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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-<str<strong>on</strong>g>II</str<strong>on</strong>g>-6<br />

AVOIDING MASS TRANSFER LIMITATIONS IN CARBON SUPPORTED<br />

CATALYSIS BY USING CARBON XEROGEL TYPE SUPPORTS<br />

Job N., Heinrichs B., Lé<strong>on</strong>ard A., Colomer J.-F. 1 , Marien J., Pirard J.-P.<br />

Université de Liège, Laboratoire de Génie Chimique (B6a), B-4000 Liège, Belgium<br />

1 Laboratoire de Rés<strong>on</strong>ance Magnétique Nucléaire, Facultés Universitaires Notre-Dame<br />

de la Paix, rue de Bruxelles 61, B-5000 Namur, Belgium<br />

e-mail: Nathalie.Job@ulg.ac.be<br />

Porous carb<strong>on</strong> xerogel with tailored texture can be obtained by evaporative drying and<br />

pyrolysis of resorcinol-<strong>for</strong>maldehyde aqueous gels [1-2]. The pore texture is c<strong>on</strong>trollable by<br />

varying the pH of the precursors soluti<strong>on</strong> in a narrow range: depending <strong>on</strong> the pH, micromacroporous,<br />

micro-mesoporous, microporous or n<strong>on</strong> porous carb<strong>on</strong>s are obtained. Solvent<br />

removal can be per<strong>for</strong>med by the c<strong>on</strong>vective air drying process, which is comm<strong>on</strong>ly used in<br />

industry and very suitable to large-scale applicati<strong>on</strong>s [3-4]. The pore texture is not influenced<br />

by the drying c<strong>on</strong>diti<strong>on</strong>s. Due to their pore texture flexibility and mechanical resistance, these<br />

materials are suitable <strong>for</strong> many applicati<strong>on</strong>s, am<strong>on</strong>g which catalyst supports. Moreover, the<br />

synthesis method is very simple and relatively cheap: industrial producti<strong>on</strong> can be envisaged.<br />

The ability to c<strong>on</strong>trol at will the pore size in carb<strong>on</strong> xerogels is a great advantage<br />

compared to classical active charcoals, whose textural parameters are mainly fixed by the<br />

origin of the raw material. Indeed, the pore texture of active charcoals obtained after thermal<br />

treatment str<strong>on</strong>gly depends <strong>on</strong> the nature of the precursor. Moreover, these supports are<br />

mainly microporous, with low meso- or macropore volume. Even if the metal is well<br />

dispersed in micropores, mass transfer limitati<strong>on</strong>s decrease the per<strong>for</strong>mances of the catalyst.<br />

On the c<strong>on</strong>trary, the presence of large amounts of meso- or macropores should minimize<br />

diffusi<strong>on</strong>al limitati<strong>on</strong>s inside carb<strong>on</strong> supports synthesized by sol-gel process, and these<br />

supports could be designed according to the c<strong>on</strong>sidered reacti<strong>on</strong>.<br />

In this study, mass transfer inside carb<strong>on</strong> xerogels was analysed during a well known<br />

chemical reacti<strong>on</strong>. The aim of this work is to show that it is possible to completely eliminate<br />

diffusi<strong>on</strong>al limitati<strong>on</strong>s inside the catalyst pellets provided that the carb<strong>on</strong> xerogel texture is<br />

adequately adjusted through an appropriate choice of synthesis variables values. Three carb<strong>on</strong><br />

xerogels with various pore size were selected: <strong>on</strong>e micro-mesoporous sample with small<br />

mesopores (maximum pore size = 10 nm), <strong>on</strong>e micro-mesoporous sample with large<br />

mesopores (maximum pore size = 40 nm) and <strong>on</strong>e micro-macroporous sample (maximum<br />

104

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