In this work, DMC (Dynamic Matrix Control) of a batch solution polymerizati
on reactor has been investigated experimentally and by simulation to achiev
e a specific constant number average chain length and conversion in a minim
um time. The process variables are reaction temperature and initiator initi
ation concentration. The performance of the DMC controller was compared wit
h that of the IMC (Internal Model Control) controller. It was seen that DMC
and IMC controllers yielded a good performance in maintaining the reactor
temperature at its set point at the isothermal conditions.