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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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288 Kenneth A. Connors<br />

Solute Solvent<br />

gA, � 2 molecule -1<br />

Calculated Observed<br />

4-Nitroaniline DMSO 101 86<br />

4-Nitroaniline Acetonitrile 30 29<br />

We now encounter a curious observation. The parameter gA is constrained, in the nonlinear<br />

regression fitting program, to be constant as x 2 varies over its entire range from 0 to 1.<br />

We have identified A as the nonpolar surface area <strong>of</strong> the solute (though it may actually be<br />

the corresponding area <strong>of</strong> the solvent cavity, and so may show some cosolvent dependency,<br />

which we have ignored). The quantity g can then be estimated. For example, from Table<br />

5.5.2 for naphthalene (A = 147 � 2 molecule -1 ), g varies from 0.29 (for 2-propanol) to 0.86<br />

(for DMSO). Yet how can g possess these different values in different cosolvents, maintain<br />

its constancy as x 2 varies, and then collapse to the unique value it must possess in water, the<br />

reference solvent for all systems? An independent calculation gives g = 0.41±0.03 in water. 8<br />

Some tentative explanations for this puzzle have been <strong>of</strong>fered, 8 and we return to this issue in<br />

Section 5.5.4.<br />

Turning to the K 1 and K 2 parameters, we have observed that these are relatively insensitive<br />

to the identity <strong>of</strong> the solute, but that they depend upon the cosolvent, whose polarity is<br />

a controlling factor. Table 5.5.3 gives some empirical correlations that provide routes to the<br />

prediction <strong>of</strong> K 1 and K 1K 2. In Table 5.5.3, P M is the 1-octanol/water partition coefficient <strong>of</strong><br />

the pure cosolvent, 12 and E T is the Dimroth-Reichardt solvatochromic polarity parameter. 13<br />

We thus have the capability <strong>of</strong> predicting gA, K 1, and K 1K 2, which extends the utility <strong>of</strong> eq.<br />

[5.5.23] from the merely descriptive to the predictive.<br />

Table 5.5.3. Empirical relationships for estimating solvation constants<br />

Equation n r Restrictions<br />

log K1 = -0.0316 ET + 2.24 10 0.91 -<br />

log (K1/K2) = 0.0171 ET - 9.23 4 0.98 ET >51<br />

log (K1/K2) = -0.0959 ET + 4.60 6 0.85 ET -1.0<br />

5.5.3.2 Surface tension<br />

In the development <strong>of</strong> the basic phenomenological model, eq. [5.5.23], we derived a relationship<br />

for the surface tension <strong>of</strong> the solvation shell. Combining eqs. [5.5.16] and [5.5.18]<br />

yields<br />

2<br />

⎡ Kxx 1 1 2 + 2KK<br />

1 2x2 γ = γ + γ′<br />

1 ⎢ 2<br />

⎣x1<br />

+ K x x + K K x<br />

1 1 2 1 2<br />

2<br />

2<br />

⎤<br />

⎥<br />

⎦<br />

[5.5.26]<br />

where γ′ = ( γ2 −γ1)/<br />

2. Now if we identify the solute-solvation shell system with the air-solvent<br />

interface, we are led to test eq. [5.5.26] as a description <strong>of</strong> the composition dependence

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