Abstract:
A new model-free control (MFC) is proposed for the single-input and multi-output system.MFC consists of linear control strategy and nonlinear control strategy with control variables constraints.The convergence of MFC algorithm and the stability of MFC system are studied.MFC is used for direct optimal productivity control of continuous stirred tank fermenter using the dulation rate as the manipulated input.Excellent simulation results are obstained by using MFC without requiring the process model.