New Configurations of Atmospheric Distillation Unit by Heat Integration: Energy & Utility Water Consumption
محل انتشار: ششمین کنفرانس بین المللی شیمی و مهندسی شیمی
سال انتشار: 1398
نوع سند: مقاله کنفرانسی
زبان: انگلیسی
مشاهده: 626
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شناسه ملی سند علمی:
IRCCE06_054
تاریخ نمایه سازی: 9 فروردین 1399
چکیده مقاله:
Crude oil distillation process is a major consumer of energy and demands 35-45% of the total energy consumed in a refinery unit. The main target of this research is to maximize the heat recovery in this unit and minimize the required superheat flows. To this end, different raw crude oils have been studied to warm up in two different configurations to evaluate the performance of atmospheric distillation unit. The simulation results showed that the plant energy consumption in two proposed configurations of cold-to-warm and warm-to-cold is significantly reduced to 20.52% and 18.97%, respectively.
کلیدواژه ها:
نویسندگان
Arvin Ayazi
Chemical Engineering, Department of Chemical Engineering, Faculty of Engineering, Arak University, Arak, Iran
Mehdi Hajjary
Mechanical Engineering, Department of Mechanical Engineering, Petroleum University of Technology
Meysam Soleymani
Assistant Professor of Chemical Engineering, Department of Chemical Engineering, Faculty of Engineering, Arak University, Arak, Iran