This paper concerns the nonlinear observer-based control design, which is m
ainly based on Fliess(1) linearization and parametrized transformation for
uncertain nonlinear processes. The proposed control scheme allows us to adj
ust the rate of tracking and the decay of observer error for regulating the
system output. Through the valid selection of tuning parameters of the out
put feedback controller, the bounded output tracking is achieved and its tu
ning scheme is robust against model uncertainties. The effectiveness of our
design method is demonstrated by a simulation example of the control of an
exothermic CSTR with multiple steady states. Under significant observer-in
itialization errors and unstable operating conditions of designs, the satis
factory output regulation and disturbance rejection are obtained.