Nonlinear analysis of the control problem in a continuous copolymerization reactor

Abstract

In this work we study the multi-input multi-output nonlinear control regulation of production composition, volume and temperature in a continuous copolymerization reactor with nonlinear tools and with suitable election of inputs and outputs, solvability by dynamic state feedback is established. A basic characterization of control structure and of required information on measured signals, the results are interpreted in physical forms. Numerical simulations are used to test the control scheme.<>