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II International Symposium on Carbon for Catalysis ABSTRACTS

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OP-I-4<br />

As it can be seen, potassium permanganate gives place to the greatest increase in both the<br />

c<strong>on</strong>centrati<strong>on</strong>s.<br />

All the supports of Tab. 1 have then been c<strong>on</strong>tacted with a palladium acetate soluti<strong>on</strong><br />

dissolved in benzene (2 g of supports with 50 ml of a benzene soluti<strong>on</strong> of palladium acetate)<br />

<strong>for</strong> 2-3 hours. In the menti<strong>on</strong>ed range of time all the palladium is adsorbed from the soluti<strong>on</strong>.<br />

The prepared catalysts c<strong>on</strong>tained about 1% by weight of palladium with the excepti<strong>on</strong> of the<br />

support prepared by oxidati<strong>on</strong> with 1 M potassium permanganate that have been prepared<br />

with 3% by weight of palladium. An increase of -COOH and -OH would favour palladium<br />

dispersi<strong>on</strong> as a c<strong>on</strong>sequence of the surface reacti<strong>on</strong>:<br />

---- COOH + Pd(OOCCH 3 ) 2 ---- COOPd(OOCCH 3 ) + CH 3 COOH<br />

The dispersi<strong>on</strong> of all the prepared catalysts has been determined by measuring hydrogen<br />

chemisorpti<strong>on</strong> with a pulse method [4] and the obtained results are always summarized in<br />

Tab. 1. As it can be seen, all the catalysts resulted well dispersed and the effect of the<br />

oxidating treatment in some cases is significant even if not very str<strong>on</strong>g. In particular there is<br />

not a direct correlati<strong>on</strong> between the increase of –COOH and –OH c<strong>on</strong>centrati<strong>on</strong>s and<br />

dispersi<strong>on</strong>. This will be discussed and justified.<br />

All the prepared catalysts have been submitted to an activity test c<strong>on</strong>sisting in the<br />

measurement in a batch reactor of the reacti<strong>on</strong> rate of the cyclo-octene hydrogenati<strong>on</strong>. The<br />

obtained results are always reported in Tab. 1. As it can be seen drastic treatments are<br />

detrimental while the oxidati<strong>on</strong> in mild c<strong>on</strong>diti<strong>on</strong> gives place to an improvement of the<br />

per<strong>for</strong>mances.<br />

The properties and catalytic per<strong>for</strong>mances of the prepare Pd-carb<strong>on</strong> catalysts have also been<br />

compared with catalysts c<strong>on</strong>taining roughly the same amount of palladium but prepared by<br />

using other different supports, such as: alumina, silica and silica alumina and other palladium<br />

precursors. A discussi<strong>on</strong> <strong>on</strong> the method more suitable <strong>for</strong> obtaining very high dispersed<br />

catalysts will c<strong>on</strong>clude the work.<br />

References<br />

[1] H.P. Boem; Advances in <strong>Catalysis</strong> 16,19 (1966)<br />

[2] A. King; J. Chem Soc. 20, 1489 (1937)<br />

[3] S. Studebaker; Rubber Chem. Technology 30, 1401(1957)<br />

[4] L. Maffucci, P. Iengo, M. Di Serio, E. Santacesaria<br />

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