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

Comparison between Experimental and Theoretical Estimations of the Thermal Expansion, Concentration Expansion Coefficients, and Viscosity for Binary Mixtures under Pressures up to 20 MPa

Bataller, H.[Henri], Miqueu, C.[Christelle], Plantier, F.[Frederic], Daridon, J. L.[Jean-Luc], Jaber, T. J.[Tawfiq J.], Abbasi, A.[Alireza], Saghir, M. Z., Bou-Ali, M. M.
J. Chem. Eng. Data 2009, 54, 6, 1710-1715
ABSTRACT
In this work, we have measured the densities of binary mixtures of n-dodecane, 1-phenyl-2-methylpropane, and 1,2,3,4-tetrahydronaphthalene for pressures varying from (0.1 to 20) MPa at an average temperature of 25 deg C. By a derivative method, we have determined the thermal expansion and concentration expansion coefficients for binary mixtures of equal mass fraction. In addition, viscosities have been measured and compared with theoretical estimates. To accurately predict the thermal expansion and concentration expansion coefficients, the densities of the binary mixtures were calculated using PC-SAFT, Peng-Robinson, and volume translated Peng-Robinson equations of state. The comparison with measured densities showed that PCSAFT has a better agreement with experimental data than the other equations of state. From calculated densities we evaluated the thermal expansion and concentration expansion variation coefficients. We have found that PC-SAFT gives a suitable prediction for the two derivative properties unlike the two other equations of state. The combination of the model of Lohrenz-Bray-Clark for the viscosity of liquid mixtures and the densities calculated with the three equations of state gave a poor prediction of the viscosities of the binary mixtures.
Compounds
# Formula Name
1 C10H12 1,2,3,4-tetrahydronaphthalene
2 C12H26 dodecane
3 C10H14 (2-methylpropyl)benzene
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
  • 2
  • 3
  • Viscosity, Pa*s ; Liquid
  • Pressure, kPa; Liquid
  • Mass fraction - 2; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Falling or rolling sphere viscometry
  • 3
  • POMD
  • 2
  • 3
  • Mass density, kg/m3 ; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Mass fraction - 2; Liquid
  • Liquid
  • Vibrating tube method
  • 55
  • POMD
  • 2
  • 3
  • Mass density, kg/m3 ; Liquid
  • Pressure, kPa; Liquid
  • Mass fraction - 3; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Vibrating tube method
  • 55
  • POMD
  • 2
  • 1
  • Viscosity, Pa*s ; Liquid
  • Pressure, kPa; Liquid
  • Mass fraction - 2; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Falling or rolling sphere viscometry
  • 3
  • POMD
  • 2
  • 1
  • Mass density, kg/m3 ; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Mass fraction - 2; Liquid
  • Liquid
  • Vibrating tube method
  • 55
  • POMD
  • 2
  • 1
  • Mass density, kg/m3 ; Liquid
  • Pressure, kPa; Liquid
  • Mass fraction - 1; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Vibrating tube method
  • 55
  • POMD
  • 1
  • 3
  • Viscosity, Pa*s ; Liquid
  • Pressure, kPa; Liquid
  • Mass fraction - 1; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Falling or rolling sphere viscometry
  • 3
  • POMD
  • 1
  • 3
  • Mass density, kg/m3 ; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Mass fraction - 1; Liquid
  • Liquid
  • Vibrating tube method
  • 55
  • POMD
  • 1
  • 3
  • Mass density, kg/m3 ; Liquid
  • Pressure, kPa; Liquid
  • Mass fraction - 1; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Vibrating tube method
  • 55