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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-9<br />

FABRICS OF ACTIVE CARBON FIBERS WITH Pd-NANOPARTICLES OF<br />

CONTROLLED DISPERSION FOR SELECTIVE 1-HEXYNE HYDROGENATION<br />

Semagina N., Renken A., Kiwi-Minsker L.<br />

LGRC-ISIC, Ecole polytechnique fédérale de Lausanne (EPFL), Switzerland<br />

e-mail: natalia.semagina@epfl.ch<br />

Catalytic hydrogenati<strong>on</strong> is <strong>on</strong>e of the key processes <strong>for</strong> manufacturing pharmaceuticals,<br />

vitamins and fine chemicals. The per<strong>for</strong>mance of the hydrogenati<strong>on</strong> process and product<br />

distributi<strong>on</strong> is str<strong>on</strong>gly influenced by the catalyst activity and selectivity, the interacti<strong>on</strong> of<br />

chemical kinetics and mass transfer, as well as the reactor design. Process intensificati<strong>on</strong> and<br />

integrated envir<strong>on</strong>mental protecti<strong>on</strong> can be improved by multiple catalyst reuses. To avoid<br />

internal and external mass transfer limitati<strong>on</strong>s and to attain high product selectivity catalyst<br />

particles of small diameter are required. In technical applicati<strong>on</strong>s the minimal size, however,<br />

is limited due to the catalyst filtrati<strong>on</strong> after the reacti<strong>on</strong>.<br />

One novel approach to overcome these problems is the use of filamentous catalytic<br />

materials like woven cloths <strong>for</strong> the depositi<strong>on</strong> of active comp<strong>on</strong>ents. The diameters of the<br />

filaments are in the order of several micrometers and corresp<strong>on</strong>d to the diameter of the<br />

traditi<strong>on</strong>al suspensi<strong>on</strong> catalysts. There<strong>for</strong>e, the influence of internal mass transfer <strong>on</strong> overall<br />

kinetics could be suppressed.<br />

Another problem of the catalyst design is related to the size c<strong>on</strong>trol of the active metal<br />

nanoparticles and the size distributi<strong>on</strong>. Traditi<strong>on</strong>al preparati<strong>on</strong> by impregnati<strong>on</strong>/i<strong>on</strong>-exchange<br />

gives broad distributi<strong>on</strong> affecting activity/selectivity in the structure-sensitive reacti<strong>on</strong>s. The<br />

aim of this work was the development of Pd catalyst with m<strong>on</strong>odispersed metal nanoparticles<br />

(~8 nm) deposited <strong>on</strong> active carb<strong>on</strong> fiber (ACF) fabrics efficient in selective liquid-phase<br />

alkyne hydrogenati<strong>on</strong>.<br />

Experimental<br />

The catalyst preparati<strong>on</strong> c<strong>on</strong>sists of a <strong>for</strong>mati<strong>on</strong> of Pd-nanoparticles of the c<strong>on</strong>trolled size<br />

in a reverse microemulsi<strong>on</strong>, evaporati<strong>on</strong> of liquid phases, surfactant removal by dissoluti<strong>on</strong> in<br />

methanol, ultrasound-assisted redispersi<strong>on</strong> of flocculated nanoparticles in water and ACF<br />

impregnati<strong>on</strong>. This method allows obtaining catalysts with high metal loading, retaining the<br />

nanoparticles m<strong>on</strong>odispersity by avoiding calcinati<strong>on</strong> steps and recovering liquid phases of<br />

microemulsi<strong>on</strong> and a part of a surfactant.<br />

54

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