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II International Symposium on Carbon for Catalysis ABSTRACTS

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OP-I-2<br />

loading. It is also interesting to observe that the particle sizes <strong>on</strong>ly increase very slightly with<br />

the metal loading.<br />

TEM characterizati<strong>on</strong> dem<strong>on</strong>strates that all the cobalt is deposited <strong>on</strong> the fibres, free of<br />

any bulk precipitati<strong>on</strong>. A representative TEM image of the 40 wt.% Co/CNF catalyst is shown<br />

in Fig. 1. The cobalt oxide particles are homogeneously distributed with a very narrow size<br />

distributi<strong>on</strong>, and seem to cover the fibre uni<strong>for</strong>mly at the 40 wt.% loading. The average<br />

particle size calculated from 120 particles is 8.3 nm, in good agreement with the XRD study.<br />

TPR study shows that all the catalysts are reduced through two main steps, from Co 3 O 4 to<br />

CoO, and from CoO to Co. The first peak is relatively narrow and the sec<strong>on</strong>d peak is quite<br />

broad. This also suggests the coexistence of Co 3 O 4 and CoO. Compared with the reducti<strong>on</strong> of<br />

Co/Al 2 O 3 , Co/CNF is reduced at a lower temperature. This is because <strong>for</strong> Co/Al 2 O 3 , cobalt<br />

will <strong>for</strong>m a surface compound with alumina, which is difficult to be reduced. Hence, TPR<br />

study clearly shows the weak interacti<strong>on</strong> of metal and CNF. This will also be an advantage of<br />

using CNF as support <strong>for</strong> F-T catalysts because high reducti<strong>on</strong> temperatures are required <strong>for</strong><br />

cobalt <strong>on</strong> str<strong>on</strong>gly interacti<strong>on</strong> supports, and they lead to the sintering of cobalt particles.<br />

In c<strong>on</strong>clusi<strong>on</strong>, DP has been used to prepare highly loaded, highly dispersed cobalt <strong>on</strong><br />

CNF catalysts. The precipitati<strong>on</strong> has been c<strong>on</strong>trolled by slowly increase the pH of the<br />

soluti<strong>on</strong>. The Co/CNF catalysts have a small particle size and narrow particle size<br />

distributi<strong>on</strong>. Combined with their easy-to-reduce property, these catalysts could be promising<br />

<strong>for</strong> F-T synthesis applicati<strong>on</strong>s.<br />

Table 1. Metal loading and particle sizes from catalyst. Fig. 1. TEM image of the 40 wt.%<br />

XRD and TEM of different catalysts.<br />

Catalyst Actual loading Particle size Particle size<br />

(wt.%) (nm, XRD) (nm, TEM)<br />

12 wt.% 10.1 8.4 6.5<br />

20 wt.% 17.1 9.5 -<br />

40 wt.% 38.6 9.4 8.3<br />

References:<br />

1 G.L. Bezemer, A. van Laak, A.J. van Dillen and K.P. de J<strong>on</strong>g, Stud. Surf. Sci. Catal. 147<br />

(2004) 259.<br />

2 J.H. Bitter, M.K. van der Lee, A.G.T. Slotboom, A.J. van Dillen, and K.P. de J<strong>on</strong>g, Catal.<br />

Lett. 89 (2003) 139.<br />

41

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