Mf. Defreitas et Jc. Pinto, DYNAMICS OF CONTINUOUS ISOBUTYLENE CATIONIC POLYMERIZATIONS, Journal of applied polymer science, 60(8), 1996, pp. 1109-1126
Polyisobutylene can be produced in either continuous cationic precipit
ation or solution polymerization reactors. It is known that the open-l
oop behavior of polymerization reactors may be very complex and may le
ad to oscillatory behavior, which is usually caused by thermal positiv
e feedback (due to the large heats of reaction of polymerization react
ions) and high viscosity effects (such as the gel effect in radical po
lymerization reactors and the decrease of heat transfer coefficients a
t high polymer concentrations). Oscillatory behavior may be observed i
n industrial isobutylene reactors, and it is intended to know whether
these oscillations are inherent to the kinetic mechanism. Based on pub
lished experimental data, mathematical models are developed for both s
olution and precipitation processes. Steady-state solutions are calcul
ated and steady-state stability is analyzed. Dynamic simulations and s
tability results reveal that only single stable steady-state solutions
are possible for such reactors at usual operation conditions, which m
eans that oscillatory behavior is not intrinsic to the reaction mechan
ism. (C) 1996 John Wiley & Sons, Inc.