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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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212 Christian Wohlfarth<br />

wrong phase equilibrium calculations and, therefore, also to wrong solvent activities from<br />

such calculations. Some ways to overcome this situation and to obtain reliable parameters<br />

for phase equilibrium calculations are provided in Ref., 371 together with examples from the<br />

literature that will not be repeated here.<br />

The perturbed-hard-sphere-chain (PHSC) equation <strong>of</strong> state is a hard-sphere-chain theory<br />

that is somewhat different to SAFT. It is based on a hard-sphere chain reference system<br />

and a van der Waals-type perturbation term using a temperature-dependent attractive parameter<br />

a(T) and a temperature-dependent co-volume parameter b(T). Song et al. 259,260 applied<br />

it to polymer systems and extended the theory also to fluids consisting <strong>of</strong><br />

heteronuclear hard chain molecules. The final equation for pure liquids or polymers as derived<br />

by Song et al. is constructed from three parts: the first term stems (as in PHC, COR or<br />

SAFT) from the Carnahan-Starling hard-sphere monomer fluid, the second is the term due<br />

to covalent chain-bonding <strong>of</strong> the hard-sphere reference chain and the third is a van der<br />

Waals-like attraction term (more details are given also in Prausnitz’s book 49 ):<br />

PV<br />

RT<br />

2<br />

4η−2η = 1+<br />

r + −r<br />

( 1−η)<br />

⎩⎪<br />

⎧<br />

⎪(<br />

1−η/ 2)<br />

( 1 ) ⎨<br />

( 1−η)<br />

3 3<br />

()<br />

⎫ 2<br />

⎪ r a T<br />

−1⎬<br />

−<br />

RTV<br />

⎭⎪<br />

[4.4.99]<br />

where:<br />

η reduced density or packing fraction<br />

a attractive van der Waals-like parameter<br />

r chain segment number<br />

The reduced density or packing fraction η is related to an effective and temperature-dependent<br />

co-volume b(T) by η = r b(T)ρ/4, with ρ being the number density, i.e., the<br />

number <strong>of</strong> molecules per volume. However, PHSC-theory does not use an analytical<br />

intermolecular potential to estimate the temperature dependence <strong>of</strong> a(T) and b(T). Instead,<br />

empirical temperature functions are fitted to experimental data <strong>of</strong> argon and methane (see<br />

also 49 ).<br />

We note that the PHSC equation <strong>of</strong> state is again an equation where three parameters<br />

have to be fitted to thermodynamic properties: σ, ε/k and r. These may be transformed into<br />

macroscopic reducing parameters for the equation <strong>of</strong> state by the common relations T*=ε/k,<br />

P*=3ε/2πσ 3 and V* = 2πrσ 3 /3. Parameter tables are given in Refs. 86,260,372-374 PHSC was successfully<br />

applied to calculate solvent activities in polymer solutions, Gupta and Prausnitz. 86<br />

Lambert et al. 374 found that it is necessary to adjust the characteristic parameters <strong>of</strong> the polymers<br />

when liquid-liquid equilibria should correctly be calculated.<br />

Even with simple cubic equations <strong>of</strong> state, a quantitative representation <strong>of</strong> solvent activities<br />

for real polymer solutions can be achieved, as was shown by Tassios and coworkers.<br />

375,376 Using generalized van der Waals theory, Sako et al. 377 obtained a three-parameter<br />

cubic equation <strong>of</strong> state which was the first applied to polymer solutions:<br />

where:<br />

PV<br />

RT<br />

aT ()<br />

( + )<br />

V − b + bc<br />

= −<br />

V −b<br />

RT V b<br />

a attractive van der Waals-like parameter<br />

b excluded volume van der Waals-like parameter<br />

[4.4.100]

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