A parameter estimation procedure was developed to fit a kinetic model with
the experimental data obtained from methyl methacrylate (MMA) solution poly
merization in a 10 L batch reader. For molecular weight control, we applied
the modified two-step method in calculating the optimal temperature trajec
tory on the basis of the identified kinetic model. Application of a convent
ional proportional-integral (PI) controller to track the temperature trajec
tory proved to be acceptable in a conventional batch reactor with both heat
ing and cooling systems. Experimental results revealed that the identified
model is accurate; therefore, one can rely on the calculated optimal temper
ature trajectories to ensure that the polymer product quality conforms to t
he specification.