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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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206 Christian Wohlfarth<br />

wi mass fraction <strong>of</strong> component i<br />

There has been a broad application <strong>of</strong> this group-contribution UNIFAC-fv concept to<br />

polymer solutions in the literature. Raetzsch and Glindemann 290 recommended the use <strong>of</strong><br />

the real free-volume relation from the Flory-Orwoll-Vrij model to account for realistic<br />

PVT-data. Problems arise for mixtures composed from chemically different components<br />

that posses the same groups, e.g., mixtures with different isomers. Kikic et al. 291 discussed<br />

the influence <strong>of</strong> the combinatorial part on results obtained with UNIFAC-fv calculations.<br />

Gottlieb and Herskowitz 292,293 gave some polemic about the special use <strong>of</strong> the c1-parameter within UNIFAC-fv calculations. Iwai et al. 294,295 demonstrated the possible use <strong>of</strong><br />

UNIFAC-fv for the calculation <strong>of</strong> gas solubilities and Henry’s constants using a somewhat<br />

different free-volume expression. Patwardhan and Belfiore 296 found quantitative discrepancies<br />

for some polymer solutions. In a number <strong>of</strong> cases UNIFAC-fv predicted the occurrence<br />

<strong>of</strong> a demixing region during the calculation <strong>of</strong> solvent activities where experimentally only<br />

a homogeneous solution exists. Price and Ashworth 297 found that the predicted variation <strong>of</strong><br />

residual solvent activity with polymer molecular mass at high polymer concentrations is opposite<br />

to that measured for polydimethylsiloxane solutions. But, qualitative correct predictions<br />

were obtained for poly(ethylene glycol) solutions with varying polymer molecular<br />

mass. 298-300 However, UNIFAC-fv is not capable <strong>of</strong> representing thermodynamic data <strong>of</strong><br />

strongly associating or solvating systems.<br />

Many attempts have been made to improve the UNIFAC-fv model which cannot be<br />

listed here. A comprehensive review was given by Fried et al. 301 An innovative method to<br />

combine the free-volume contribution within a corrected Flory-Huggins combinatorial entropy<br />

and the UNIFAC concept was found by Elbro et al. 302 and improved by Kontogeorgis<br />

et al. 303 These authors take into account the free-volume dissimilarity by assuming different<br />

van der Waals hard-core volumes (again from Bondi’s tables 264 ) for the solvent and the<br />

polymer segments<br />

13 / 13 / ( , )<br />

fv<br />

V = q V −V<br />

i<br />

fv<br />

ϕ i<br />

i i i vdW<br />

= i<br />

fv<br />

i ∑<br />

j<br />

fv<br />

j j<br />

3<br />

[4.4.92a]<br />

xV / xV<br />

[4.4.92b]<br />

where:<br />

qi surface area <strong>of</strong> component i based on Bondi’s van der Waals surfaces<br />

xi mole fraction <strong>of</strong> component i<br />

Vi molar volume <strong>of</strong> component i<br />

Vi,vdW van der Waals hard-core molar volume <strong>of</strong> component i<br />

and introduced these free-volume terms into Equation [4.4.68] to obtain a free-volume corrected<br />

Flory-Huggins combinatorial term:<br />

or<br />

fv<br />

fv ( i xi) ( i xi)<br />

fv<br />

lnγ = ln ϕ / + 1 − ϕ /<br />

[4.4.93a]<br />

i<br />

fv<br />

fv<br />

( ϕiwi) ( ϕi<br />

xi)<br />

fv<br />

lnΩ i = ln / + 1 − /<br />

[4.4.93b]

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