Dynamic matrix control (DMC) was used to neutralize a continuous proce
ss stream in a stirred tank. In the presence of large disturbances, th
e controller performance deteriorated because of process-model mismatc
h. An adaptive DMC was successful in overcoming this difficulty. A clo
sed-loop online method has been developed for identification of a proc
ess in terms of pseudo impulse response coefficients. Using this schem
e a first-order with delay time model was fitted to the process. This
model was subsequently used to update the dynamic matrix thus making t
he DMC algorithm adaptive.