Ua. El-nafaty et R. Mann, Coke burnoff in a typical FCC particle analyzed by an SEM mapped 2-D network pore structure, CHEM ENG SC, 56(3), 2001, pp. 865-872
The pore morphology of a selected (congruent to 70 mum) fluid catalytic cra
cking (FCC) catalyst particle, as viewed on a SEM image of sectioned surfac
e of low melting point alloy (LMPA) impregnated FCC catalyst sample, was ma
pped onto an approximately 'equivalent' 2-D 30 x 30 pseudo-random pore netw
ork to investigate the consequences for burnoff characteristics in the part
icle. The mapped 2-D structure was constructed from a set of pores having a
psd close to that given by BJH adsorption results by preferentially assign
ing larger macropores to corresponding apparent locations in the SEM image
while the rest of the meso- and micro-pores were then randomly assigned acr
oss the rest of the network. Major parameters such as pore structural confi
guration, residual coke, and spatial oxygen profile were tracked as a funct
ion of time. The model results were compared to experimental coke burnoff d
ata, carried out in a micro-scale reaction unit. The model prediction fits
fairly well within the experimental fluctuations. The results also showed t
hat over 90% coke is burnt off within the first 50% of reaction time. For c
omparative purposes, the model predictions were also applied to a 'shuffled
' structure, produced by random permutation of the same radii of the mapped
structure as well as an 'optimally sparsed' structure. Burnoff in the shuf
fled structure exhibited the worst performance. This was attributed to the
decrease in the proportion of larger pores on the network skin in contrast
to the mapped and optimally sparsed structures. Since Visual inspections of
SEM images of most particles tend to reveal a randomly oriented pore confi
guration (whereas the mapped structure was for a selected particle), the pr
edicted aggregate performance of the FCC catalyst sample studied would be e
xpected to lie somewhere in between the curves of the shuffled and mapped s
tructures. The support pore architectural design of those particles could,
therefore, still be improved for better performance in terms of accessibili
ty, reactivity and selectivity. (C) 2001 Elsevier Science Ltd. All rights r
eserved.