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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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104 Valery Yu. Senichev, Vasiliy V. Tereshatov<br />

δis a parameter <strong>of</strong> intermolecular interaction <strong>of</strong> an individual liquid. The aim <strong>of</strong> many<br />

studies was to find relationship between energy <strong>of</strong> mixing <strong>of</strong> liquids and their δ. The first attempt<br />

was made by Hildebrand and Scatchard 5,6 who proposed the following equation:<br />

( )<br />

m<br />

ΔU<br />

= x V + x V<br />

1 1 2 2<br />

( xV x V)(<br />

)<br />

2<br />

/ 12 / ⎤<br />

2<br />

ϕϕ 1 2<br />

⎛ΔE<br />

⎞ ΔE<br />

⎜<br />

⎟<br />

⎝ V ⎟<br />

−<br />

⎠ V<br />

⎛<br />

12 ⎡<br />

1<br />

⎢ ⎜<br />

⎣⎢<br />

1 ⎝ 2<br />

= + δ −δ<br />

ϕ ϕ [4.1.10]<br />

1 1 2 2 1 2<br />

2<br />

1 2<br />

where:<br />

ΔU m<br />

internal energy <strong>of</strong> mixing, that is a residual between energies <strong>of</strong> a solution and<br />

components,<br />

x1,x2 molar fractions <strong>of</strong> components<br />

V1,V2 molar volumes <strong>of</strong> components<br />

ϕ1, ϕ2 volume fractions <strong>of</strong> components<br />

The Hildebrand-Scatchard equation became the basis <strong>of</strong> the Hildebrand theory <strong>of</strong> regular<br />

solutions. 5 They interpreted a regular solution as a solution formed due to the ideal entropy<br />

<strong>of</strong> mixing and the change <strong>of</strong> an internal energy. The assumed lack <strong>of</strong> the volume<br />

change makes an enthalpy or heat <strong>of</strong> mixing equated with the right members <strong>of</strong> the equation.<br />

The equation permits calculation heat <strong>of</strong> mixing <strong>of</strong> two liquids. It is evident from equation<br />

that these heats can only be positive. Because <strong>of</strong> the equality <strong>of</strong> <strong>of</strong> components, ΔH m =0.<br />

The free energy <strong>of</strong> mixing <strong>of</strong> solution can be calculated from the equation<br />

( )<br />

m<br />

ΔG<br />

= x V + x V<br />

1 1 2 2<br />

( )<br />

⎛ΔE<br />

⎞ ΔE<br />

⎜<br />

⎟<br />

⎝ V ⎟<br />

−<br />

⎠ V<br />

⎛<br />

12 ⎡<br />

1<br />

⎢ ⎜<br />

⎣⎢<br />

1 ⎝ 2<br />

− TΔS = V δ −δ ϕ ϕ −TΔS<br />

id<br />

1 2<br />

2<br />

⎞<br />

⎟<br />

⎠<br />

⎞<br />

⎟<br />

⎠<br />

⎥<br />

⎦⎥<br />

2<br />

/ 12 / ⎤<br />

2<br />

ϕϕ 1 2<br />

⎥<br />

⎦⎥<br />

1 2 [4.1.11]<br />

The change <strong>of</strong> entropy, ΔS id, is calculated from the Gibbs equation for mixing <strong>of</strong> ideal<br />

gases. The calculated values are always positive.<br />

( )<br />

ΔS =− R x lnx + x ln x<br />

[4.1.12]<br />

id<br />

1 1 2 2<br />

where:<br />

R gas constant<br />

Considering the signs <strong>of</strong> the parameters ΔSid and ΔH m in Eq. [4.1.10], the ideal entropy<br />

<strong>of</strong> mixing promotes a negative value <strong>of</strong> ΔG m , i.e., the dissolution and the value <strong>of</strong> ΔH m reduces<br />

the ΔG m value. It is pertinent that the most negative ΔG m value is when ΔH m =0, i.e.,<br />

when δ <strong>of</strong> components are equal. With these general principles in mind, the components<br />

with solubility parameters close to each other have the best mutual solubility. The theory <strong>of</strong><br />

regular solutions has essential assumptions and restrictions. 7 The Eq. [4.1.10] is deduced<br />

under assumption <strong>of</strong> the central role <strong>of</strong> dispersion forces <strong>of</strong> interaction between components<br />

<strong>of</strong> solution that is correct only for the dispersion forces. Only in this case it is possible to accept<br />

that the energy <strong>of</strong> contacts between heterogeneous molecules is a geometric mean<br />

value <strong>of</strong> energy <strong>of</strong> contacts between homogeneous molecules:<br />

=<br />

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