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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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21.1 Supercritical solvents 1435<br />

where:<br />

ρ rm i<br />

i<br />

y V<br />

= ∑<br />

V<br />

ci<br />

v<br />

m<br />

where:<br />

λ v<br />

thermal conductivity<br />

ρrm reduced molar density for mixtures<br />

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

Mi molecular weight <strong>of</strong> component i<br />

Tci critical temperature <strong>of</strong> component i<br />

Vci critical volume <strong>of</strong> component i<br />

Zci critical compressibility <strong>of</strong> component i<br />

The vapor molar volume, V v m can be obtained from the equation <strong>of</strong> state models as described<br />

above.<br />

21.1.2.2.4 Surface tension<br />

Stability <strong>of</strong> phase boundaries depends on the surface tension. Surface tension in a supercritical<br />

fluid system is <strong>of</strong> major importance for drying, surfactant efficacy, and extraction. The<br />

surface tension <strong>of</strong> a gas increases with pressure and approaches zero at the critical point<br />

while the surface tension <strong>of</strong> liquid decreases with pressure resulting in dissolution <strong>of</strong> supercritical<br />

components in the liquid phase. The methods useful in correlating surface tension<br />

include Macleod-Sugden correlation and corresponding states theory. 21<br />

21.1.2.3 Entrainer (co-solvent effects) <strong>of</strong> supercritical solvents<br />

Entrainers, modifiers, and co-solvents are basically mixed solvent systems and provide another<br />

dimension to supercritical fluid extraction. The entrainers enhance the solubility <strong>of</strong><br />

the low volatile substance in the solvent, provide selective solubility in multi-solute instances,<br />

and enhance the sensitivity <strong>of</strong> the solubility and selectivity to temperature, pressure,<br />

and composition. The entrainers may be reactive and are also useful as slurrying<br />

media. Table 21.1.4 shows representative data on the effect <strong>of</strong> entrainers on vapor liquid<br />

systems that has been systematically studied by Brunner’s group. Kurnik and Reid 50 as well<br />

as Johnston’s group 51 present data for dense gas-solid systems.<br />

Table 21.1.4. The effect <strong>of</strong> entrainers on separation factor (Adapted from Brunner 21 )<br />

Entrainer α Entrainer α<br />

Hexadecanol(1) - octadecane(2) - entrainer - nitrous<br />

oxide (120 bar, 70°C, y 0 = 1.5 wt%, a 0 =2,<br />

y (1)+(2) = 2 wt%)<br />

acetone<br />

methanol<br />

dichloromethane<br />

benzene<br />

methyl acetate<br />

hexane<br />

cyclohexane<br />

3<br />

2.4<br />

2.1<br />

2<br />

2<br />

1.9<br />

1.7<br />

Octadecane(1) - salicylic acid phenal ester(2) -<br />

entrainer - nitrous oxide (120 bar, 70 °C, y 0 = 1.5<br />

wt%, a 0 =2,y (1)+(2) = 1.7 wt%)<br />

methanol<br />

dichloromethane<br />

benzene<br />

cyclohexane<br />

acetone<br />

hexane<br />

methyl acetate<br />

1.65<br />

1.5<br />

1.45<br />

1.4<br />

1.4<br />

1.3<br />

1.2

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