Coke burnoff in a typical FCC particle analyzed by an SEM mapped 2-D network pore structure

Citation
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
Citations number
20
Categorie Soggetti
Chemical Engineering
Journal title
CHEMICAL ENGINEERING SCIENCE
ISSN journal
00092509 → ACNP
Volume
56
Issue
3
Year of publication
2001
Pages
865 - 872
Database
ISI
SICI code
0009-2509(200102)56:3<865:CBIATF>2.0.ZU;2-7
Abstract
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.