Although it is able to exploit the full power of optimal state variable fee
dback within a non-minimum state-space (NMSS) setting, the proportional-int
egral-plus (PIP) controller is simple to implement and provides a logical e
xtension of conventional proportional-integral and proportional-integral-de
rivative (PI/PID) controllers, with additional dynamic feedback and input c
ompensators introduced automatically by the NMSS formulation of the problem
when the process is of greater than first order or has appreciable pure ti
me delays. The present paper applies the PIP methodology to the ALSTOM benc
hmark challenge, which takes the form of a highly coupled multi-variable li
near model, representing the gasifier system of an integrated gasification
combined cycle (IGCC) power plant. In particular, a straightforwardly tuned
discrete-time PIP control system based on a reduced-order backward-shift m
odel of the gasifier is found to yield good control of the benchmark, meeti
ng most of the specified performance requirements at three different operat
ing points.