The
addition of a nonextractable salt has an important influence
on the solvent extraction of metal ions, but the underlying principles
are not completely understood yet. However, relating solute hydration
mechanisms to solvent extraction equilibria is key to understanding
the mechanism of solvent extraction of metal ions as a whole. We have
studied the speciation of Co(II), Zn(II), and Cu(II) in aqueous solutions
containing different chloride salts to understand their extraction
to the basic extractant methyltrioctylammonium chloride (TOMAC). This
includes the first speciation profile of Zn(II) in chloride media
with the three Zn(II) species [Zn(H
2
O)
6
]
2+
, [ZnCl
3
H
2
O]
−
, and
[ZnCl
4
]
2–
. The observed differences in
extraction efficiency for a given transition metal ion can be explained
by transition metal ion hydration due to ion–solvent interactions,
rather than by ion–solute interactions or by differences in
speciation. Chloride salting agents bearing a cation with a larger
hydration Gibbs free energy reduce the free water content more, resulting
in a lower hydration for the transition metal ion. This destabilizes
the transition metal chloro complex in the aqueous phase and increases
the extraction efficiency. Salting agents with di- and trivalent cations
reduce the transition metal chloro complex hydration less than expected,
resulting in a lower extraction efficiency. The cations of these salting
agents have a very large hydration Gibbs free energy, but the overall
hydration of these salts is reduced due to significant salt ion pair
formation. The general order of salting-out strength for the extraction
of metal ions from chloride salt solutions is Cs
+
<
Rb
+
< NH
4
+
≈ K
+
< Al
3+
≈ Mg
2+
≈ Ca
2+
≈ Na
+
< Li
+
. These findings can
help in predicting the optimal conditions for metal separation by
solvent extraction and also contribute to a broader understanding
of the effects of dissolved salts on solutes.