Thermodynamics Research Center / ThermoML | Journal of Chemical Thermodynamics

(p,rho,T,x) and viscosity measurements of {x1 n-heptane + (1 - x1) n-octane} mixtures at high temperatures and high pressures

Abdulagatov, I. M., Azizov, N. D.
J. Chem. Thermodyn. 2006, 38, 11, 1402-1415
ABSTRACT
Density and viscosity measurements are reported for {x1n-heptane + (1 x1)n-octane} mixtures at x1 = (0.2808, 0.5427, 0.7906). The measurements of density and viscosity were made with a constant-volume piezometer immersed in a precision liquid thermostat and a capillary flow technique, respectively. Measurements were made at pressures up to 10 MPa. The range of temperature was (293 to 557) K for the density measurements and (298 to 473) K for the viscosity measurements. The total uncertainty of density, viscosity, pressure, temperature, and composition measurements was estimated to be less than 0.06%, 1.6%, 0.05%, 15 mK, and 0.02%, respectively. The effect of temperature, pressure, and concentration on density and viscosity of the binary {x1n-heptane + (1 x1)n-octane} mixtures was studied. The measured values of density and viscosity for the pure components and mixtures were compared with those generated by reference equations and prediction techniques for the mixtures. The excess molar volumes V E m and the viscosity deviations Dg were derived using the measured values of density and viscosity for the mixtures and pure components. The viscosity data have been interpreted in terms of the Grunberg Nissan equation for binary mixtures. The temperature dependence of the Grunberg Nissan constant was studied using the present viscosity data. The molar excess Gibbs energy of activation for flow DEa was also calculated from our experimental viscosity data for the (n-heptane + n-octane) mixtures.
Compounds
# Formula Name
1 C8H18 octane
2 C7H16 heptane
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
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Capillary tube (Ostwald; Ubbelohde) method
  • 13
  • POMD
  • 1
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • ISOCHOR
  • 13
  • POMD
  • 2
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Capillary tube (Ostwald; Ubbelohde) method
  • 15
  • POMD
  • 2
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • ISOCHOR
  • 13
  • POMD
  • 1
  • 2
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 2; Liquid
  • Liquid
  • Capillary tube (Ostwald; Ubbelohde) method
  • 122
  • POMD
  • 1
  • 2
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 2; Liquid
  • Liquid
  • ISOCHOR
  • 141