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

Liquid-Liquid Equilibria for the Ternary System Water + Acetic Acid + Propyl Acetate

Xiao, X.[Xianjiang], Wang, L., Ding, G.[Ganhong], Li, X.[Xi]
J. Chem. Eng. Data 2006, 51, 2, 582-583
ABSTRACT
In this work, we present the liquid-liquid equilibrium data of a ternary system water + acetic acid + propyl acetate, at 298.15 K, 313.15 K, and 363.65 K under atmospheric pressure. The experimental data were correlated with the UNIQUAC model, and a good agreement was obtained.
Compounds
# Formula Name
1 C2H4O2 acetic acid
2 C5H10O2 propyl ethanoate
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
  • 2
  • 3
  • Mole fraction - 1 ; Liquid mixture 2
  • Mole fraction - 1 ; Liquid mixture 1
  • Mole fraction - 3 ; Liquid mixture 1
  • Temperature, K; Liquid mixture 1
  • Mole fraction - 3; Liquid mixture 2
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 2
  • Liquid mixture 1
  • CHROM:UFactor:8
  • CHROM:UFactor:8
  • CHROM:UFactor:8
  • 19
  • POMD
  • 2
  • 3
  • Mole fraction - 3 ; Liquid mixture 2
  • Temperature, K; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 2
  • Liquid mixture 1
  • CHROM:UFactor:8
  • 1
  • POMD
  • 2
  • 3
  • Mole fraction - 3 ; Liquid mixture 1
  • Temperature, K; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • CHROM:UFactor:8
  • 1