Abstract
Controlling the level in the nonlinear process is hectic because of its shape. In many industries the flow and level control plays a vital role. Controlling the level in the conical tank is a challenging process because of its nonlinearity and constantly changing of cross section with respect to height. The Model for a conical tank was identified for different operating regions which were best approximated to first order plus dead time model. For the identified model different controllers such as Direct Synthesis Proportional Integral (DSPI) and Model Predictive Control (MPC) were designed and compared.
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.
