An adaptive controller–observer scheme for temperature control of non‐chain reactions in batch reactors

Abstract

In this paper an adaptive controller–observer temperature control scheme is developed for a class of irreversible non-chain reactions taking place in batch reactors. The scheme is based on a nonlinear observer for the estimation of the heat released by the reaction, where the heat transfer coefficient is adaptively estimated. Tracking of the desired reactor temperature is achieved via a two-loop control scheme, where an independent adaptive estimate of the heat transfer coefficient is used as well. Remarkably, the observer and the controller can be designed and tuned separately. The convergence of both the nonlinear observer and of the overall controller–observer scheme is analyzed by resorting to a Lyapunov-like argument. A comparative simulation case study is developed to test the performance of the proposed scheme and compare it with other approaches already known in the literature

Fault diagnosis for a class of chemical batch processes

“…The model-based temperature controller proposed in [12] is adopted. A first-order linear dynamics (with a time constant equal to τ = 3 [s]) between the commanded control input (computed by the controller) and the real temperature of the water entering the jacket is introduced, but not modeled in the design of the controller and of the observers.…”