13.02.2013 Views

R7.1 Polymerization

R7.1 Polymerization

R7.1 Polymerization

SHOW MORE
SHOW LESS

You also want an ePaper? Increase the reach of your titles

YUMPU automatically turns print PDFs into web optimized ePapers that Google loves.

369<br />

Chap.<br />

Now that we can determine the monomer concentration as a function of<br />

time, we will focus on determining the distribution of dead polymer, Pj.<br />

The<br />

concentrations of dead polymer and the molecular weight distribution can be<br />

derived in the following manner. 5 The probability of propagation is<br />

Simplifying<br />

(<strong>R7.1</strong>-22)<br />

In the absence of chain transfer, the monomer concentration, M,<br />

can be determined<br />

from Equation (<strong>R7.1</strong>-22) and concentration of initiator, I2,<br />

from Equation<br />

(<strong>R7.1</strong>-19). Consequently we have � as a function of time. We now set<br />

to use in the Flory distribution.<br />

It can be shown that in the absence of termination by combination, the<br />

mole fractions yj<br />

and weight fraction wj<br />

are exactly the same as those for step<br />

polymerization. That is, we can determine the dead polymer concentrations<br />

and molecular weight distribution of dead polymer in free radial polymerization<br />

for the Flory distributions. For example, the concentration of dead polymer<br />

of chain length n is<br />

⎛ � ⎞<br />

where ⎜ Pn is the total dead polymer concentration and<br />

⎝�⎟ ⎠<br />

(<strong>R7.1</strong>-6)<br />

which is the same as the mole fraction obtained in step polymerization, i.e.<br />

Equation (<strong>R7.1</strong>-6).<br />

If the termination is only by disproportionation, the dead polymer Pj<br />

will<br />

have the same distribution as the live polymer .<br />

5<br />

n�2<br />

Rate of propagation<br />

� � ---------------------------------------------------------------------------------------------------- � --------------<br />

Rate of propagation � Rate of termination �<br />

k p MR �<br />

�<br />

k p MR� ks SR� km MR� kcCR� kt R� ( ) 2<br />

� -----------------------------------------------------------------------------------------------------------<br />

� � � �<br />

k p M<br />

� � -----------------------------------------------------------------------------------------------<br />

� � � � ( )<br />

k p M k m M k cC k s S 2k t k o f I 2<br />

� � p<br />

⎛ � ⎞ ⎛ � ⎞<br />

Pn � yn ⎜ P � j⎟<br />

� ⎜ P j<br />

⎝ ⎠ ⎝�⎟ ( 1 � p)<br />

⎠<br />

j�2<br />

j�2<br />

yn ( 1 � p)pn�1<br />

�<br />

E. J. Schork, P. B. Deshpande, and K. W. Leffew, Control of <strong>Polymerization</strong> Reactor<br />

(New York: Marcel Dekker, 1993).<br />

R<br />

j<br />

pn�1<br />

r p<br />

r p rt

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!