Gasoline is mainly created by converting light and heavy naphtha from crude oil distillation column. Overhead temperature of main column is the most important parameter in quality control of gasoline. This protocol would offer two pathways to control the overhead temperature of crude oil distillation column in refinery. In this offer, temperature, flow parameters are cotrolled by proportional integral and derivative (PID) and fuzzy PID controllers. The feasibility and effectiveness of the proposed method are verified by the simulation results using Matlab/Simulink. |
