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

Solubility of H2S in Aqueous Diisopropanolamine + Piperazine Solutions: New Experimental Data and Modeling with the Electrolyte Cubic Square-Well Equation of State

Mazloumi, S. H., Haghtalab, A., Jalili, A. H., Shokouhi, M.
J. Chem. Eng. Data 2012, 57, 10, 2625-2631
ABSTRACT
The solubilities of H2S in aqueous solutions of diisopropanolamine (DIPA) and in aqueous mixtures of DIPA and piperazine (Pz) have been measured. The molality of DIPA was fixed at 2.96 m, and the concentration of Pz was (1.20 or 1.80) m. Experiments were carried out at (40, 60, and 80) deg C over the pressure range (19 to 1554) kPa. For modeling of the DIPA + Pz + H2S + H2O system, the electrolyte cubic square well (eCSW) equation of state (EOS) (Haghtalab, A.; Mazloumi, S. H. Fluid Phase Equilib. 2009, 285, 96-104) was applied to predict the total and partial pressures of H2S over aqueous solutions of DIPA, Pz, and DIPA + Pz using only the interaction parameters, kij, of the H2S + H2O system. The reasonable agreement of the eCSW EOS and experimental results demonstrates the good accuracy of the eCSW EOS for thermodynamic modeling of the solubilities of acid gases in aqueous alkanolamine solutions.
Compounds
# Formula Name
1 C6H15NO2 N-(2-hydroxypropyl)-2-hydroxy-1-propanamine
2 H2O water
3 H2S hydrogen sulfide
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
  • 2
  • 3
  • Mole fraction - 3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Molality, mol/kg - 1; Liquid
  • Liquid
  • Gas
  • pressure drop
  • 23