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

Solubility of Red 153 and Blue 1 in Supercritical Carbon Dioxide

Coelho, J.[Jose], Stateva, R.[Roumiana]
J. Chem. Eng. Data 2011, 56, 12, 4686-4690
ABSTRACT
Solubilities of red 153, (3-[[4-[[5,6(or 6,7)-dichloro-2-benzothiazolyl]azo]phenyl]ethylamino]propanenitrile), an azo compound, and disperse blue 1 (1,4,5,8-tetraaminoantraquinone) in supercritical carbon dioxide (SC CO2) were measured at T = (333.2 to 393.2) K over the pressure range (12.0 to 40.0) MPa by a flow type apparatus. The solubility of red 153 (0.985*10 6 to 37.2*10 6) in the overall region of measurements is found to be significantly higher than that of disperse blue 1 (1.12*10 7 to 4.89*10 7). The solubility behavior of disperse red 153 follows the general solubility trend displayed by disperse dyes with a crossover pressure at about 20 MPa. On the other hand, blue 1, which is a disperse anthraquinone dye, exhibits unexpected behavior not recorded previously there is no crossover pressure at the temperature and pressure ranges studied, and the dye's solubility at T = 333.2 K practically does not increase with pressure. To the best of our knowledge, there are no previous measurements of blue 1 solubility in SC CO2 reported in the literature. The experimental data were correlated by using the Soave Redlich Kwong equation of state (EoS) with the one-fluid van der Waals mixing rule, and an acceptable correlation of the solubility data for both dyes was obtained.
Compounds
# Formula Name
1 C18H15Cl2N5S 3-((4-((5,6-dichlorobenzo[d]thiazol-2-yl)diazenyl)phenyl)(ethyl)amino)propanenitrile
2 C14H12N4O2 1,4,5,8-tetraamino-9,10-anthracenedione
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
  • 3
  • 1
  • Mole fraction - 1 ; Fluid (supercritical or subcritical phases)
  • Temperature, K; Fluid (supercritical or subcritical phases)
  • Pressure, kPa; Fluid (supercritical or subcritical phases)
  • Fluid (supercritical or subcritical phases)
  • Crystal - 1
  • UV-visible equipment
  • 16
  • POMD
  • 3
  • 2
  • Mole fraction - 2 ; Fluid (supercritical or subcritical phases)
  • Temperature, K; Fluid (supercritical or subcritical phases)
  • Pressure, kPa; Fluid (supercritical or subcritical phases)
  • Fluid (supercritical or subcritical phases)
  • Crystal - 2
  • UV-visible equipment
  • 18