Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

The solubility of H2S in liquid sulfur

Marriott, R. A.[Robert A.], Fitzpatrick, E.[Ed], Lesage, K. L.[Kevin L.]
Fluid Phase Equilib. 2008, 269, 1-2, 69-72
ABSTRACT
The need for fundamental data describing the dissolution of hydrogen sulfide, H2S, in Claus recovered liquid sulfur prompted an examination of equilibrium H2S solubility at typical industrial condensation temperatures and partial pressures. An FT/IR absorption technique has been described and new H2S solubility measurements have been reported for partial H2S pressures from 0.4 to 56 kPa and temperatures from 120 to 155 .C. The measurements were combined with previously reported values for atmospheric pressures of H2S and used to calibrate a semi-empirical equation for the Henry s law solubility in liquid sulfur as a function of temperature. Estimations were compared to Claus plant field data and appear to underestimate the H2S solubility for the first and second catalyst condenser stages. This underestimation was attributed to rapid condensation resulting in super-saturation of the recovered sulfur liquid, or an inaccurate measurement of the condensation temperatures.
Compounds
# Formula Name
1 S sulfur
2 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
  • Vapor or sublimation pressure, kPa ; Gas
  • Temperature, K; Gas
  • Mass fraction - 2; Gas
  • Gas
  • Liquid
  • CCELL:UFactor:32
  • 34