Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Solubility of flavone, 6-methoxyflavone and anthracene in supercritical CO2 with/without a co-solvent of ethanol correlated by using a newly proposed entropy-based solubility parameter

Ota, M.[Masaki], Hashimoto, Y.[Yoshiaki], Sato, M.[Megumi], Sato, Y.[Yoshiyuki], Smith, R. L.[Richard Lee], Inomata, H.[Hiroshi]
Fluid Phase Equilib. 2016, 425, 65-71
ABSTRACT
Solubility of flavone, 6-methoxyflavone and anthracene in supercritical CO2 with an ethanol co-solvent ranging from 0.05 to 0.40 were measured at 333 K and 22.0 MPa. Solubility of each compound increased with increasing mole fraction of ethanol. Solubility data were correlated with Chrastil equation considering a relationship between fluid density and solubility and compared with newly proposed relations that use an entropy-based solubility parameter (SSP). Among proposed relations, one relation taking temperature dependence into consideration, that included two fitting parameters had absolute relative deviation (ARD) of 3.9% compared to the experimental data and were much more reliable than a relation not taking temperature dependence into consideration within ARD of 7.6%. The expression similar to Chrastil model that included three fitting parameters and considered SSP was the best ARD within 3.6% among the proposed relations. From these correlation results, the SSP can be applied to determine the solubility of substances at high pressure with multicomponent solvent mixtures.
Compounds
# Formula Name
1 CO2 carbon dioxide
2 C2H6O ethanol
3 C15H10O2 flavone
4 C16H12O3 6-methoxyflavone
5 C14H10 anthracene
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
  • 2
  • 1
  • Mole fraction - 3 ; Gas
  • Mole fraction - 2; Liquid
  • Temperature, K; Gas
  • Pressure, kPa; Gas
  • Gas
  • Liquid
  • Peng-Robinson EOS
  • 3
  • POMD
  • 4
  • 2
  • 1
  • Mole fraction - 4 ; Gas
  • Mole fraction - 2; Liquid
  • Temperature, K; Gas
  • Pressure, kPa; Gas
  • Gas
  • Liquid
  • Peng-Robinson EOS
  • 3
  • POMD
  • 5
  • 2
  • 1
  • Mole fraction - 5 ; Gas
  • Mole fraction - 2; Liquid
  • Temperature, K; Gas
  • Pressure, kPa; Gas
  • Gas
  • Liquid
  • Peng-Robinson EOS
  • 6
  • POMD
  • 5
  • 1
  • Boiling temperature at pressure P, K ; Gas
  • Mole fraction - 5; Gas
  • Pressure, kPa; Gas
  • Gas
  • Liquid
  • Peng-Robinson EOS
  • 1