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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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5.5 The phenomenological theory <strong>of</strong> solvent effects 285<br />

where γ′ = ( γ2 −γ1)/<br />

2. Notice that the general medium and solvation effects are coupled<br />

through the solvation constants K1 and K2. When x2 = 0, eq. [5.5.19] yields ΔGgen med =gAγ1. We interpret this as a quantitative expression<br />

for the hydrophobic effect. In general, eq. [5.5.19] describes the solvophobic effect.<br />

This is a phenomenological description, not a detailed structural description.<br />

5.5.2.5 The total solvent effect<br />

The solution free energy is now obtained by inserting eqs. [5.5.13] and [5.5.19] into eq.<br />

[5.5.4]. We obtain<br />

*<br />

ΔGsoln ( x2) = gAγ1 + ΔGintersol + ΔGWW<br />

+<br />

( γ′ − ln ) + ( 2 γ′<br />

− ln )<br />

gA kT K K x x gA kT K K K K x<br />

2<br />

x1 + K1x1x2 2<br />

+KK 1 2x2 When x 2 = 0, eq. [5.5.20] gives<br />

( 0)<br />

1 1 1 2 1 2 1 2<br />

2<br />

2<br />

[5.5.20]<br />

*<br />

ΔGsoln x2 = = gAγ 1 + ΔGintersol + ΔGWW<br />

[5.5.21]<br />

With the Leffler-Grunwald delta operator symbolism 7 we define<br />

* ( ) ( )<br />

* *<br />

δMΔG = ΔGsoln x2 − ΔGsoln<br />

x2<br />

= 0 [5.5.22]<br />

which, applied to eqs. [5.5.20] and [5.5.21], gives our final result:<br />

δ<br />

MΔsoln ( γ′ − ) + ( 2 γ′<br />

− )<br />

G<br />

gA kT lnK K x x gA kT lnK<br />

K K K x<br />

*<br />

=<br />

2<br />

2<br />

x + Kxx + KKx 1 1 1 2 1 2 1 2<br />

2<br />

2<br />

1<br />

1 1 2 1 2 2<br />

[5.5.23]<br />

The quantity δMΔ Gsoln<br />

*<br />

can be read “the solvent effect on the solution free energy.” Because<br />

<strong>of</strong> eq. [5.5.1], δMΔ G<br />

* is proportional to the “relative solubility,” log[( x3) x / ( x3)<br />

x 0]<br />

2 2 = , that<br />

is, the logarithm <strong>of</strong> the solubility in the mixed solvent <strong>of</strong> composition x2 relative to the solubility<br />

in pure water. The subtraction that yields eq. [5.5.23], a workable equation with just<br />

three unknown parameters (gA, K1, and K2), has also prevented us from dealing with absolute<br />

solubilities.<br />

5.5.3 APPLICATIONS<br />

5.5.3.1 Solubility<br />

It will be no surprise that the first use <strong>of</strong> eq. [5.5.23] was to describe the equilibrium solubility<br />

<strong>of</strong> solid nonelectrolytes in mixed aqueous-organic solvents. 1 Equilibrium solubility in<br />

mol L -1 ,c3, is converted to mole fraction, x3, with eq. [5.5.24], where ρ is the saturated solution<br />

density, w is the wt/wt percentage <strong>of</strong> organic cosolvent, and M1,M2,M3are the molecular<br />

weights <strong>of</strong> water, cosolvent, and solute. 8<br />

x<br />

3<br />

c3<br />

=<br />

⎛ w<br />

c3( 1000ρ<br />

− c3M3) ⎜<br />

+<br />

⎝M<br />

( 1−w)<br />

M<br />

2 1<br />

⎞<br />

⎟<br />

⎠<br />

[5.5.24]

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