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II International Symposium on Carbon for Catalysis ABSTRACTS

II International Symposium on Carbon for Catalysis ABSTRACTS

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Results and discussi<strong>on</strong><br />

OP-I-6<br />

The Table summarizes the effect of the activati<strong>on</strong> treatment of the carb<strong>on</strong> <strong>on</strong> the catalytic<br />

properties of Pt catalysts prepared by both methods<br />

Both catalysts prepared by impregnati<strong>on</strong> with the same dispersi<strong>on</strong> behave similarly in<br />

dioxane, with comparable initial reacti<strong>on</strong> rate, total c<strong>on</strong>versi<strong>on</strong> within 6-7 h and a very good<br />

selectivity to Bzal. In dioxane/alkaline aqueous soluti<strong>on</strong>, c<strong>on</strong>versi<strong>on</strong> of Bzol to Bzal was very<br />

rapid, but while Bzal was totally c<strong>on</strong>verted to the acid in the presence of 2%Pt imp /C35C, <strong>on</strong>ly<br />

46% of Bzoic were produced over 3%Pt imp /C44A. These results are attributed to the polar<br />

groups <strong>on</strong> C44A which make the catalyst hydrophilic and retains a water film <strong>on</strong> the metallic<br />

surface.<br />

The catalysts prepared by cati<strong>on</strong>ic exchange were surprisingly very poorly dispersed<br />

(5 and 20%). Dispersi<strong>on</strong> of Pt in 3%Pt ex /C35C ox and c<strong>on</strong>sequently the catalytic activity in<br />

dioxane/alkaline aqueous soluti<strong>on</strong> could be improved, by heating C39C ox under Ar at 500°C<br />

(noted C ox cal) to selectively eliminate carboxylic groups and preserve phenolic groups. Further<br />

improvement could be obtained by decompositi<strong>on</strong> of the catalyst precursor under air, be<strong>for</strong>e<br />

the reducti<strong>on</strong> step (noted C ox cal and C ox/Ar cal ). However the per<strong>for</strong>mances were lower than<br />

those of 2%Pt imp /C35C.<br />

Table: Oxidati<strong>on</strong> of Bzol (100 mmol l -1 , 100 ml solvent, 1 g catalyst, 100°C, 10 bar air).<br />

Dispersi<strong>on</strong> In dioxane In dioxane/alkaline water<br />

(%) Initial rate Bzol c<strong>on</strong>v Bzal yield Bzol c<strong>on</strong>v Bzoic yield<br />

mol h -1 -1<br />

mol Pt (%)/h (%)/h (%)/h (%)/h<br />

2%Pt imp /C44A 44 51 100/6 95/6 100/2 46/23<br />

2%Pt imp /C35C 35 63 99/7 98/7 99/2 98/23<br />

2.7%Pt ex /C39A 20 7 94/23 86/23 100/4 39/23<br />

3%Pt ex /C39C ox 5 7 91/23 85/23 100/4 20/23<br />

3%Pt ex /C39C ox/Ar 15 100/3 66/23<br />

3%Pt ex /C39C ox calc 19 100/3 95/23<br />

3%Pt ex /C39C ox/Ar cac 24 100/2 95/23<br />

In c<strong>on</strong>clusi<strong>on</strong>, the activati<strong>on</strong> treatment of this synthetic carb<strong>on</strong> and the mose of depositi<strong>on</strong><br />

of Pt are of prime importance <strong>for</strong> activity of the resulting supported platinum catalyst in<br />

selective oxidati<strong>on</strong> of benzylalcohol.<br />

References<br />

[1] R.A. Sheld<strong>on</strong>, I. W. C. E. Arends, A. Dijksman, Catal. Today 2000, 57, 157.<br />

[2] P. Korovchenko, C. D<strong>on</strong>ze, P. Gallezot, M. Bess<strong>on</strong>, Appl. Catal. B, revised manuscript.<br />

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