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n - PATh :.: Process and Product Applied Thermodynamics research ...

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Modeling<br />

The mixture parameters a <strong>and</strong> b are calculated from the parameters of the pure<br />

components aii <strong>and</strong> bii using the one fluid van der Waals mixing rules<br />

∑∑<br />

a z z a<br />

(III.37)<br />

= i j<br />

∑<br />

= i<br />

i<br />

j<br />

ij<br />

b zibi<br />

(III.38)<br />

where zi is the phase mole fraction of component i. The combining rule used for a is<br />

( )( ) 2 / 1<br />

k a a<br />

aij = 1− ij ii jj<br />

(III.39)<br />

The kij is an adjustable parameter for each binary mixture. The kij´s fitted to the<br />

experimental solubility data obtained in this work for O2/n-perfluoroalkanes, show strong<br />

temperature dependence mainly for perfluoro-n-hexane <strong>and</strong> perfluoro-n-heptane where a<br />

quadratic equation of the type<br />

k ij<br />

B C<br />

= A + +<br />

(III.40)<br />

2<br />

T T<br />

had to be used in order to correctly describe the experimental data (Coutinho et al.,<br />

1994).The coefficients A, B <strong>and</strong> C for the systems studied in this work are given in<br />

Table III.4.<br />

Table III.4. Coefficients for Equation III.40 <strong>and</strong> Average Binary Interaction Parameters, for all the<br />

Temperatures. AAD is the Corresponding Average Absolute Errors for Binary Oxygen-<br />

Perfluoroalkane Mixtures When an Averaged k is Used<br />

ij<br />

System A B C k AAD %<br />

ij<br />

O2 – C6F14<br />

O2 – C7F16<br />

3.66 x 10 1<br />

2.20 x 10 1<br />

-2.08 x 10 4<br />

-1.26 x 10 4<br />

2.94 x 10 6<br />

1.80 x 10 6<br />

0.122 12.35<br />

0.091 10.07<br />

O2 – C8F18 0.658 -196.42 -- 0.004 2.64<br />

O2 – C9F20 0.481 -165.10 -- -0.073 2.95<br />

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