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Physical
Properties Calculation |
The reduced density
is the ratio between the density r(T,P) and the extrapolated density at 0 Kelvin, r* (also called hard-core density):

For the purposes of our
calculations, the variations of density with temperature are defined as:
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where a is the classical volumetric coefficient of
thermal expansion. Where no experimental PVT data was available, either as
tables or as an empirical relation such as the Tait equation,1,2 a was estimated by group contribution
methods. The method for the estimation of a is based in the work of D.Boudoirs, L. Constantiou and C.
Panayiotou.3 In this method, the Lattice Fluid theory (LF)
characteristic parameters, T0, P0 and r0
are estimated using group contributions and used to calculate the density in
the desired temperature range. The coefficient of thermal expansion is the
exponential regression of the densities calculation. The hard-core density,r*, is assumed to be the intercept of the
regression with zero Kelvin temperature.
For the polymer
construction section of the applet a simple empirical approach for the
estimation of the coefficient of thermal expansion based on the polymer glass
transition, Tg is used:4

The coefficient obtained
by this equation is not exact, but is an ok estimate if no other information is
available.
The hard-core volume (n) is the
extrapolation of the repeat unit volume at 0 Kelvin. It can be related to hard-core density, r* by:

where
Munit is the molecular weight of the repeating unit (expressed in
g/mol). The parameter used in the applet is a molar hard-core volume, which is
obtained by multiplying the molecular value by Avogadroís number.
For
the polymer construction section of the applet, the hard-core density is
obtained from the hard-core parameter, ro, calculated using the
Boudoris group contribution method. 3
\Solubility parameter
The Hildebrand
solubility parameter or cohesive energy density is defined as:

This parameter is a measure of the interacting
behavior of the chemical species. In the Hildebrand Solubility Parameter
Theory, chemical species with similar solubility parameters are miscible. For
our phase behavior prediction, the solubility parameter for each component is
estimated using the group contribution method described by Van Krevelen5.
From this method, a solubility parameter at 298 K is obtained. The repeat unit
volume, V repeat unit, is also obtained using Van Krevelenís
group contribution method.
The molecular
weights of the polymer, Mpolymer, components are incorporated into
the CRS model in a similar fashion as in the Flory-Huggins model. The parameter
used for the calculation is the number of repeat units, N, which can be easily
obtained if the molecular weight for the repeat unit is known:

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