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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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21.1 Supercritical solvents 1429<br />

K<br />

i<br />

( TPx)<br />

( TPy)<br />

= � , , ϕ<br />

ϕ�<br />

, ,<br />

β<br />

i i<br />

α<br />

i i<br />

For the unsymmetrical approach:<br />

β<br />

γ ( TPx , , ) f( TP<br />

i i i , )<br />

Ki<br />

α<br />

ϕ�<br />

TPy , ,<br />

( )<br />

i i<br />

where:<br />

Ki partition coefficient <strong>of</strong> component i in phases α and β<br />

�ϕ β<br />

i fugacity coefficient <strong>of</strong> component i in mixture for phase β<br />

�ϕ α<br />

i fugacity coefficient <strong>of</strong> component i in mixture for phase α<br />

γ β<br />

i activity coefficient <strong>of</strong> component i in mixture for phase β<br />

fi fugacity <strong>of</strong> pure component i<br />

If one assumes no solvent in the solid phase, the relation for solubility <strong>of</strong> the solid in<br />

the supercritical solvent reduces to:<br />

y<br />

i<br />

sub<br />

PiT =<br />

P<br />

⎛<br />

⎜<br />

⎝<br />

( )<br />

s sub<br />

() ⎞⎛<br />

⎞ ⎛ViP<br />

−P<br />

() T<br />

⎟⎜<br />

1<br />

⎟⎜<br />

⎠⎝ϕ�<br />

DG<br />

i<br />

⎟<br />

exp⎜<br />

⎠<br />

⎜<br />

⎝<br />

RT<br />

A B C<br />

where:<br />

yi mole fraction <strong>of</strong> component i in gas phase<br />

sub<br />

Pi sublimation pressure <strong>of</strong> component i<br />

P total pressure<br />

�ϕ<br />

DG<br />

i fugacity coefficient <strong>of</strong> component i in mixture for dense gas phase<br />

s<br />

Vi partial molar volume <strong>of</strong> component i in solid phase<br />

R universal gas constant<br />

T absolute temperature<br />

The first term A is for ideal gas solubility, the second term B accounts for the<br />

non-ideality, while the third term C (Poynting correction) accounts for the pressure effects.<br />

The product <strong>of</strong> the second and third terms is <strong>of</strong>ten referred as the Enhancement Factor (over<br />

the ideal). In the absence <strong>of</strong> data, the sublimation pressure may be approximated through extrapolation<br />

<strong>of</strong> the vapor pressure information.<br />

21.1.2.1.3 Modeling<br />

The approaches to modeling the high pressure phase behavior follow either use <strong>of</strong> the equation<br />

<strong>of</strong> state models for fugacity coefficient determination or the treatment <strong>of</strong> the dense gas<br />

as an “expanded liquid” through an activity coefficient model, the former approach being<br />

more popular.<br />

The macroscopic dense gas modeling approaches include van der Waals family <strong>of</strong><br />

equation <strong>of</strong> states, virial family <strong>of</strong> equation <strong>of</strong> states, and non-classical approaches. The molecular/theoretical<br />

approaches and considerations contribute not only to more comprehensive<br />

models but also provide insight bringing forth sound parameters/terms to the<br />

macroscopic models. Computer simulation (molecular) can also be used to directly compute<br />

phase behavior with some success. 27,28 The virial family <strong>of</strong> equation <strong>of</strong> states finds limited<br />

use in supercritical applications due to the necessity for a large number <strong>of</strong> terms and<br />

⎞<br />

⎟<br />

⎟<br />

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