Solubility of sparingly soluble salts,
i.e., CaF2(s), MgF2(s), and ZnF2(s), in ZnSO4 aqueous solution is necessary for the process
design to remove Ca2+, Mg2+, and F– ions from zinc
hydrometallurgical systems. However, these data have been unavailable
in any literature up to now. In this work, the solubilities of MF2(s) (M = Ca, Mg, Zn) in ZnSO4 and MF2(s) (M = Ca, Mg) in ZnF2 aqueous solutions have been elaborately
measured at 298.15 K. The results showed that the CaF2(s) and MgF2(s) solubilities increase with the increasing
ZnSO4 concentration; for example, their solubility in 2
mol·kg–1 ZnSO4 aqueous solution
increases to about 6 times of that in pure water. The ZnSO4 has a slightly stronger salt-in effect on CaF2(s) than
on MgF2(s). However, the ZnF2(s) solubility
in ZnSO4 aqueous solution decreases at first and then increases
with increasing ZnSO4 concentration. As expected, ZnF2 possesses strong salting-out effect on the solubility of
CaF2(s) and MgF2(s). A remarkable character
is that the CaF2(s) solubility goes through a minimum point
and then increases again with the ZnF2 addition; inversely,
the MgF2(s) solubility decreases with the ZnF2 addition with time. Their different solubility characters have been
interpreted from the aspect of ion association interaction. An ion
association model has been applied to predict the CaF2(s) and MgF2(s) solubility in ZnF2 aqueous solution.
The predicted results agree with the experimental ones quite well,
which indicates that the ion association dominates the excess properties
of these concerned systems.