Thermodynamics Research Center / ThermoML | Journal of Chemical Thermodynamics

Measurement of the phase behaviour of the binary systems {carbon dioxide (CO2) + non-ionic surfactants (CiEOj)}

Sandoval, T. E.[Tania E.], Garate, M. P.
J. Chem. Thermodyn. 2012, 45, 1, 109-113
ABSTRACT
Solubility experiments of ethoxylates surfactants denoted as CiEOj (where Ci = hydrocarbon tail, EOj = oxyethylene groups, i = 6 to 8 and j = 3 to 5) in sub- and supercritical carbon dioxide were carried out at different temperatures, pressures, and concentrations in a Cailletet apparatus as a representative model for dry cleaning system. For a variety of compositions, results are reported for binary systems within temperature and pressure ranges of (260 to 310) K and (2.0 to 10) MPa respectively. In each experiment, the surfactants reach equilibrium with carbon dioxide at different concentrations. The data show that with all the surfactants upon increasing concentration, the liquid liquid (L-L) curve shifts to lower temperatures. Therefore, the one-phase solution gap is reduced in pressure and temperature at higher concentrations. When the length of the hydrocarbon tail remains constant and the ethoxylated chain is increased from three to five groups, the L-L curve once again shifts to lower temperatures and the two phases start earlier. This effect can be attributed to the higher surfactant's polarity due to the increase in j. On the other hand, when the number of ethoxylated groups j remains constant and the length of the hydrocarbon tail is increased from six to eight carbon atoms, no significant shift in the L-L curve is observed. That signals the fact that the appearance of two phases is directly related to the number of ethoxylated groupwhich determine the polarity of the molecule.
Compounds
# Formula Name
1 C14H30O4 2-[2-[2-(octyloxy)ethoxy]ethoxy]ethanol
2 C18H38O6 3,6,9,12,15-pentaoxatricosan-1-ol
3 C16H34O6 2-(hexyloxytetraethoxy)ethanol
4 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
  • 4
  • 1
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 1; Liquid
  • Liquid
  • Gas
  • Cailletet apparatus
  • 41
  • POMD
  • 4
  • 1
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Mole fraction - 1; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS
  • 31
  • POMD
  • 4
  • 2
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 2; Liquid
  • Liquid
  • Gas
  • Cailletet apparatus
  • 18
  • POMD
  • 4
  • 2
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Mole fraction - 2; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS
  • 36
  • POMD
  • 4
  • 3
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 3; Liquid
  • Liquid
  • Gas
  • Cailletet apparatus
  • 20
  • POMD
  • 4
  • 3
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Mole fraction - 3; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS
  • 31