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The solubility of K2SO4 in various mixed solvent systems

The following five systems are considered on this page:

  1. Methanol-K2SO4-H2O at 60°C
  2. Ethanol-K2SO4-H2O at 25°C
  3. 1-Propanol-K2SO4-H2O at 45°C
  4. i-Propanol-K2SO4-H2O at 50°C
  5. NH3-K2SO4-H2O at 60°C

The figures 1 to 5 show solubility isotherms for these five systems. The solubility isotherms describe compositions of each system in equilibrium with solid potassium sulfate.  In all these systems, K2SO4 is being salted out by the addition of an extra solvent. 'Salted out' means that the solubility decreases and an excess of salt precipitates. 

In the triangular diagrams shown below, lines of constant mass % potassium sulfate are lines parallel to the right hand side of the triangle. This side is opposite to the corner representing pure K2SO4 and represents potassium sulfate free solutions. A decreasing solubility of K2SO4 is characterized by solubility lines getting closer to the right side of the diagram. 

Of the five solvents added one by one in each of the five diagrams, ammonia has a stronger salting out effect on K2SO4 than the four alcohols. In all the depicted diagrams, the red circles represent experimental data while the solubility equilibrium lines were calculated with the Extended UNIQUAC model.

1. The Methanol-K2SO4-H2O system at 60°C:

Phase diagram for the Methanol-K2SO4-H2O system at 60°C. Data calculated with the Extended UNIQUAC model are plotted together with experimental data

Figure 1: The Methanol-K2SO4-H2O system at 60°C

2. Ethanol-K2SO4-H2O at 25°C

Phase diagram for the Ethanol-K2SO4-H2O system at 25°C. Data calculated with the Extended UNIQUAC model are plotted together with experimental data

Figure 2: The ethanol-K2SO4-H2O system at 25°C

3. 1-Propanol-K2SO4-H2O at 45°C

Phase diagram for the n-propanol-K2SO4-H2O system at 45°C. Data calculated with the Extended UNIQUAC model are plotted together with experimental data

Figure 3: The 1-Propanol-K2SO4-H2O system at 45°C

4. i-Propanol-K2SO4-H2O at 50°C

Phase diagram for the iso-propanol-K2SO4-H2O system at 50°C. Data calculated with the Extended UNIQUAC model are plotted together with experimental data

Figure 4: The i-Propanol-K2SO4-H2O system at 50°C

5. The NH3-K2SO4-H2O system at 60°C

Phase diagram for the Ammonia-K2SO4-H2O system at 60°C. Data calculated with the Extended UNIQUAC model are plotted together with experimental data

Figure 5: The NH3-K2SO4-H2O system at 60°C