این سایت در حال حاضر پشتیبانی نمی شود و امکان دارد داده های نشریات بروز نباشند
Iranian Journal of Chemistry and Chemical Engineering، جلد ۴۴، شماره ۳، صفحات ۸۴۶-۸۵۷

عنوان فارسی
چکیده فارسی مقاله
کلیدواژه‌های فارسی مقاله

عنوان انگلیسی Comparative Simulation of PI and Fuzzy Control for Fluid Catalytic Cracking Unit
چکیده انگلیسی مقاله The fluid catalytic cracking unit converts heavy material feeds into more useful gasoline and oil products and represents an essential component in refineries. The variables, including gas oil supply temperature (Tf), gas oil supply flow rate (Ff), and air temperature (Ta), are controlled and manipulated by this unit, which poses a significant challenge due to its complex interactions. To address these complexities, this study investigates the control of riser and regenerator temperatures (TR, TG) in an industrial Universal Oil Products (UOP) fluid catalytic cracking unit using proportional-integral and fuzzy logic controllers. The fuzzy logic controller, with five fuzzy sets generating 25 rules, is implemented through MATLAB simulation. The simulation program is formulated based on the principles of mass and energy balance of the unit. The performance of the controllers, including PI and fuzzy logic controllers, is evaluated and compared by introducing disturbances in the gas oil supply temperature, gas oil supply flow rate, and air temperature. The results show that the fuzzy logic controller outperforms the PI controller, exhibiting a lower integral absolute error. Compared to the PI controller, the fuzzy logic controller demonstrates improved performance, characterized by stable responses and shorter settling times. These findings highlight the effectiveness of the fuzzy logic controller in achieving better control performance for Fluid Catalytic Cracking Units (FCCU).
کلیدواژه‌های انگلیسی مقاله Riser,regenerator,MATLAB simulation,Proportional Integral Controller (PID),Fuzzy Controller

نویسندگان مقاله Safa Khalaf Atiyaha |
Petroleum Systems Control Engineering Department, College of Petroleum Processes Engineering, Tikrit University, Tikrit, IRAQ

Buthainah Ali AL-Timimi |
Chemical Engineering Department, University of Technology –Iraq, Alsinaa Street 52, 10066 Baghdad, IRAQ

Ahmed Yaseen Ali |
Modeling and Design Program, Atilim University, Ankara, 06830, TURKEY

Mohamed Salih Ahmed |
Mechanical Engineering Department, College of Engineering, Tikrit University, Tikrit, 3400, IRAQ

Talib M. Albayati |
Chemical Engineering Department, University of Technology –Iraq, Alsinaa Street 52, 10066 Baghdad, IRAQ

Ghassan H. Abdullah |
Oil and Gas Refining Engineering Department, College of Petroleum Process Engineering, Tikrit University, IRAQ

Maizirwan Mel |
Chemical Engineering and Sustainability Department, Faculty of Engineering, International Islamic University of Malaysia (IIUM), Gombak, 50728, Kuala Lumpur, MALAYSIA


نشانی اینترنتی https://ijcce.ac.ir/article_719357_45713e6fbaf2464c9803acc3733132ff.pdf
فایل مقاله فایلی برای مقاله ذخیره نشده است
کد مقاله (doi)
زبان مقاله منتشر شده en
موضوعات مقاله منتشر شده
نوع مقاله منتشر شده
برگشت به: صفحه اول پایگاه   |   نسخه مرتبط   |   نشریه مرتبط   |   فهرست نشریات