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

Diffusion Coefficients of Aromatic Compounds at Infinite Dilution in Binary Mixtures at 298.15 K

Safi, A.[Amor], Nicolas, C.[Christophe], Neau, E.[Evelyne], Chevalier, J.-L.[Jean-Louis]
J. Chem. Eng. Data 2007, 52, 1, 126-130
ABSTRACT
Infinite dilution diffusion coefficients of aromatic compounds (benzene, toluene, chlorobenzene, ethylbenzene, p-chlorotoluene, naphthalene, pyrene, and perylene) in mixtures of hexane + heptane and of benzene in polar mixtures (hexane + ethanol and acetone + ethanol) were measured at 298.15 K by the Taylor dispersion technique. Experimental data were correlated by means of literature models depending in most cases on the diffusion coefficient D1p yen of the solute at infinite dilution in the pure solvent. It is shown that the use of experimental values for D1p yen should always be preferred to the Wilke-Chang predictions, especially in the case of nonideal mixed solvents. All models provide equivalent predictions except the Maxwell-Stefan and Dullien-Asfour equations, which lead to less stable results.
Compounds
# Formula Name
1 C6H6 benzene
2 C6H5Cl chlorobenzene
3 C8H10 ethylbenzene
4 C7H8 toluene
5 C7H7Cl 4-chlorotoluene
6 C10H8 naphthalene
7 C16H10 pyrene
8 C20H12 perylene
9 C6H14 hexane
10 C7H16 heptane
11 C2H6O ethanol
12 C3H6O acetone
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
  • 10
  • Tracer diffusion coefficient, m2/s - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 1; Liquid
  • Liquid
  • OTHER::sMethod:Taylor dispersion
  • 1
  • POMD
  • 1
  • 9
  • Tracer diffusion coefficient, m2/s - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 1; Liquid
  • Liquid
  • OTHER::sMethod:Taylor dispersion
  • 1
  • POMD
  • 2
  • 10
  • Tracer diffusion coefficient, m2/s - 2 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 2; Liquid
  • Liquid
  • OTHER::sMethod:Taylor dispersion
  • 1
  • POMD
  • 2
  • 9
  • Tracer diffusion coefficient, m2/s - 2 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 2; Liquid
  • Liquid
  • OTHER::sMethod:Taylor dispersion
  • 1
  • POMD
  • 3
  • 10
  • Tracer diffusion coefficient, m2/s - 3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 3; Liquid
  • Liquid
  • Taylor dispersion
  • 1
  • POMD
  • 3
  • 9
  • Tracer diffusion coefficient, m2/s - 3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 3; Liquid
  • Liquid
  • OTHER::sMethod:Taylor dispersion
  • 1
  • POMD
  • 4
  • 10
  • Tracer diffusion coefficient, m2/s - 4 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 4; Liquid
  • Liquid
  • Taylor dispersion
  • 1
  • POMD
  • 4
  • 9
  • Tracer diffusion coefficient, m2/s - 4 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 4; Liquid
  • Liquid
  • OTHER::sMethod:Taylor dispersion
  • 1
  • POMD
  • 5
  • 10
  • Tracer diffusion coefficient, m2/s - 5 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 5; Liquid
  • Liquid
  • OTHER::sMethod:Taylor dispersion
  • 1
  • POMD
  • 5
  • 9
  • Tracer diffusion coefficient, m2/s - 5 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 5; Liquid
  • Liquid
  • OTHER::sMethod:Taylor dispersion
  • 1
  • POMD
  • 6
  • 10
  • Tracer diffusion coefficient, m2/s - 6 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 6; Liquid
  • Liquid
  • OTHER::sMethod:Taylor dispersion
  • 1
  • POMD
  • 6
  • 9
  • Tracer diffusion coefficient, m2/s - 6 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 6; Liquid
  • Liquid
  • OTHER::sMethod:Taylor dispersion
  • 1
  • POMD
  • 7
  • 10
  • Tracer diffusion coefficient, m2/s - 7 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 7; Liquid
  • Liquid
  • OTHER::sMethod:Taylor dispersion
  • 1
  • POMD
  • 9
  • 7
  • Tracer diffusion coefficient, m2/s - 7 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 7; Liquid
  • Liquid
  • OTHER::sMethod:Taylor dispersion
  • 1
  • POMD
  • 10
  • 8
  • Tracer diffusion coefficient, m2/s - 8 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 8; Liquid
  • Liquid
  • OTHER::sMethod:Taylor dispersion
  • 1
  • POMD
  • 9
  • 8
  • Tracer diffusion coefficient, m2/s - 8 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 8; Liquid
  • Liquid
  • OTHER::sMethod:Taylor dispersion
  • 1
  • POMD
  • 11
  • 1
  • Tracer diffusion coefficient, m2/s - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 1; Liquid
  • Liquid
  • OTHER::sMethod:Taylor dispersion
  • 1
  • POMD
  • 12
  • 1
  • Tracer diffusion coefficient, m2/s - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 1; Liquid
  • Liquid
  • OTHER::sMethod:Taylor dispersion
  • 1
  • POMD
  • 1
  • 9
  • 10
  • Tracer diffusion coefficient, m2/s - 1 ; Liquid
  • Solvent: Mole fraction - 9; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 1; Liquid
  • Liquid
  • Taylor dispersion
  • 11
  • POMD
  • 2
  • 9
  • 10
  • Tracer diffusion coefficient, m2/s - 2 ; Liquid
  • Solvent: Mole fraction - 9; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 2; Liquid
  • Liquid
  • Taylor dispersion
  • 11
  • POMD
  • 3
  • 9
  • 10
  • Tracer diffusion coefficient, m2/s - 3 ; Liquid
  • Solvent: Mole fraction - 9; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 3; Liquid
  • Liquid
  • Taylor dispersion
  • 11
  • POMD
  • 4
  • 9
  • 10
  • Tracer diffusion coefficient, m2/s - 4 ; Liquid
  • Solvent: Mole fraction - 9; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 4; Liquid
  • Liquid
  • Taylor dispersion
  • 11
  • POMD
  • 5
  • 9
  • 10
  • Tracer diffusion coefficient, m2/s - 5 ; Liquid
  • Solvent: Mole fraction - 9; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 5; Liquid
  • Liquid
  • Taylor dispersion
  • 11
  • POMD
  • 6
  • 9
  • 10
  • Tracer diffusion coefficient, m2/s - 6 ; Liquid
  • Solvent: Mole fraction - 9; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 6; Liquid
  • Liquid
  • Taylor dispersion
  • 11
  • POMD
  • 9
  • 7
  • 10
  • Tracer diffusion coefficient, m2/s - 7 ; Liquid
  • Solvent: Mole fraction - 9; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 7; Liquid
  • Liquid
  • Taylor dispersion
  • 11
  • POMD
  • 9
  • 10
  • 8
  • Tracer diffusion coefficient, m2/s - 8 ; Liquid
  • Solvent: Mole fraction - 9; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 8; Liquid
  • Liquid
  • Taylor dispersion
  • 11
  • POMD
  • 11
  • 1
  • 9
  • Tracer diffusion coefficient, m2/s - 1 ; Liquid
  • Solvent: Mole fraction - 9; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 1; Liquid
  • Liquid
  • Taylor dispersion
  • 10
  • POMD
  • 11
  • 12
  • 1
  • Tracer diffusion coefficient, m2/s - 1 ; Liquid
  • Solvent: Mole fraction - 12; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 1; Liquid
  • Liquid
  • Taylor dispersion
  • 10