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

Solubility of p-Aminobenzenesulfonamide in Supercritical Carbon Dioxide with Acetone Cosolvent

Jin, J.-s.[Jun-su], Pei, X.-m.[Xue-mei], Li, J.-l.[Jia-lin], Zhang, Z.-t.[Ze-ting]
J. Chem. Eng. Data 2009, 54, 1, 157-159
ABSTRACT
Using a flow-type apparatus, the solubilities of p-aminobenzenesulfonamide in supercritical carbon dioxide were determined at three different temperatures (308.15, 318.15, and 328.15) K and in the pressure range from (11.0 to 21.0) MPa. The effect of acetone cosolvent on the solubility of p-aminobenzenesulfonamide was studied at the mole percents of 3.0 % and 6.0 %. The experimental data in supercritical carbon dioxide without and with cosolvent were satisfactorily correlated with the Chrastil equation and the modified Chrastil equation.
Compounds
# Formula Name
1 C6H8N2O2S 4-aminobenzenesulfonamide
2 C3H6O acetone
3 CO2 carbon dioxide
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
  • 3
  • Mass concentration, kg/m3 ; Fluid (supercritical or subcritical phases)
  • Pressure, kPa; Fluid (supercritical or subcritical phases)
  • Temperature, K; Fluid (supercritical or subcritical phases)
  • Fluid (supercritical or subcritical phases)
  • Crystal - 1
  • flow apparatus
  • 15
  • POMD
  • 1
  • 2
  • 3
  • Mass concentration, kg/m3 - 1 ; Fluid (supercritical or subcritical phases)
  • Pressure, kPa; Fluid (supercritical or subcritical phases)
  • Solvent: Mole fraction - 2; Fluid (supercritical or subcritical phases)
  • Temperature, K; Fluid (supercritical or subcritical phases)
  • Fluid (supercritical or subcritical phases)
  • Crystal - 1
  • flow apparatus
  • 15