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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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4.4 Measurement <strong>of</strong> solvent activity 201<br />

~ / 13<br />

~ ~<br />

PV V<br />

~ ~<br />

T V q T V V<br />

/ ~ ⎛<br />

⎞<br />

2 . .<br />

=<br />

−<br />

⎜12045<br />

1011<br />

−<br />

⎟<br />

13 ⎜ ~ 2 ~ 4 ⎟<br />

−0.<br />

8909 ⎝<br />

⎠<br />

[4.4.77]<br />

where the reduced variables and characteristic parameters have the same definitions as in<br />

the Flory model above. Equation [4.4.77] is formally identical with Prigogine’s result, except<br />

for the additional constant parameter q, which can also be viewed as a correction to the<br />

hard-core cell volume. The value <strong>of</strong> q = 1.07 corresponds approximately to a 25% increase<br />

in the hard-core volume in comparison with the original Prigogine model. Characteristic parameters<br />

for this model are given in Refs. 249,262 The final result for the residual solvent activity<br />

in a binary polymer solution reads:<br />

~<br />

* * ~ .<br />

ln ln<br />

.<br />

/<br />

~ /<br />

13<br />

residual PV 1 1 V1 −08909q<br />

⎛<br />

12045 12045 05055 0505<br />

a1<br />

= 3T1<br />

+<br />

⎜ . .<br />

⎞<br />

−<br />

⎟ . . 5<br />

− −<br />

13<br />

2 2<br />

4<br />

RT<br />

⎜ ~ ~ ⎟ ~<br />

4<br />

V −08909q ⎝ V1 V ⎠ V1<br />

V ~<br />

⎡<br />

⎛<br />

⎞⎤<br />

⎢<br />

⎜<br />

⎟⎥<br />

⎢<br />

⎜<br />

⎟⎥<br />

⎣<br />

⎝<br />

⎠⎦<br />

* 2<br />

V<br />

~ ⎛<br />

⎞ *<br />

1θ2 ⎛<br />

⎞<br />

+ ⎜ −<br />

⎜12045<br />

. 0. 5055<br />

Χ12<br />

TQ12 V ⎟ −<br />

⎟ PV ~ ~<br />

1⎛<br />

⎞<br />

RT ⎝<br />

⎠⎜<br />

~ 2 ~ 4 ⎟<br />

+ ⎜V−V1⎟<br />

RT ⎝ ⎠<br />

⎝ V V ⎠<br />

[4.4.78]<br />

The last term in Equation [4.4.78] is again negligible at normal pressures, which is the<br />

case for the calculation <strong>of</strong> solvent activities <strong>of</strong> common polymer solutions. The reduced volume<br />

<strong>of</strong> the mixture is to be calculated from the equation <strong>of</strong> state where the same mixing<br />

rules are valid, as given by Equations [4.4.75, 4.4.76] if random mixing is assumed. Equation<br />

[4.4.78] is somewhat more flexible than Equation [4.4.74]. Again, entropic parameter<br />

Q 12 and interaction parameter X 12 have to be fitted to experimental data <strong>of</strong> the mixture.<br />

There is not much experience with the model regarding thermodynamic data <strong>of</strong> polymer solutions<br />

because it was mainly applied to polymer blends, where it provides much better results<br />

than the simple Flory model.<br />

To improve on the cell model, two other classes <strong>of</strong> models were developed, namely,<br />

lattice-fluid and lattice-hole theories. In these theories, vacant cells or holes are introduced<br />

into the lattice to describe the extra entropy change in the system as a function <strong>of</strong> volume<br />

and temperature. The lattice size, or cell volume, is fixed so that the changes in volume can<br />

only occur by the appearance <strong>of</strong> new holes, or vacant sites, on the lattice. The most popular<br />

theories <strong>of</strong> such kind were developed by Simha and Somcynsky 245 or Sanchez and<br />

Lacombe. 246-248<br />

The Sanchez-Lacombe lattice-fluid equation <strong>of</strong> state reads:<br />

~ ~<br />

PV<br />

V<br />

T<br />

r<br />

V 1 ~ −1 1<br />

= −1− ln −<br />

~<br />

~ ~ ~<br />

V VT<br />

~<br />

[4.4.79]<br />

where the reduced parameters are given in Equation [4.4.73], but no c-parameter is included,<br />

and the size parameter, r, and the characteristic parameters are related by<br />

P * V* = ( r / M) RT *<br />

[4.4.80]

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