Soybean Oil Transesterification Reactions in the Presence of Mussel Shell: Pseudo-First Order Kinetics

سال انتشار: 1397
نوع سند: مقاله ژورنالی
زبان: انگلیسی
مشاهده: 200

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شناسه ملی سند علمی:

JR_IJCCE-37-4_004

تاریخ نمایه سازی: 17 خرداد 1404

چکیده مقاله:

Calcium oxide is one of the appropriate catalysts for biodiesel production. In this study, cheap and compatible with environment catalyst has been used. Mussel shell of Persian Gulf coast is one of the sources of calcium carbonate that is converted to calcium oxide at calcination temperature up to ۹۵۰°C. Transesterification reaction was carried out at optimum condition of our previous study (calcination temperature of ۱۰۵۰°C, methanol to oil ratio of ۲۴:۱ and catalyst to oil ratio of to ۱۲ wt.%) in a ۲۵۰mL two-necked flask. In this study, the effects of stirrer speed (۲۵۰ and ۳۵۰rpm), the reaction temperature (۳۲۸.۱۵, ۳۳۳.۱۵, and ۳۳۸.۱۵K) and reaction time (۱, ۳, ۵, ۷ and ۸h) on the methyl ester conversion were investigated. The methyl ester conversion, in stirrer speed of ۲۵۰rpm, reaction temperatures of ۳۲۸.۱۵ and ۳۳۳.۱۵K and reaction times of less than ۵h is too low. But at the reaction temperature of ۳۳۸.۱۵K (near to methanol boiling point), the mixing is increased slightly and the reaction occurs at a higher rate and the methyl ester conversion is increased. These results indicate that diffusion has a significant role in the methyl ester conversion rate in the heterogeneously catalyzed reaction. In stirrer speed of ۳۵۰rpm, the diffusion problem has been solved somewhat and the reaction in the catalyst surface is the controller of the overall reaction rate. In this stirrer speed (۳۵۰rpm) the methyl ester conversion versus time in all temperature shows pseudo-first-order kinetics. Firstly, the rate was determined at the various temperatures and then the activation energy for the transesterification reaction of soybean oil with methanol was obtained in the presence of mussel shell as the catalyst. Results demonstrate the high precision of the pseudo-first-order kinetics model regard to methyl esters concentration.

نویسندگان

Majid Mohadesi

Chemical Engineering Department, Faculty of Energy, Kermanshah University of Technology, Kermanshah, I.R. IRAN

Gholamreza Moradi

Catalyst Research Center, Faculty of Chemical and Petroleum Engineering, Razi University, Kermanshah, I.R. IRAN

Yegane Davoodbeygi

Catalyst Research Center, Faculty of Chemical and Petroleum Engineering, Razi University, Kermanshah, I.R. IRAN

Shokoufe Hosseini

Catalyst Research Center, Faculty of Chemical and Petroleum Engineering, Razi University, Kermanshah, I.R. IRAN

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