Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Thermodynamic models for determination of the solubility of 2, 5-bis(2-furylmethylidene) cyclopentan-1-one in different solvents at temperatures ranging from 308.15 to 403.15 K.

Prapasawat, T.[Tatchanok], Hronec, M.[Milan], Stolcova, M.[Magdalena], Lothongkum, A. W.[Anchaleeporn Waritswat], Pancharoen, U.[Ura], Phatanasri, S.[Suphot]
Fluid Phase Equilib. 2014, 367, 57-62
ABSTRACT
The solubility data of 2,5-bis(2-furylmethylidene)cyclopentan-1-one (F2C) in solid-liquid equilibrium in alternative solvents are vital for a preliminary study of industrial applications aimed at producing sustainable and renewable materials and fuels. The solubility behavior of F2C in different solvents such as tetrahydrofuran, mixed water-tetrahydrofuran, methanol and water at temperatures ranging from 308.15 to 403.15 K was investigated. An isothermal method was employed to measure the solubility data of F2C. The experimental data showed that the solubility of F2C increased as the temperature increased and was strongly affected by the surface tension and polarity index. The solubility of F2C in the studied solvents increased in the following order: H2O less than methanol less than H2O-THF mixture less than THF. The thermodynamic models, such as the polynomial empirical equation, the Van't Hoff and the modified Apelblat models were investigated to describe the experimental data. It was found that the modified Apelblat model was the most suitable for predicting the solubility behavior of F2C with a temperature increment. The calculated thermodynamic parameters indicated that in each studied solvent the dissolution process of F2C is endothermic and spontaneous.
Compounds
# Formula Name
1 C15H12O3 cyclopentanone, 2,5-bis(2-furanylmethylene)-
2 CH4O methanol
3 C4H8O tetrahydrofuran
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
  • 3
  • 1
  • Mole fraction - 1 ; Liquid mixture 1
  • Temperature, K; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • Chromatography
  • 12
  • POMD
  • 3
  • 1
  • 4
  • Mole fraction - 1 ; Liquid mixture 1
  • Temperature, K; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Solvent: Volume fraction - 3; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • Chromatography
  • 11
  • POMD
  • 2
  • 1
  • Mole fraction - 1 ; Liquid mixture 1
  • Temperature, K; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • Chromatography
  • 9
  • POMD
  • 1
  • 4
  • Mole fraction - 1 ; Liquid mixture 1
  • Temperature, K; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • Chromatography
  • 7