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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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9.4 Mixed solvent influence on the chemical equilibrium 543<br />

Figure 9.13. The composition <strong>of</strong> solvate shell Ni 2+ (in<br />

molar parts <strong>of</strong> water) in the mixtures <strong>of</strong> solvents<br />

formed from water and propanol (1), ethanol (2),<br />

methanol (3) and DMSO (4). Data from Ref. 43.<br />

or<br />

[ − ]<br />

+<br />

In the mixed solvents water - non-aqueous<br />

solvent, in spite <strong>of</strong> its donor and polar<br />

properties, water is a preferred solvating<br />

agent. This generalization has some exceptions<br />

(solvation in systems Ag + - H 2O -<br />

acetonitrile, Cr 3+ -H 2O - DMSO, F - -H 2O-ethylene<br />

glycol). 45<br />

Solvation energy <strong>of</strong> proton by donor solvents<br />

is very high. The regularities <strong>of</strong> the proton<br />

selective solvation and re-solvation<br />

processes were studied in more detail in comparison<br />

with other ions.<br />

Let us consider the changes in the system,<br />

when donor component is added to protic<br />

acid HA in solvent A. Anion solvation can be<br />

neglected, if both solvents have donor character.<br />

The interaction influences the proton<br />

re-solvation process.<br />

+<br />

+ B<br />

+<br />

HAp + B ←⎯→ HAp 1B←⎯→� ←⎯ →HB<br />

p + A<br />

[9.99]<br />

+ +<br />

HA + qB ←⎯→� ←⎯ →HB<br />

+ pA<br />

[9.99a]<br />

p q<br />

The model related to eq. [9.99a] was evaluated, 46 resulting in the supposition that the<br />

+ +<br />

equilibrium <strong>of</strong> two forms <strong>of</strong> solvated proton: HA p and HBq is important. Solvation<br />

stoichiometry was not considered. Both proton solvated forms are denoted as HA + and HB + .<br />

If B is the better donor component (it is a necessary requirement for equilibrium [9.99]<br />

shift to the right hand side <strong>of</strong> equation), the equation from work 46 can be simplified to the<br />

form: 47<br />

{ }<br />

B A ( a a)<br />

[ us B / ( B) ] / [ us B / ( B)<br />

]<br />

A<br />

K = K + K −K K x 1− x 1+ K x 1 −x<br />

[9.100]<br />

a a<br />

where:<br />

Ka ionic association constant<br />

A B<br />

Ka , Ka<br />

the ionic association constants <strong>of</strong> acid in individual solvents A and B<br />

Kus a constant <strong>of</strong> resolvation process<br />

xB molar fraction <strong>of</strong> B<br />

For the calculation <strong>of</strong> resolvation constant, one must determine the experimental con-<br />

A B<br />

stant <strong>of</strong> HA association in the mixed solvent and determine independently K a and K a .<br />

When the resolvation process is completed at low concentration <strong>of</strong> the second component,<br />

the change <strong>of</strong> permittivity <strong>of</strong> mixed solvent A-B may be ignored. Thus, one may as-<br />

A B<br />

sume that K and K are constant and calculate Kus from the equation [9.100] in the form:<br />

a<br />

a<br />

{ [ ] }<br />

A<br />

B A<br />

B A<br />

( Ka Ka) ( Ka Ka) [ ( xB) xB] Kus( Ka Ka)<br />

1/ − = 1/ − + 1− / 1/<br />

− [9.101]

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