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II International Symposium on Carbon for Catalysis ABSTRACTS

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OP-I-12<br />

The carb<strong>on</strong> matrix avoids the <strong>for</strong>mati<strong>on</strong> of large Al 2 O 3 or TiO 2 crystallite in the<br />

composite, as shown by XRD. XPS show that both organic and inorganic phases were nearly<br />

independent, no significant interacti<strong>on</strong>s between them were observed. The carb<strong>on</strong> matrix, as<br />

well Al 2 O 3 or TiO 2 oxides present similar XPS patterns than their pure phases. Their acidity,<br />

determined by isopropanol decompositi<strong>on</strong> depended <strong>on</strong> the nature of the metal oxide present<br />

(TiO 2 ≥Al 2 O 3 ) while the organic fracti<strong>on</strong> was not active.<br />

Regarding to the hydrophilic character of the samples, two types of active sites were<br />

determined by water adsorpti<strong>on</strong> at room temperature. The str<strong>on</strong>g primary centres corresp<strong>on</strong>d<br />

to the micropore filling or water adsorpti<strong>on</strong> <strong>on</strong> acidic centres and weak sec<strong>on</strong>dary centres<br />

corresp<strong>on</strong>d to adsorpti<strong>on</strong> <strong>on</strong> hydrophilic (C=O) groups (2). Primary centres were more<br />

abundant and str<strong>on</strong>ger <strong>on</strong> composites than in carb<strong>on</strong> aerogels according with their more acid<br />

character and smaller microporosity.<br />

The activity order in toluene combusti<strong>on</strong> was C1000Pt > TiC1000Pt > AlC1000Pt<br />

(Figure 1). In previous works (1) we found that catalyst activity increase with Pt-particle size,<br />

thus combusti<strong>on</strong> is a structure sensitive reacti<strong>on</strong>. In this sense, Al/C-Pt catalyst must be the<br />

most active of this series. The large c<strong>on</strong>centrati<strong>on</strong> and strength of primary water adsorpti<strong>on</strong><br />

sites <strong>on</strong> composite surface could be related with their smaller combusti<strong>on</strong> activity.<br />

Table 1. Textural characteristics and dispersi<strong>on</strong>.<br />

Figure 1. Catalysts activity<br />

C1000Pt TiC100Pt AlC1000Pt<br />

Sample Oxide SCO 2 V 2 V 3 d H2<br />

% wt m 2 g -1 cm 3 g -1 nm<br />

C-Pt 0 857 0.62 0.00 5.7<br />

AlC-Pt 47 421 0.27 0.80 13.1<br />

TiC-Pt 41 415 0.31 0.40 1.9<br />

CCO2 (%)<br />

100<br />

80<br />

60<br />

40<br />

20<br />

0<br />

150 170 190 210 230<br />

T (ºC)<br />

References<br />

1 F.J. Mald<strong>on</strong>ado-Hódar, C. Moreno-Castilla, A.F. Pérez-Cadenas; Appl. Catal. B. 54, 209<br />

(2004)<br />

2 F. Kraehenbuehl, C. Quellet, B. Schmitter, F. Stoeckly. J. Chem. Soc. Faraday Trans., 82,<br />

3439 (1986)<br />

61

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