Mohamad Hafizi Zakria - School of Chemical and Energy Engineering, Faculty of Engineering, Universiti Teknologi Malaysia, ۸۱۳۱۰, Johor, Malaysia
Mohd Ghazali Mohd Nawawi - School of Chemical and Energy Engineering, Faculty of Engineering, Universiti Teknologi Malaysia, ۸۱۳۱۰, Johor, Malaysia
Mohd Rizal Abdul Rahman - Steam Cracker Complex, Manufacturing Division, Pengerang Integrated Refining Complex, ۸۱۶۰۰, Johor, Malaysia
Mohd Anas Saudi - Steam Cracker Complex, Manufacturing Division, Pengerang Integrated Refining Complex, ۸۱۶۰۰, Johor, Malaysia

The research was carried out in a large-scale olefin process to see how different variables affect ethylene yield in an actual fluctuating plant condition. Regression analysis was adopted using Minitab Software Version ۱۸ to create a reliable ethylene yield model. Regression analysis is a robust, practical, and advanced tool that is used in various applications as an alternative to the complex, expensive, and restricted simulation software that is specifically designed for the olefin process. The ۱۶۸۸ data taken from the studied plant underwent outliers and residuals removal utilizing normality and stability tools in Minitab for the analysis to be conducted as normal data. The Regression was conducted a few times until all variables satisfactorily met the multicollinearity criteria with Variance Inflation Factor (VIF) < ۱۰ and ۹۵% confidence level criteria with P-Value < ۰.۰۵. The final Regression model established ۴ significant variables which were Hearth Burner Flow, Integral Burner Flow, Super High- Pressure Steam (SHP) Temperature, and Naphtha Feed Flow by factors of -۰.۰۰۱۲۶۶, ۰.۰۴۵۱۵, -۰.۰۷۹۵, and ۰.۲۱۰۵, respectively. The maximum ethylene yield was calculated at ۳۱.۷۵% using Response Optimizer with the recommended operating conditions at ۹۹۰۸.۵۰ kg/h Hearth Burner Flow, ۶۰۰.۳۹ kg/h Integral Burner Flow, ۴۹۴.۶۵°C SHP Temperature, and ۶۳.۵۰ t/h Naphtha Feed Flow.

Olefin yield, steam cracker furnace, optimization, statistical analysis, minitab