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

Density, Viscosity, Vapor-Liquid Equilibrium, Excess Molar Volume, Viscosity Deviation, and Their Correlations for the Chloroform + 2-Butanone Binary System

Clara, R. A.[Rene A.], Marigliano, A. C. G.[Ana C. Gomez], Solimo, H. N.[Horacio N.]
J. Chem. Eng. Data 2006, 51, 4, 1473-1478
ABSTRACT
Density and viscosity measurements for pure trichloromethane and 2-butanone as well as for trichloromethane (1) + 2-butanone (2) were made at (283.15, 293.15, 303.15, and 313.15) K over the whole concentration range. The experimental results were fitted to empirical equations, which permit the calculation of these properties in the whole concentration range and in the studied range of temperatures. The calculated values are in good agreement with the experimental ones. Data of the binary mixture were further used to calculate the excess molar volume and viscosity deviation. Vapor-liquid equilibrium (VLE) at T ) 303.15 K for this binary system was also measured in order to calculate the activity coefficients and the excess molar Gibbs function. This binary system shows negative deviations from ideal behavior and forms a minimum pressure azeotrope at x1 ) 0.199 and p ) 15.3 kPa. The excess or deviation properties were fitted by the Redlich-Kister polynomial relation to obtain their coefficients and standard deviations.
Compounds
# Formula Name
1 CHCl3 trichloromethane
2 C4H8O butanone
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
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:4
  • 1
  • POMD
  • 1
  • Refractive index (Na D-line) ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Standard Abbe refractometry
  • 4
  • POMD
  • 1
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • CAPTUB:UFactor:2
  • 4
  • POMD
  • 1
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:2
  • 4
  • POMD
  • 2
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • EBULLIO::UFactor:4
  • 1
  • POMD
  • 2
  • Refractive index (Na D-line) ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Standard Abbe refractometry
  • 4
  • POMD
  • 2
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • CAPTUB::UFactor:2
  • 4
  • POMD
  • 2
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB::UFactor:2
  • 4
  • POMD
  • 1
  • 2
  • Vapor or sublimation pressure, kPa ; Liquid
  • Mole fraction - 1; Liquid
  • Temperature, K; Gas
  • Liquid
  • Gas
  • EBULLIO:UFactor:4
  • 22
  • POMD
  • 1
  • 2
  • Mole fraction - 1 ; Gas
  • Mole fraction - 1; Liquid
  • Temperature, K; Gas
  • Gas
  • Liquid
  • Density calibration data
  • 22
  • POMD
  • 1
  • 2
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • CAPTUB:UFactor:2
  • 48
  • POMD
  • 1
  • 2
  • Mass density, kg/m3 ; Liquid
  • Mole fraction - 1; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:2
  • 48