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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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6.2 Equilibrium swelling in binary solvents 325<br />

At the same values <strong>of</strong> Q v difference between coordinates on the abscissa axes <strong>of</strong> points<br />

<strong>of</strong> the curves 1-1�, 2-2� (Figures 6.2.5-6.2.8) are equal ε (Figure 6.2.9).<br />

As expected, 10 preferential sorption was observed, with the essential distinction <strong>of</strong><br />

molar volumes V 1 and V 2 <strong>of</strong> components <strong>of</strong> the mixed solvent (hexane-DBP, DOS-DEP).<br />

For swelling <strong>of</strong> the crosslinked elastomer SCN-26 in the mixture <strong>of</strong> components, having<br />

similar molar volumes V 1 and V 2 (e.g., amyl acetate-dimethyl phthalate) the preferential<br />

sorption <strong>of</strong> components <strong>of</strong> SL is practically absent. Influence <strong>of</strong> V 1 and V 2 and the influence<br />

<strong>of</strong> double interaction parameters on the sorption <strong>of</strong> binary liquids by crosslinked elastomers<br />

was examined by the method <strong>of</strong> mathematical experiment. Therewith the set <strong>of</strong> equations<br />

describing swelling <strong>of</strong> crosslinked elastomers in binary mixture, similar to the equations obtained<br />

by Bristow 6 from the Flory-Rehner theory 11 and from the work <strong>of</strong> Schulz and Flory, 12<br />

were used:<br />

2<br />

( 1 l) ( 1 l)<br />

2<br />

2<br />

lnϕ + − ϕ + χ ϕ = lnυ<br />

+ − υ + υ + χ υ + χ υ +<br />

1 2 12 2<br />

1 2 3 12 2<br />

⎛ 13 2<br />

+ ( χ12 + χ13 − lχ23) υ2υ3+ ( νe V3) V1⎜υ3−<br />

υ<br />

⎝ f<br />

/<br />

/<br />

1<br />

1 2<br />

1<br />

( 1 ) 1 12 1 2 ( 1 )<br />

lnϕ + − l ϕ + l χ ϕ = lnυ<br />

+ − l υ + υ + l<br />

2<br />

− − − −1<br />

1 3<br />

⎡ 13 / 2 ⎤<br />

χ υ + lχ υ + χ12 + lχ23 − χ13 υ1υ3+ ν V3V2υ3− υ3<br />

⎣<br />

⎢ f ⎦<br />

⎥<br />

2<br />

2<br />

⎣ 12 1 23 3 ( ) ⎦ ( e / )<br />

3<br />

⎞<br />

⎟<br />

⎠<br />

12 3<br />

[6.2.6]<br />

[6.2.7]<br />

where:<br />

l =V1/V2 f functionality <strong>of</strong> a network<br />

The analysis <strong>of</strong> calculations from Eqs. [6.2.6] and [6.2.7] has shown that if V1 χ13. The greater is χ12 value at V1 ≠ V2 the more likely preferential sorption takes place with all<br />

other parameters being equal. The same applies to the diluted polymer solutions.<br />

To improve calculations <strong>of</strong> the preferential sorption in the diluted solutions <strong>of</strong> polymers,<br />

the correction <strong>of</strong> Flory’s theory is given in works 9,13-15 by introduction <strong>of</strong> the parameter<br />

<strong>of</strong> three-component interaction, χT, into the expression for free energy <strong>of</strong> mixing, and<br />

substitution <strong>of</strong> χT by qT. 14 This approach is an essential advancement in the analysis <strong>of</strong> a<br />

sorption <strong>of</strong> two-component liquids by polymer. On the other hand, the increase in the number<br />

<strong>of</strong> experimental parameters complicates the task <strong>of</strong> prediction <strong>of</strong> the preferential sorption.<br />

In swelling crosslinked elastomers, the preferential sorption corresponds to the maximum<br />

QV value and compositions in a swollen polymer and a liquid phase practically coincide<br />

(Figures 6.2.5-6.2.8). This observation can be successfully used for an approximate<br />

evaluation <strong>of</strong> the preferential sorption.<br />

Assuming that ϕ1 = φ1and<br />

ϕ2 = φ2<br />

at extremum <strong>of</strong> the total sorption (φ3 = φ3<br />

min ), AUL 5<br />

e<br />

can be used to calculate the effective value <strong>of</strong> χ12 from the expression for χ123: 16<br />

χ<br />

e<br />

12<br />

m<br />

χ13<br />

χ 23V1 χ123V1<br />

= + − [6.2.8]<br />

m m<br />

m m m<br />

ϕ ϕ V V ϕ ϕ<br />

2<br />

1 2<br />

12 1 2

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