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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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13.1 Solvent effects on chemical reactivity 747<br />

3<br />

η = πρσ / 6=<br />

ρVHS<br />

[13.1.7]<br />

where:<br />

η packing density<br />

ρ number density N/V= number <strong>of</strong> particles per unit volume<br />

σ HS diameter<br />

VHS HS volume<br />

For the determination <strong>of</strong> σ(and henceη), the most direct method is arguably that based<br />

on inert gas solubility data. 39,40 However, in view <strong>of</strong> the arduousness involved and the uncertainties<br />

in both the extrapolation procedure and the experimental solubilities, it is natural to<br />

look out for alternatives. From the various suggestions, 41,42 a convenient way is to adjust σ<br />

such that the computed value <strong>of</strong> some selected thermodynamic quantity, related to σ, is consistent<br />

with experiment. The hitherto likely best method 43 is the following: To diminish effects<br />

<strong>of</strong> attraction, the property chosen should probe primarily repulsive forces rather than<br />

attractions. Since the low compressibility <strong>of</strong> the condensed phase is due to short-range repulsive<br />

forces, the isothermal compressibilityβT = -(1/V)(∂V/∂P) T might be a suitable candidate,<br />

in the framework <strong>of</strong> the generalized van der Waals (vdW) equation <strong>of</strong> state<br />

( )<br />

βT RT V Qr<br />

/ = 1 [13.1.8]<br />

where Qr is the density derivative <strong>of</strong> the compressibility factor <strong>of</strong> a suitable reference system.<br />

In the work referred to, the reference system adopted is that <strong>of</strong> polar-polarizable<br />

spheres in a mean field,<br />

Qr Z<br />

( )<br />

=<br />

⎡ 2 3<br />

5η −2η<br />

⎤<br />

⎢2<br />

−1−2 ⎥<br />

4<br />

μ<br />

⎣<br />

⎢ 1−η<br />

⎦<br />

⎥<br />

[13.1.9]<br />

where Zμ = compressibility factor due to dipole-dipole forces, 43 which is important only for<br />

a few solvents such as MeCN and MeNO2. The HS diameters so determined are found to be<br />

in excellent agreement with those derived from inert gas solubilities. It may be noted that<br />

the method <strong>of</strong> Ben-Amotz and Willis, 44 also based on βT, uses the nonpolar HS liquid as the<br />

reference and, therefore, is applicable only to liquids <strong>of</strong> weak dipole-dipole forces. Of<br />

course, as the reference potential approaches that <strong>of</strong> the real liquid, the HS diameter <strong>of</strong> the<br />

reference liquid should more closely approximate the actual hard-core length. Finally, because<br />

<strong>of</strong> its popularity, an older method should be mentioned that relies on the isobaric<br />

expansibility αp as the probe, but this method is inadequate for polar liquids. It turns out that<br />

solvent expansibility is appreciably determined by attractions.<br />

Some values <strong>of</strong> η and σ are shown in Table 13.1.2 including the two extreme cases.<br />

Actually, water and n-hexadecane have the lowest and highest packing density, respectively,<br />

<strong>of</strong> the common solvents. As is seen, there is an appreciable free volume, which may<br />

be expressed by the volume fraction η−η0 , where η0 is the maximum value <strong>of</strong> η calculated<br />

for the face-centered cubic packing <strong>of</strong> HS molecules where all molecules are in contact with<br />

each other is η0 = π 2/ 6= 074 . . Thus, 1 - η 0 corresponds to the minimum <strong>of</strong> unoccupied<br />

volume. Since η typically is around 0.5, about a quarter <strong>of</strong> the total liquid volume is empty<br />

enabling solvent molecules to change their coordinates and hence local density fluctuations<br />

to occur.

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