Abstract
This paper deals with the feedback stabilization of the operation of a simple hybrid chemical plant at an optimally scheduled operation. The optimally scheduled plant operation is obtained as a solution of a cyclic discrete time scheduling optimization problem and it is open loop unstable. The goal is to illustrate how the stability problem of an hybrid chemical process can be solved by using simple P and PI – like control laws. The sensitivity of the closed loop plant operation to the choice of the controllers parameters is also presented.
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.
