In this paper, we propose a modified Smith predictor with a new structure f
or unstable processes. The proposed new structure makes it possible to use
the unstable model itself as a process model, while the previous modified S
mith predictors provided no option to use a mismatched stable process model
to guarantee stability. Accordingly, the proposed Smith predictor can pred
ict the dynamics of the actual process much better than previous approaches
. It also guarantees good robustness to modeling errors by separating servo
and regulatory problems. Moreover, it demonstrates good disturbance reject
ion performances because the adjustable parameters of the PID controller fo
r the regulatory problem are tuned systematically with an internal feedback
loop.