Abstract
This paper deals with the control of the temperature in non-isothermal stirred tank reactors involving M (M ≥ 1) chemical reactions. The proposed control algorithm is an input output linearization controller which accounts for the well-known process nonlinearities. The control scheme is also adaptive in order to deal with the parameter uncertainty, it is shown how to include explicit on-line estimates of the M activation energies within the adaptive linearizing controller. The performance of the control law is illustrated in simulation.
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