This paper is concerned with multivariable predictive control and its imple
mentation in thermal treatment processes. The choice of a control structure
that ensures decoupling is discussed. A unified predictive controller is u
sed to implement the monovariable control systems for each channel of the d
ecoupled plant. Aspects of the modelling and performance of the control sch
eme are dealt with and illustrated by plant results. The model of the therm
al treatment processes has been used to check the controller behaviour befo
re its real implementation and some simulation results are also given. (C)
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