PI and PID controllers continue to be popular methods in industrial applica
tions. It is well known that linear PI and PID controllers result fi-om the
application of model-based controller design methods to linear first- and
second-order systems. It is shown that nonlinear PI and PID controllers res
ult from the application of nonlinear controller design methods to nonlinea
r first- and second-order systems. As a result, the controllers resulting f
rom nonlinear model-based control theory are put in a convenient form, more
amenable to industrial implementation. Additionally, the quantities used i
n the controller are useful for monitoring the process and quantifying mode
ling error. Chemical engineering examples are used to illustrate the result
ing control laws. A simulation example further demonstrates the performance
of the nonlinear controllers, as well as their useful process monitoring q
uantities.