Jy. Kim et Rl. Laurence, MATHEMATICAL-MODEL AND ANALYSIS OF PMMA SOLUTION PROCESSES, The Korean journal of chemical engineering, 15(3), 1998, pp. 287-296
A mathematical model of reactors for the polymerization of methylmetha
crylate (MMA) has been developed and analyzed in order to better under
stand the reactor dynamics and to determine conditions for improved op
eration. The exploration of the effect of heat transfer in an MMA poly
merization reactor system has been conducted by the development of a d
etailed model. Two correlations for the overall heat transfer coeffici
ent have been used to study the effect of heat transfer. The heat tran
sfer coefficient estimated by an empirical correlation (Kravaris) is o
nly a function of conversion. Due to its simplicity, it may not expres
s very well the true heat transfer phenomena. But in Henderson's corre
lation, it is related to the viscosity of the reaction mixture, which
in turn depends on the reaction temperature and volume fraction of eac
h species in the reactor. The steady state solutions of mass and energ
y balances in the reactor depend on the nature of the heat transfer co
rrelation, as does the number of isola branches. Henderson's correlati
on may be preferred to calculate the dynamics of the PMMA reactors. Th
e addition of jacket dynamics to the system results in no isola soluti
on branches and no Hopf bifurcations.