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dc.contributor.authorKusmiyati, Kusmiyati
dc.date.accessioned2015-01-31T03:46:37Z
dc.date.available2015-01-31T03:46:37Z
dc.date.issued2015-01-24
dc.identifier.citationAstawan, Made, 2004,Ikan Yang Sedap dan Bergizi, Tiga Serangkai, Solo. Canakci, Mustofa, 2001, Production of Biodiesel from Feedstock with High Free Fatty Acids and Its Effect on Diesel Engine Performance and Emissions, Iowa State University, 74-126. Demirbas A.,2005, Biodiesel production from vegetable oils via catalytic and noncatalytic supercritical methanol transesterification methods. Progress in Energy and Combustion Science 31, 466– 487 Encinar, J.M., Gonzales, J.F., Rodriguez, J.J., and Tejedor, A., 2002, Biodiesel Fuels from Vegetable Oils: Transesterification of Cynara Cardunculus L. Oils with Ethanol, Energy and Fuels, 16, 443-450. Encinar, J.M., Gonzales, Juan F., and Rodriguez-Reinares, 2005, Biodiesel From Used Oil, Ind. Eng. Chem. Res., 44, 5491-5499. Gerpen, J.V., 2005, Biodiesel Processing and Production, Fuel Processing Technology 86, 1097-1107. Kusmiyati and Sugiharto A, 2010, Production of Biodiesel from Oleic Acid and Methanol by Reactive Distillation, Bulletin of Chemical Reaction Engineering & Catalysis, 5 (1), 1 – 6. Lotero E, Liu Y, Lopez DE, Suwannakarn K, Bruce D, and Goodwin JG, 2005, Synthesis of Biodiesel via Acid Catalysis, Ind. Eng. Chem. Res., 44, 5353-5363 Ma, F., Clements, L. Davis, and Hanna, Milford A., 1998, Biodiesel Fuels from Animal Fat.Accilary Studies Transesterification of Beef Tallow, Ind.Eng.Chem.Res., 37, 3768-3771. Ma, F., Clements, L. Davis, and Hanna, Milford A., 1999, The Effect of Mixing on Transesterification of Beef Tallow, Bioresoure Technology 69, 289-293. Mohamad I. Al-Widyan, Ali O. Al-Shyoukh. 2002. Experimental Evaluation Of The Transesterification of Waste Palm Oil into Biodiesel. Bioresource Technology . 85 (2002) 253–256 Narasiman, Jeyakumar, Mani and GuttuOfgaa, 2012, Effect of Neat Sardine Oil With Varies Blends On The Performance And Emission Characteristics of Diesel Engine, Science. Technology and Arts Research Journal, 1(4), 58-64. Noiroj, K., Intarapong, P., Luengnaruemitchai, A., and Jai-In, S., 2009, KOH/Al2O3 and KOH/NaY Catalyst for Biodiesel from Palm Oil, Renewable Energy, 84, 1145-1150. Ramadhas, A.S., Jayaraj,S., and Muraleedharan, C., 2005, Biodiesel Production from High FFA Rubber Seed Oil, Fuel, 84, 335-340. V.NarasimanA ,S.Jeyakumar B, M. Mani. 2012. Effect of Performance and Emission Characteristics on Methyl Esters of Sardine Oil Fuelled in Diesel Engine with Various Blends. Journal of Mechanical Engineering Research And Development (IJMERD), Volume 2, Number 1. 17-26 Y. Zhang , M.A. Dub, D.D. McLean, M. Kates. 2003. Biodiesel Production From Waste Cooking Oil: 2. Economic Assessment And Sensitivity Analysis. Bioresource Technology 90 . 229–240 Y. Zhang A, M.A. Dub_E A, D.D. Mclean A, M. Kates. 2003. Review Paper Biodiesel Production From Waste Cooking Oil: 1. Process Design And Technological Assessment. Bioresource Technology 89 . 1–16 Zahidah, Nurulfitri R. 2011.Utilization Of Liquid Waste By-Product of The fish Canning As Raw Materials For Biodiesel As Alternative Energy Sources, International Conference On Chemical, Biological And Environment Sciences (ICCEBS'2011), Bangkoken_US
dc.identifier.issn2407 - 9189
dc.identifier.urihttp://hdl.handle.net/11617/5108
dc.description.abstractThis study utilized the oil derived from fish waste as raw material. Biodiesel production from fish waste oil was carried out using a catalytic reaction with two stages processes: esterification and transesterification. The first step was the esterification process using an acid catalyst (H2SO4) to reduce the free acid content in waste fish oil. Then, it was followed by transesterification in the second step using alkaline catalyst (NaOH or KOH) to convert the oil into biodiesel. In the esterification reaction,waste fish oil was reacted with methanol at 60 °C and 2% H2SO4 catalyst in a three-neck flask apparatus for various times (2, 3, 4 hours) with various stirring speeds (500, 600, 700 rpm) and temperatures ( 50, 60, 70 °C). The results of esterification were used for transesterification. It was mixed with methanol (molar ratio 1: 6), 2% NaOH catalyst in a three-neck flask apparatus. The optimum conversion 66.09% was obtained at 60 ° C for 4 hours. The effect of stirring speed shows that at the speed of 700 rpm for 4 hours, the maximum conversion 68.03% was obtained. The effect of alkaline catalyst types showed that optimum conversion was obtained using KOH (88.99%).en_US
dc.publisherLPPM UMSen_US
dc.subjectbiodieselen_US
dc.subjectwaste fish oilen_US
dc.subjectesterificationen_US
dc.subjecttransesterificationen_US
dc.titleFish Waste Oil Conversion For Biodiesel Production Using Two Stages Reactionen_US
dc.typeArticleen_US


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