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II International Symposium on Carbon for Catalysis ABSTRACTS

II International Symposium on Carbon for Catalysis ABSTRACTS

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OP-I-6<br />

CARBON SUPPORTED PLATINUM CATALYSTS: INFLUENCE OF ACTIVATION<br />

TREATMENT OF A SYNTHETIC CARBON SUPPORT AND OF METAL<br />

DEPOSITION IN THE SELECTIVE LIQUID PHASE OXIDATION OF ALCOHOLS<br />

Korovchenko P., D<strong>on</strong>ze C., Gallezot P., Bess<strong>on</strong> M.<br />

Institut de Recherches sur la Catalyse-CNRS 2 Avenue Albert Einstein 69626 Villeurbanne<br />

Cedex France<br />

e-mail: michele.bess<strong>on</strong>@catalyse.cnrs.fr<br />

Oxidati<strong>on</strong>s of alcohols into carb<strong>on</strong>yl functi<strong>on</strong>alities are key reacti<strong>on</strong>s in the synthesis of<br />

fine chemicals. The need to substitute stoichiometric oxidati<strong>on</strong>s (using mineral oxidants) with<br />

“green” oxidati<strong>on</strong>s using benign oxidizing agents like molecular oxygen or hydrogen<br />

peroxide has been often emphasized [1]. Supported noble metal catalysts, e.g. Pd/C or Pt/C<br />

are known to catalyse the oxidati<strong>on</strong> of alcohols in the presence of molecular oxygen.<br />

It was previously reported that benzylalcohol (Bzol) can be very selectively oxidized to<br />

benzylalcohol (Bzal) in dioxane, while the use of a 50/50 mixture of dioxane and alkaline<br />

aqueous soluti<strong>on</strong> yielded benzoic acid (Bzoic) by further oxidati<strong>on</strong> of Bzal [2]. In this work,<br />

we examined the effect of the activati<strong>on</strong> treatment of the synthetic carb<strong>on</strong> and of the method<br />

of depositi<strong>on</strong> of the metal <strong>on</strong> the characteristics of the supported metallic catalyst and its<br />

activity in thi reacti<strong>on</strong>.<br />

Experimental<br />

Synthetic carb<strong>on</strong> samples were activated carb<strong>on</strong>s with c<strong>on</strong>trolled pore size. They were<br />

prepared by carb<strong>on</strong>isati<strong>on</strong> at 800°C of a porous polymeric resin precursor prepared from<br />

Novolac resin and hexamethylenetetramine in polyethyleneglycol. The carb<strong>on</strong> particles thus<br />

produced were spherical particles (50-90 µm). Then, they were activated by a “burn off”<br />

technique using either CO 2 at 850°C (carb<strong>on</strong> noted xC) or air at 450°C (carb<strong>on</strong> noted xA),<br />

with x = burn-off percentage (MAST). In some cases, the carb<strong>on</strong>s activated under CO 2 were<br />

oxidized with NaOCl be<strong>for</strong>e the cati<strong>on</strong>ic exchange (carb<strong>on</strong> note xC ox ).<br />

Platinum depositi<strong>on</strong> (nominal 3 wt. %) was per<strong>for</strong>med by liquid phase impregnati<strong>on</strong><br />

using H 2 PtCl 6 and in situ <strong>for</strong>maldehyde reducti<strong>on</strong> in basic medium (noted imp) or by cati<strong>on</strong>ic<br />

exchange with Pt(NH 3 ) 4 Cl 2 (noted ex) and reducti<strong>on</strong> under hydrogen at 300°C.<br />

Carb<strong>on</strong>s were characterized by standard BET method, Boehm titrati<strong>on</strong>, TPD-MS.<br />

Catalysts were characterized by Transmissi<strong>on</strong> Electr<strong>on</strong> Microscopy (TEM) and by CO<br />

chemisorpti<strong>on</strong> at 35°C. The catalytic activity of prepared catalysts was estimated using<br />

oxidati<strong>on</strong> of benzylalcohol to benzaldehyde or benzoic acid with air in a 250 ml batch reactor.<br />

48

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