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Catalysis of Organic..

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114Oxidation <strong>of</strong> n-Pentanethe presence <strong>of</strong> P-OH groups arising from the transformation <strong>of</strong> pyrophosphate intoorthophosphate groups.Catalytic tests were carried out following a protocol that allowed establishrelationships between the characteristics <strong>of</strong> fresh and spent catalysts and the catalyticperformance. Specifically, within the first 5-10 hours reaction time, the catalyticperformance was not stable, due to variations in samples characteristics. Therefore,two different sets <strong>of</strong> results were taken, the first after less than 1 hour (representative<strong>of</strong> fresh samples), and the second one after 3-4 hours (representative <strong>of</strong> spentsamples). Only in the case <strong>of</strong> the equilibrated sample, no difference was foundbetween the characteristics <strong>of</strong> samples eq and eqsp (Tables 1 and 2); for this catalyst,also the catalytic performance did not vary at all during catalytic tests.Figure 4 shows the catalytic performance <strong>of</strong> sample ox1sp; the conversion <strong>of</strong> n-pentane, and the selectivity to the main products, MA, PA and carbon oxides, arereported as functions <strong>of</strong> the reaction temperature. The selectivity to MA increased onincreasing the reaction temperature, and correspondingly the selectivity to PAdecreased. The overall selectivity to PA and MA was approximately constant up to400°C, but then decreased, due to the preferred formation <strong>of</strong> carbon oxides.100n-pentane conversion80conversion, selectivity %604020PA selectMA select.COx select0330 360 390 420reaction temperature, °CFigure 4. Effect <strong>of</strong> temperature on catalytic performance. Catalyst ox1sp.Figure 5 summarizes the results obtained for fresh and spent samples; theselectivity to MA and that to PA at approximately 43-50% n-pentane conversion areplotted as a function <strong>of</strong> the average oxidation state <strong>of</strong> V. The most oxidized thecatalyst was, the most preferred was the formation <strong>of</strong> MA with respect to that <strong>of</strong> PA,with a MA/PA selectivity ratio equal to 7 at 50% n-pentane conversion for sampleox3. The opposite was true for most reduced samples, with a MA/PA selectivity ratio

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