%% Adaptive MPC Control of Nonlinear Chemical Reactor Using Online Model Estimation % This example shows how to use an Adaptive MPC controller to control a % nonlinear continuous stirred tank reactor (CSTR) as it transitions from % low conversion rate to high conversion rate. % % A discrete time ARX model is being identified online by the Recursive % Polynomial Model Estimator block at each control interval. The adaptive % MPC controller uses it to update internal plant model and achieves % nonlinear control successfully.