Abstract
Desalination MSF plant controlled by conventional one parameter controllers through operator interface stations show enough stability at steady state conditions. Load variation is frequently needed in large evaporator units. Hence, it becomes a hard task for the operator to control the distillate product flow rate without disturbing the plant equilibrium. A computer supervisory load variation control program is introduced as applied in MSF plants in the Arabian Gulf area which are engineered by the Office of Dr. M.H. Ali El-Saie, Consulting Engineers, Cairo (Egypt) and Kuwait.
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.
