Nr. Sripada et Dg. Fisher, A state space model based multistep adaptive predictive controller (MAPC) with disturbance modeling and Kalman filter prediction, I J CHEM T, 6(4), 1999, pp. 225-236
A multistep adaptive predictive control strategy based on a state space mod
el of the process has been developed. It can he compared with the Generaliz
ed Predictive Control algorithm. The emphasis in the development of the pro
posed control scheme is on modeling and elimination of disturbances. In the
proposed scheme any prior information regarding the disturbances can be in
corporated (by specifying certain polynomials and/or the noise covariances)
. If no prior information is available then the unknown unmodeled effects (
such as noise, unmeasured load-disturbances and model process mismatch) can
be represented by a residual model which can best be identified in a two-s
tage setting. This approach leads to satisfactory modeling of disturbances
and good regulation via predictive control. Some important features of the
proposed algorithm are: (i) it uses a state space model which allows separa
te modeling of u-to-y process dynamics, process and measurement noise; this
is not possible in an ARMAX-type input/output model where process and meas
urement noise appear lumped in the noise polynomial; (ii) it uses a Kalman
Filter (KF) to generate the predictions of the output; the KF can be easily
tuned via noise covariances and is a simpler and better alternative to spe
cifying or estimating a noise polynomial; (iii) there is no need to solve a
Diophantine identity on-line; the result is reduced computation; and (iv)
if residual modeling is used it leads to simpler and improved way of handli
ng disturbances. The proposed control algorithm is presented for the single
-input, single-output case. Applying the algorithm to multivariable process
es is straightforward. Simulation examples are included to illustrate the a
dvantages and performance of the proposed control scheme.