Operating Conditions on Coupling Reactor Assisted by Two Membrane Concept for FT Synthesis
محل انتشار: چهارمین کنفرانس علوم و مهندسی جداسازی
سال انتشار: 1396
نوع سند: مقاله کنفرانسی
زبان: انگلیسی
مشاهده: 788
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شناسه ملی سند علمی:
CSSE04_104
تاریخ نمایه سازی: 13 شهریور 1396
چکیده مقاله:
Auto-thermal heat exchanger configurations are recognized as a novel concept in process intensification. In the current study, the influence of operating conditions in a novel coupling reactor with two different membranes is investigated for FT synthesis process. Fischer-Tropsch (FT) synthesis takes place in the exothermic side and supplies the necessary heat for the endothermic dehydrogenation of cyclohexane reaction. The performance of the reactor is numerically investigated for various key operating variables such as inlet molar flow rates of exothermic and endothermic streams and Pd/Ag membrane thickness. The reactor performance is analyzed based on hydrogen recovery yield, cyclohexane conversion and gasoline yield.
کلیدواژه ها:
Operating Conditions ، Coupling reactor ، Two membrane ، FT synthesis ، Hydrogenation of cyclohexane to benzene
نویسندگان
M Bayat
Department of chemical Engineering, Faculty of Engineering, University of Bojnord, Bojnord, Iran