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44 No. p. 5353 ISSN 0888-5885 Ma, F. & Hanna, M. A. (1999). Biodiesel production: a review. Bioresource Technology, Vol. 70, No. p. 1-15, ISSN 09608524 MacLeod, C. , Harvey, A. , Lee, A. , & Wilson, K. (2008). Evaluation of the activity and stability of alkali-doped metal oxide catalysts for application to an intensified method of biodiesel production. Chemical Engineering Journal, Vol. 135, No. p. 63-70, ISSN 1385-8947 Madje, B. , Patil, P. , Shindalkar, S. , Shingare, M. S. & Dongare, M. K. (2004).
Vol. p. , & Hattori, Y. (2002). Catalysts for transesterification. S. Patent 6407269, June 18, 2002. K. & Chadha, A. (2005). Preparation of biodiesel from crude oil of Pongamia pinnata. p. , Matsubara, K. & Honda, K. (2009). Acceleration of catalytic activity of calcium oxide for biodiesel production. Bioresource Technology, Vol. 100, No. p. J. ) (2001). Nanoscale Materials in Chemistry, Jonh Wiley & Sons, Inc. ISBN 0471-38395-3, New York, United States. Körbitz, W. (1998). Multi-Feed-Stock-Biodiesel:The Modern & Profitable FAME.
2003) Rodrigues et al. (2008a) Watanabe et al. (2002) Watanabe et al. (2002) Du et al. (2004) Table 2. (Continued). Lipase-catalyzed reactions for biodiesel production in batch systems. An Overview of Enzyme-Catalyzed Reactions and Alternative Feedstockfor Biodiesel Production 35 Novozym 435 Crude and refined soybean oil Methyl acetate 92% yield Novozym 435 Soybean oil Ethanol 100% conversion 12:1 methyl acetate to oil molar ratio; 14h; 150rpm; 40°C; 30wt% enzyme (based on oil); 100 cycles of reuse with no loss of activity 6:1 ethanol to oil molar ratio; 6h; 1000rpm; 65°C; 50bar; 5wt% lipase (based on oil and ethanol); compressed propane (solvent to substrates weight ratio of 2:1) Du et al.