Abstract

Reactive distillation (RD) is a favourable alternative to conventional series of reaction-separation processes. Control of RD is challenging due to its integrated functionality and complex dynamics. Linear PID algorithm is not satisfactory and needs because of the need for adequate retuning over a wide range of operating conditions. Combined gain-scheduling and multimodel control scheme is proposed to handle the nonlinearities of the process. Simulation results show the superior performance of the proposed method to that of a standard PI control.

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