Most chemical processes are nonlinear in nature and large setpoint changes
or load disturbances make such processes more challenging for control. Rece
ntly a simple transition control structure was introduced so that the trade
off between nominal performance and robust stability of the model with larg
e uncertainties is converted into the development of several models with sm
all uncertainties in such a way that the former problem can be solved satis
factorily. In this work, a modification to that transition control structur
e is proposed to address nonlinear systems. The performance of this transit
ion control structure is demonstrated on a nonlinear pH neutralization proc
ess. The simulation results show that the proposed structure has good prope
rties not only for setpoint changes but also for disturbance rejection.