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International Journal of Engineering، جلد ۲۶، شماره ۶، صفحات ۵۶۳-۵۷۰
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عنوان فارسی |
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چکیده فارسی مقاله |
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کلیدواژههای فارسی مقاله |
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عنوان انگلیسی |
A Two-step Catalytic Production of Biodiesel from Waste Cooking Oil |
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چکیده انگلیسی مقاله |
Waste cooking oil (WCO) was used as a potential feedstock for biodiesel production. High levels of free fatty acids (9.85% w/w) in WCO made it an undesirable substrate for direct transesterification reaction. To solve this issue, a two-step process was implemented in this research. Firstly, esterification reaction was performed in presence of sulfuric acid as a common acid catalyst to reduce the amount of FFA to less than 1.5% w/w. The triglycerides (TGs) in WCO were transesterified with methanol catalyzed by potassium hydroxide in the second step of reaction. Several effective parameters were evaluated in terms of reaction temperature (323-363 K), reaction time (0.5-3 h) and catalyst concentration (0-5.52% w/w). The optimum reaction conditions were defined as the reaction temperature of 355 K, reaction time of 3 h and catalyst concentration of 3.68~ 4% w/w, in which maximum FFA conversion of 87 wt% was obtained. The biodiesel synthesis condition in the second stage was defined as the reaction temperature of 338 K, methanol/ WCO molar ratio of 6:1, KOH concentration of 1% w/w and reaction time of 90 min; under these conditions, maximum triglyceride (TG) conversion of 96.66 wt% was obtained. |
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کلیدواژههای انگلیسی مقاله |
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نویسندگان مقاله |
A.A. Ghoreyshi | Chemical Eng., BNUT
Maryam Hassani | Chemical Eng, BNUT
Ghasem Najafpour | Biochemical & Chemical Engineering, Noshirvani University of Technology, Babol
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نشانی اینترنتی |
http://www.ije.ir/article_72126_eb1089187e631007c953f639eabe769e.pdf |
فایل مقاله |
اشکال در دسترسی به فایل - ./files/site1/rds_journals/409/article-409-2062897.pdf |
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زبان مقاله منتشر شده |
en |
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