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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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

where:<br />

ϕ 1′<br />

volume fraction <strong>of</strong> a solvent in a binary mixture <strong>of</strong> solvents causing a maximum <strong>of</strong><br />

equilibrium swelling<br />

ΔHmix experimental value <strong>of</strong> the mixing enthalpy <strong>of</strong> components <strong>of</strong> binary solvent. It can be<br />

taken from literature. 23-24<br />

V12 the molar volume <strong>of</strong> binary solvent<br />

If there are no volume changes, V12 can be calculated using the additivity method:<br />

V = V ϕ + V ϕ [5.1.19]<br />

12 1 1 2 2<br />

Attempts 25 were made to relate intrinsic viscosity [η] to solubility parameters <strong>of</strong> mixed<br />

solvents. δ2 <strong>of</strong> polymer was calculated from the equation: [η]=f(δ1 ). The authors assumed<br />

that the maximum value <strong>of</strong> [η] is when δ1 = δ2 <strong>of</strong> polymer. However, studying [η] for<br />

polymethylmethacrylate in fourteen liquids, the authors found a large scatter <strong>of</strong> experimental<br />

points through which they have drawn a curve with a diffusion maximum. Thus the precision<br />

<strong>of</strong> δ2 values was affected by 10% scatter in experimental data.<br />

This method was widely used by Mangaray et al. 26-28 The authors have presented [η]as<br />

the Gaussian function <strong>of</strong> (δ1 - δ2 ) 2 12 /<br />

. Therefore, dependence {( 1/<br />

V1)ln[ η] max / [ η]} = f(<br />

δ1)<br />

can be expressed by a straight line intersecting the abscissa at a point for which δ1 = δ2 . For<br />

natural rubber and polyisobutylene, the paraffin solvents and ethers containing alkyl chains<br />

<strong>of</strong> a large molecular mass were studied. 26 For polystyrene, aromatic hydrocarbons were<br />

used. For polyacrylates and polymethacrylates esters (acetates, propionates, butyrates)<br />

were used. 27,28 The method was used for determination <strong>of</strong> δ2 <strong>of</strong> many polymers. 29-31 In all<br />

cases, the authors observed extrema in the dependence <strong>of</strong> [η] =f(δ1 ), and the obtained values<br />

<strong>of</strong> δ2 coincided well with the values determined by other methods. But for some polymers<br />

it was not possible to obtain extremum in dependence <strong>of</strong> [η] =f(δ1 ). 32<br />

A method <strong>of</strong> the evaluation [η] in one solvent at different temperatures was used for<br />

polyisobutylene 33 and polyurethanes. 34<br />

For polymers soluble in a limited range <strong>of</strong> solvents, more complex methods utilizing<br />

[η] relationship are described. 35-37<br />

In addition to the above methods, δ2 <strong>of</strong> polymer can be determined from a threshold <strong>of</strong><br />

sedimentation 38 and by critical opalescence. 39 In recent years the method <strong>of</strong> inverse gas-liquid<br />

chromatography has been used to evaluate δ2 <strong>of</strong> polymers. 40,41 One may also use some<br />

empirical ratios relating solubility parameters <strong>of</strong> polymers with some <strong>of</strong> their physical properties,<br />

such as, surface tension 42-44 and glass transition temperature. 45<br />

The solubility parameters for various polymers are given in Table 5.1.3.<br />

Table 5.1.4. Solubility parameters <strong>of</strong> some polymers 36,46<br />

Polymer<br />

(cal/cm 3 ) 1/2<br />

δ<br />

(MJ/m 3 ) 1/2<br />

Polymer<br />

(cal/cm 3 ) 1/2<br />

δ<br />

(MJ/m 3 ) 1/2<br />

Butyl rubber 7.84 16.0 Polydimethylsiloxane 9.53 19.5<br />

Cellulose diacetate 10.9 22.2 Polydimethylphenyleneoxide 8.6 17.6<br />

Cellulose dinitrate 10.6 21.6 Polyisobutylene 7.95 16.2<br />

Polyamide-66 13.6 27.8 Polymethylmethacrylate 9.3 19.0

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