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

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OP-V-4Catalyst deactivation was more severe with very small Pd particles, whereas completeconversion <strong>of</strong> stearic acid was achieved with <strong>the</strong> catalyst exhibiting optimum dispersion.The main products were hepta- and pentadecane, which were formed in a parallel fashionup to 45% conversion, <strong>the</strong>reafter heptadecane reacted fur<strong>the</strong>r to pentadecane and thus <strong>the</strong>reaction proceeded both parallelly and consecutively to <strong>the</strong>se two products. Selectivity <strong>of</strong>heptadecane as a function <strong>of</strong> stearic acid conversion is shown in Fig. 1b. No o<strong>the</strong>r liquidphase products were observed. Analysis <strong>of</strong> <strong>the</strong> gas phase products revealed presence <strong>of</strong>methane, carbon dioxide, carbon monoxide, propene and propane indicating that bothdecarbonylation and decarboxylation took place.a) b)1.00.80.600.55Mol %0.60.40.2Selectivity to C170.500.450.400.350.00 100 200 300 400Time, min0.300.0 0.2 0.4 0.6 0.8 1.0C18 conversionFig. 1. a) Deoxygenation <strong>of</strong> stearic acid and b) selectivity to heptadecane as a function <strong>of</strong> conversion over differentPd/C catalysts at 300°C under 17 bar. Symbols: Pd dispersion 18% (•), 47% (♦), 65% (•) and 72% (▲).4. ConclusionsSeveral supported palladium catalysts with varying metal dispersions were tested instearic acid deoxygenation. Catalyst deactivation was found to be crucial using lower amounts<strong>of</strong> catalyst. There was an optimum metal dispersion exhibiting <strong>the</strong> highest reaction rate. Themain products were hepta- and pentadecane being formed parallelly. At high conversionlevels <strong>of</strong> stearic acid heptadecane reacted consecutively to pentadecane. The reactionmechanism will be discussed in <strong>the</strong> final presentation.AcknowledgmentsThe part <strong>of</strong> research work was supported by RFBR Grant № 07-03-12159.References1. Snåre, M., Kubickova, I., Mäki-Arvela, P., Eränen, K., Murzin, D.Yu., Ind.Engn Chem. Res. 45 (2006),5708.2. Mäki-Arvela, P., Kubickova, I., Eränen, K., Snåre, M., Murzin, D. Yu., Energy and Fuels, 21 (2007), 30.3. Snåre, M., Kubickova, I., Mäki-Arvela, P., Eränen, K., Murzin, D. Yu., Catal Org. React. 115 (2006), 415.4. P.A. Simonov, S.Yu. Troitskii, V.A. Likholobov, Kinet. Catal. (Russ. Ed.) 41 (2000), 281.174

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