This paper discusses a method to improve the quality of temperature control
of the polyvinyl chloride (PVC) emulsion reactor by implementing Model Pre
dictive Control (MPC) and cascade control for this exponentially unstable p
rocess with very non-linear behaviour.
These methods were tested for different disturbances, and their performance
s were compared with those obtained with classical proportional-integral-de
rivative (PID) control.
Significant improvement of temperature control was achieved using MPC. The
process model used in MPC is presented.