Thermodynamics Research Center / ThermoML | Journal of Chemical Thermodynamics

Phase equilibria for ternary liquid systems of (water + levulinic acid + cyclic solvent) at T = 298.2 K: Thermodynamic modeling

Senol, A.[Aynur]
J. Chem. Thermodyn. 2005, 37, 10, 1104-1110
ABSTRACT
(Liquid + liquid) equilibrium (LLE) data of the solubility curves and tie-line end compositions are presented for mixtures of {water (1) + levulinic acid (2) + methylcyclohexanol, or cyclohexanone, or cyclohexyl acetate (3)} at T = 298.2 K and P = (101.3 +- 0.7) kPa. Among the studied C6 ring-containing cyclic solvents, methylcyclohexanol and cyclohexyl acetate give the largest distribution ratio and separation factors for extraction of levulinic acid. A solvation energy relation (SERLAS) has been used to estimate the (liquid + liquid) equilibria of associated systems containing components capable of a physical interaction through hydrogen bonding. The tie-lines were also predicted using the UNIFAC-original model. The reliability of both models has been analyzed against the LLE data with respect to the distribution ratio and separation factor. SERLAS matches LLE data quite accurately, yielding a mean error of 3.6% for all the systems considered.
Compounds
# Formula Name
1 C6H10O cyclohexanone
2 C8H14O2 cyclohexyl ethanoate
3 C5H8O3 4-oxopentanoic acid
4 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
  • 4
  • Mass fraction - 4 ; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Temperature, K; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • TITR:UFactor:4
  • 1
  • POMD
  • 1
  • 4
  • Mass fraction - 4 ; Liquid mixture 2
  • Temperature, K; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 2
  • Liquid mixture 1
  • TITR:UFactor:4
  • 1
  • POMD
  • 2
  • 4
  • Mass fraction - 4 ; Liquid mixture 1
  • Temperature, K; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • TITR:UFactor:4
  • 1
  • POMD
  • 2
  • 4
  • Mass fraction - 4 ; Liquid mixture 2
  • Temperature, K; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 2
  • Liquid mixture 1
  • TITR:UFactor:4
  • 1
  • POMD
  • 1
  • 3
  • 4
  • Mass fraction - 3 ; Liquid mixture 1
  • Mass fraction - 4 ; Liquid mixture 2
  • Mass fraction - 3 ; Liquid mixture 2
  • Mass fraction - 4; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Temperature, K; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • TITR:UFactor:4
  • TITR:UFactor:4
  • TITR:UFactor:4
  • 5
  • POMD
  • 3
  • 2
  • 4
  • Mass fraction - 3 ; Liquid mixture 1
  • Mass fraction - 4 ; Liquid mixture 2
  • Mass fraction - 3 ; Liquid mixture 2
  • Mass fraction - 4; Liquid mixture 1
  • Temperature, K; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • TITR:UFactor:4
  • TITR:UFactor:4
  • TITR:UFactor:4
  • 6