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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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6.2 Equilibrium swelling in binary solvents 321<br />

where:<br />

χ13 and χ 23 parameters <strong>of</strong> interaction <strong>of</strong> components 1 and 2 with polymer, correspondingly<br />

χ12 parameter <strong>of</strong> interaction <strong>of</strong> components 1and 2 <strong>of</strong> liquid mixture<br />

In the equation obtained from the fundamental work by Scott, 5 mixed solvent is represented<br />

as “a uniform liquid” with the variable thermodynamic parameters depending on<br />

composition.<br />

If the χ123 value is considered as a criterion <strong>of</strong> existence <strong>of</strong> a maximum <strong>of</strong> equilibrium<br />

swelling <strong>of</strong> polymer in the mixed solvent, a maximum <strong>of</strong> Q should correspond to the minimum<br />

<strong>of</strong> χ123. For practical use <strong>of</strong> Eq. [6.2.2] it is necessary to know parameters χ13, χ23, and<br />

χ12. The values χ13 and χ23 can be determined by the Flory-Rehner equation, with data on<br />

swelling <strong>of</strong> a crosslinked elastomer in individual solvents 1 and 2. The evaluation <strong>of</strong> the χ12 value can be carried out with use <strong>of</strong> results <strong>of</strong> the experimental evaluation <strong>of</strong> vapor pressure,<br />

viscosity and other characteristics <strong>of</strong> a binary mixture. 6,7<br />

To raise the forecasting efficiency <strong>of</strong> prediction force <strong>of</strong> such criterion as χ123 minimum,<br />

the amount <strong>of</strong> performance parameters determined experimentally must be reduced.<br />

For this purpose, the following expression for the quality criterion <strong>of</strong> the mixed solvent (the<br />

analogy with expression <strong>of</strong> the Flory-Huggins parameter for individual solvent-polymer<br />

system) is used:<br />

s V12<br />

2<br />

χ123 = χ123 + ( δ3 − δ12)<br />

V12 = V1x1+ V2x 2<br />

[6.2.2]<br />

RT<br />

where:<br />

V12 molar volume <strong>of</strong> the liquid mixture<br />

V1,V2 molar volumes <strong>of</strong> components 1 and 2<br />

x1,x2 molar fractions <strong>of</strong> components 1 and 2 in the solvent<br />

R universal gas constant<br />

T temperature, K.<br />

s<br />

χ123 constant, equal to 0.34<br />

s s<br />

The values <strong>of</strong> entropy components <strong>of</strong> parameters χ13 and χ 23 (essential for quality prediction)<br />

8 were taken into account. Using the real values <strong>of</strong> entropy components <strong>of</strong> interac-<br />

s s<br />

tion parameters χ13 and χ 23,<br />

we have:<br />

s V1<br />

2<br />

χ13 = χ13 − ( δ3 − δ1)<br />

[6.2.3]<br />

RT<br />

s V2<br />

2<br />

χ23 = χ23 − ( δ3 − δ2)<br />

[6.2.4]<br />

RT<br />

quality criterion <strong>of</strong> mixed solvent is represented by: 3<br />

( )<br />

12<br />

χ123 = χ13 ϕ1+ χ23 ϕ2+ δ −δ<br />

RT<br />

s s V<br />

3 12<br />

2<br />

[6.2.5]<br />

The values <strong>of</strong> parameters χ13 and χ23 were calculated from the Flory-Rehner equation,<br />

s s<br />

using data on swelling <strong>of</strong> crosslinked polymer in individual solvents, the values χ13, χ 23,<br />

and χ123 were estimated from Eqs. [6.2.3-6.2.5). Then equilibrium swelling <strong>of</strong> elastomer in<br />

SL was calculated from the equation similar to Flory-Rehner equation, considering the mix-

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