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

Vapor-Liquid Equilibrium in a Ternary System Cyclohexane + Ethanol + Water

Antosik, M.[Maria], Galka, M.[Maria], Malanowski, S. K.[Stanislaw]
J. Chem. Eng. Data 2004, 49, 1, 7-10
ABSTRACT
Experimental vapor-liquid equilibrium (p, T, x, y) data of the cyclohexane + ethanol + water system have been determined by an ebulliometric method at the temperatures (323, 333, and 343) K. The vapor pressures of pure components have been measured by the ebulliometric method in the range from (310 to 340) K.
Compounds
# Formula Name
1 C2H6O ethanol
2 C6H12 cyclohexane
3 H2O water
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
  • 19
  • POMD
  • 2
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:4
  • 16
  • POMD
  • 3
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:4
  • 12
  • POMD
  • 1
  • 2
  • 3
  • Mole fraction - 2 ; Liquid
  • Mole fraction - 2 ; Gas
  • Mole fraction - 1 ; Gas
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 1; Liquid
  • Liquid
  • Gas
  • DYNAMIC
  • DYNAMIC
  • DYNAMIC
  • 58