R7.1 Polymerization
R7.1 Polymerization
R7.1 Polymerization
Create successful ePaper yourself
Turn your PDF publications into a flip-book with our unique Google optimized e-Paper software.
Rate of<br />
disappearance<br />
of monomer<br />
Rate of formation of<br />
dead polymers<br />
Monomer<br />
balance<br />
Initiator<br />
balance<br />
367<br />
Using Equation (<strong>R7.1</strong>-14) to substitute for<br />
monomer is<br />
The rate of disappearance of monomer,<br />
agation, :<br />
r<br />
p<br />
�rM � k p M R �<br />
�r M<br />
j�1<br />
Finally, the net rate of formation of dead polymer<br />
r P j<br />
The rate of formation of all dead polymers is<br />
rP<br />
� 0.5kta(<br />
R�)<br />
2<br />
<strong>R7.1</strong>.3 Modeling a Batch <strong>Polymerization</strong> Reactor<br />
Chap.<br />
(<strong>R7.1</strong>-15)<br />
R�,<br />
the rate of disappearance of<br />
(<strong>R7.1</strong>-16)<br />
�rM,<br />
is also equal to the rate of prop-<br />
Pj<br />
by addition is<br />
(<strong>R7.1</strong>-17)<br />
To conclude this section we determine the concentration of monomer as a<br />
function of time in a batch reactor. A balance on the monomer combined with<br />
the LCA gives<br />
�<br />
A balance on the initiator I2<br />
gives<br />
dM<br />
------- � k p M ∑ R j � k p MR�<br />
�<br />
dt<br />
Integrating and using the initial condition<br />
tion of the initiator concentration profile:<br />
�<br />
�<br />
�<br />
j<br />
k p MR�<br />
k p M 2k0<br />
( I2)<br />
f<br />
� --------------------<br />
r p<br />
0.5k ta<br />
r P<br />
� �rM<br />
�<br />
k�j�1<br />
�<br />
k�1<br />
�<br />
�<br />
j�1<br />
r P j<br />
� dI2 ------- �<br />
k0 I2 dt<br />
k<br />
t<br />
Rk<br />
R j�k<br />
k<br />
p<br />
M 2k0<br />
( I2)<br />
f<br />
--------------------<br />
k<br />
t<br />
(<strong>R7.1</strong>-18)<br />
I2<br />
� I20<br />
at t � 0, we obtain the equa