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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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560 Y. Y. Fialkov, V. L. Chumak<br />

( 2 / / ε) ( / / ε)<br />

ΔH =− R a + a T + a ΔS<br />

= R a − a T + a<br />

T 01 02 11 T<br />

00 02 10<br />

Comparison <strong>of</strong> ΔH i with ΔH T and ΔS i with ΔS T shows that integral values <strong>of</strong> thermodynamic<br />

characteristics <strong>of</strong> the ionic association process for HCOOH are not only less informative<br />

than van’t H<strong>of</strong>f’s characteristics, but they contradict the physical model <strong>of</strong> the process<br />

in this case. Indeed, corresponding dependencies <strong>of</strong> compensative effect are described by<br />

equations:<br />

ΔH i = -0.704ΔS i + 22.87 kJ/mol<br />

ΔH T = 0.592ΔS T - 22.22 kJ/mol<br />

Thus, if the compensative effect for integral thermodynamic functions is interpreted,<br />

one should conclude that characteristic temperature (this is tanα = ΔH/ΔS) is a negative<br />

value, but that is, <strong>of</strong> course, devoid <strong>of</strong> physical sense.<br />

In common cases, when the dependence [9.125] is approximated using equation<br />

[9.56], “van’t H<strong>of</strong>f’s” (original) thermodynamic constituents <strong>of</strong> equilibrium process are<br />

equal to:<br />

( )<br />

ΔH =− R a + a<br />

T<br />

01 11<br />

( )<br />

ΔS = R a + a<br />

T<br />

00 10<br />

/ ε [9.130]<br />

/ ε [9.131]<br />

As it is evident from [9.130] and [9.131], the original thermodynamic characteristics<br />

<strong>of</strong> the process are summarized by the terms where the first <strong>of</strong> them does not depend, and the<br />

second one depends, on permittivity. These terms accordingly are called covalent and electrostatic<br />

constituents <strong>of</strong> the process in solution, i.e.,<br />

cov<br />

el<br />

ΔH=− Ra01 and ΔH=−Ra11<br />

/ ε [9.132]<br />

cov<br />

el<br />

ΔS= Ra00 and ΔS=<br />

Ra10<br />

/ ε [9.133]<br />

It should be emphasized that ΔG T values are substantially more informative than integral<br />

thermodynamic values for thermodynamic analysis <strong>of</strong> chemical equilibrium in solutions<br />

<strong>of</strong> mixed solvents. Indeed, in frequent cases <strong>of</strong> equilibrium constant polytherm<br />

characterized by an extreme (i.e., sign <strong>of</strong> ΔH i changes), one may arrive at the wrong conclusion<br />

that the process nature changes greatly at temperature <strong>of</strong> extreme value. As has been<br />

shown, 71 appearance <strong>of</strong> extreme value <strong>of</strong> equilibrium constant polytherms is caused in the<br />

majority <strong>of</strong> cases by temperature change <strong>of</strong> solvent permittivity. The condition <strong>of</strong> extreme<br />

appearance for the process described by equation [9.55] is:<br />

where:<br />

( ) ( )<br />

a exp αT + γ + αa<br />

T a T + a = [9.134]<br />

01 extr 11 extr 10 extr 11 0<br />

αγ , the coefficients <strong>of</strong> lnε = αT +γequation<br />

γ activity coefficient<br />

Textr temperature corresponding to extremum <strong>of</strong> isotherm <strong>of</strong> equilibrium constant

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