michael], Gmehling, J.[Juergen]
J. Chem. Eng. Data 2003, 48, 2, 435-439
ABSTRACT
Excess molar enthalpies, HE, for the binary systems of benzene or cyclohexane with 1,1-diethoxyethane at 323.15 K and with 2,2-dimethoxybutane at 303.15 K are presented. Additionally, infinite dilution activity coefficients for benzene and cyclohexane in 1,1-diethoxyethane have been measured between 293.08 and 323.15 K. The heat of mixing measurements have been carried out by means of a commercially available flow calorimeter Hart Scientific (model 7501) with an estimated accuracy of better than +- 1% over the whole composition range. For the description of the experimental data a Redlich-Kister polynomial was used. The infinite dilution activity coefficients have been measured using the dilutor technique. The experimental results were compared with those predicted by Modified UNIFAC (Dortmund) using the available interaction parameters for the "ether" group. The aim of this work is to supplement the available data base for acetal systems required for the introduction the new "acetal" group in modified UNIFAC (Dortmund).
Compounds
# Formula Name
1 C6H6 benzene
2 C6H12 cyclohexane
3 C6H14O2 2,2-dimethoxybutane
4 C6H14O2 1,1-diethoxyethane
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
  • 4
  • Excess molar enthalpy (molar enthalpy of mixing), kJ/mol ; Liquid
  • Mole fraction - 1; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Flow calorimetry
  • 19
  • POMD
  • 1
  • 4
  • Activity coefficient - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 1; Liquid
  • Liquid
  • OTHER
  • 4
  • POMD
  • 1
  • 3
  • Excess molar enthalpy (molar enthalpy of mixing), kJ/mol ; Liquid
  • Mole fraction - 1; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Flow calorimetry
  • 18
  • POMD
  • 4
  • 2
  • Excess molar enthalpy (molar enthalpy of mixing), kJ/mol ; Liquid
  • Mole fraction - 2; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Flow calorimetry
  • 19
  • POMD
  • 4
  • 2
  • Activity coefficient - 2 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 2; Liquid
  • Liquid
  • OTHER
  • 4
  • POMD
  • 2
  • 3
  • Excess molar enthalpy (molar enthalpy of mixing), kJ/mol ; Liquid
  • Mole fraction - 2; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Flow calorimetry
  • 19