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Boreskov Institute of Catalysis of the Siberian Branch of Russian ...

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PP-V-10composition (methyl esters, mono-, di and triglycerides content) was determined by GCanalysisusing tricaprin as internal standard.Results and discussionIn <strong>the</strong> performed reaction conditions (140°C, 24 hours, 15% wt <strong>of</strong> catalyst respect to oil,oil:methanol molar ratio equal to 1:10) <strong>the</strong> potassium silicate shows <strong>the</strong> highest oleic acidconversion value (93%), followed by <strong>the</strong> sodium silicate with a conversion value <strong>of</strong> 88%.Among <strong>the</strong> zeolites, <strong>the</strong> K-Silicalite-1 allows to reach <strong>the</strong> 50% <strong>of</strong> conversion, with respect <strong>the</strong>20% <strong>of</strong> <strong>the</strong> Fau-X. To achieve a conversion value comparable with <strong>the</strong> basic catalyst, <strong>the</strong> acidzeolites require <strong>the</strong> increasing <strong>of</strong> <strong>the</strong> temperature and methanol amount. These results suggestthat <strong>the</strong> faster reaction rate achieved using silicates could be due to <strong>the</strong> presence <strong>of</strong> base siteson amorphous surface <strong>of</strong> <strong>the</strong>se catalysts. At <strong>the</strong> same time, <strong>the</strong> weak acid sites also present onsilicates surface allow to achieve an acid esterification <strong>of</strong> <strong>the</strong> free fatty acid, avoiding <strong>the</strong> soapformation.In <strong>the</strong> transesterfication <strong>of</strong> an olive oil with <strong>the</strong> following fatty acid composition: 74% <strong>of</strong>oleic acid, 12,3% <strong>of</strong> palmitic acid, 3,5% <strong>of</strong> stearic acid and 7,7% <strong>of</strong> linoleic acid and 2,5% <strong>of</strong>myrisitc acid, <strong>the</strong> selectivity <strong>of</strong> <strong>the</strong> silicates catalyst has been compared with that <strong>of</strong> <strong>the</strong>conventional alkaline homogeneous catalyst KOH. The sodium silicate catalyst shows ahigher selective towards <strong>the</strong> long chain fatty acids (Figure 1). The maximum content <strong>of</strong>methyl palmitate, methyl oleate and methyl linoletae (C18) increases and no myristic acidconversion occurs at <strong>the</strong> end <strong>of</strong> <strong>the</strong> reaction catalyzed by <strong>the</strong> sodium silicate.80Finally, some <strong>of</strong> <strong>the</strong> most important70Sodium SilicateKOHparameters <strong>of</strong> biodiesel quality60(monoglyceride, diglyceride and50403020triglyceride content, total glycerol leveland acid value) for reactions using eachcatalyst have been evaluated. For example,100<strong>the</strong> acid value <strong>of</strong> <strong>the</strong> biodiesel produced byFigure 1. Methyl esters content obtained bytransesterification reaction catalyzed by KOH andsodium silicate.Methyl Methyl Methyl Methyl MethylMiristate Palmitate Sterate Oleate Linoleatepotassium silicate is equal to 0.23 mgKOH/g (0.5 mg KOH/g is <strong>the</strong> maximumvalue defined by <strong>the</strong> European UnionDraft Standard prEN 14214).Methyl Esters C ontent [% wt]References1. F. Ma, M.A. Hanna, Bioresour. Technol., 70 (1999) 1-15.2. B. Freedman, E.H. Pryde, T.L. Mounts, J. Am. Oil Chem. Soc., 61 (1984) 1638-1643.476

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