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

Phase Equilibrium of the MgSO4-(NH4)2SO4-H2O Ternary System: Effects of Sulfuric Acid and Iron Sulfate and Its Application in Mineral Carbonation of Serpentine

Liu, Weizao, Chu, Guanrun, Yue, Hairong, Liang, Bin, Luo, Dongmei, Li, Chun
J. Chem. Eng. Data 2018, 63, 5, 1603-1612
ABSTRACT
The carbonation Mg-rich natural minerals or industrial wastes is an attractive route to store CO2. Recently, an approach involving the indirect mineral carbonation of serpentine with recyclable (NH4)2SO4 or NH4HSO4 is receiving widespread attention. In this study, the solubilities associated with the mineral process (ternary system of (NH4)2SO4-MgSO4-H2O) were measured and calculated using the isothermal method and Pitzer model, respectively. The effects of adding small amounts of H2SO4 and iron sulfate on the solubilities were evaluated. The results showed that the crystalline region of MgSO4*(NH4)2SO4*6H2O (boussingaultite) is larger than those of the other species, which indicates that boussingaultite is crystallized out easily. The presence of H2SO4 at a concentration of up to 10 wt.% and iron sulfate of 2.5 wt.% almost had no effect of the solubilities. The minimal ratios of liquid to solid during the leaching unit were calculated as 3.45, 2.19 and 1.36 mL/g at 25, 55 and 80 C, respectively. Compared with the case of 25 C, the energy consumption for the evaporation could be reduced by 36.5% at 55 C and 60.6% at 80 C. During the crystallization of ammonium sulfate, high purity (NH4)2SO4 is hardly obtained due to the small crystalline field.
Compounds
# Formula Name
1 MgO4S magnesium sulfate
2 H8N2O4S ammonium sulfate
3 H2O water
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
  • Mass fraction - 2 ; Liquid
  • Mass fraction - 1; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal of intercomponent compound 1
  • Titration method
  • 2
  • POMD
  • 1
  • 2
  • 3
  • Mass fraction - 2 ; Liquid
  • Temperature, K; Liquid
  • Mass fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal of intercomponent compound 2
  • Titration method
  • 37
  • POMD
  • 1
  • 2
  • 3
  • Mass fraction - 2 ; Liquid
  • Temperature, K; Liquid
  • Mass fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 2
  • Titration method
  • 6
  • POMD
  • 1
  • 2
  • 3
  • Mass fraction - 2 ; Liquid
  • Mass fraction - 1; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal of intercomponent compound 3
  • Titration method
  • 2
  • POMD
  • 1
  • 2
  • 3
  • Mass fraction - 2 ; Liquid
  • Mass fraction - 1; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal of intercomponent compound 1
  • Titration method
  • 2
  • POMD
  • 1
  • 3
  • Solid-liquid equilibrium temperature, K ; Liquid
  • Mass fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal of intercomponent compound 1
  • titration
  • 1
  • POMD
  • 1
  • 3
  • Solid-liquid equilibrium temperature, K ; Liquid
  • Mass fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal of intercomponent compound 3
  • titration
  • 1
  • POMD
  • 1
  • 3
  • Solid-liquid equilibrium temperature, K ; Liquid
  • Mass fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal of intercomponent compound 2
  • titration
  • 1
  • POMD
  • 2
  • 3
  • Mass fraction - 2 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Crystal - 2
  • Titration method
  • 3