Abstract
Abstract The design of a model reference cascade controller is analyzed for the control of a nonlinear system [xdot] = f(x) + g(x)u + d(t), y = cx which has a relative order two. Integral and derivative control actions are incorporated in the control law. Theoretical analysis on robustness of the proposed control scheme under process/model parameters uncertainty is provided. The controller design method is applied theoretically to the concentration control of a non-isothermal CSTR which has a severe nonlinearity and steady-state multiplicities.
Sign-in/Register to access full text options 
Talk to us
Join us for a 30 min session where you can share your feedback and ask us any queries you have
Schedule a callDisclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.
