Page 207 - Principles of Catalyst Development
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196 CHAPTER 8
CRYSTALLITE MIGRATION INTERPARTICLE TRANSFER
VAPOR
SURFACE
DIFFUSION
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( b)
(d)
Figure 8.7. Mechanisms for the sintering of dispersed metals.
results which leads to a statistical number of movements. A type of surface
Brownian motion, this mobility produces collisions and consequential
coalescence. Migration rates may control the kinetics, but these depend on
a number of parameters including temperature, crystallite size, surface
wetting, and support substrate. For platinum-alumina catalysts, the limiting
crystallite diameters appears to be about 5 nm. Figure 8.8 shows crystallite
size distributions during sintering of 40 wt % Ni/Si0 2 • Progression of smal-
ler crystallites to larger sizes is clearly seen. (266)
The second mechanism is interparticle transport of atoms from small
to large crystallites. The driving force is the larger free energy of smaller
crystallites, which increases the vapor pressure and evaporation, with con-
densation occurring on larger crystallites. Distribution changes for this
process are shown in Fig. 8.9, where small crystallites disappear as larger
ones grow. (267)
Transport may occur over the surface or through the atmosphere, with
the latter most likely to involve molecular intermediates. This is true with
platinum-alumina, for example, where oxidizing atmospheres during regen-
eration produce volatile Pt0 2 molecules. In nickel-silica catalysts exposed
to carbon monoxide, nickel carbonyl serves the same purpose. For surface
transport, atomic migration is favored, but depends on the substrate compo-
sition.