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Influence of framework aluminium gradients on the catalytic activity of Y zeolites: cracking of gas-oil on Y zeolites dealuminated by different procedures

Journal Article · · J. Catal.; (United States)
OSTI ID:5269674
The catalytic cracking of gas-oil has been studied in a series of REHY and HY zeolite catalysts dealuminated by deep bed calcination, steaming, and SiCl/sub 4/ treatment. The samples have been characterized by X-ray diffraction, pyridine adsorption, and X-ray photoelectron spectroscopy (XPS). It has been found that the framework Si/Al ratio determined by XPS (surface Si/Al) and that determined from unit cell dimension measurements (bulk Si/Al) differ, indicating a gradient in the concentration of the framework aluminum normal to the surface of the zeolite crystallites. When the gas-oil cracking activity is plotted versus unit cell dimension, three different volcano curves are obtained, with activity maxima located at about 24.59, 24.35, and 24.33 A for deep bed, steamed, and SiCl/sub 4/-treated zeolites, respectively. These results, together with the behavior of the selectivity curves to gasoline, light cycle oil (LCO), gases, coke, and butene/butane ratio, are discussed on the basis of Si/Al gradients. Comparison of the cracking behavior of a short molecule such as n-heptane with that of gas-oil, in relation to the acidity of the samples measured by pyridine adsorption, supports the idea that gas-oil does not penetrate the zeolite deeply and, therefore, that the activity of the catalyst is controlled by the framework Si/Al ratio close to the external surface, instead of the bulk Si/Al ratio of the zeolite crystallites.
Research Organization:
CSIC, Madrid (Spain)
OSTI ID:
5269674
Journal Information:
J. Catal.; (United States), Journal Name: J. Catal.; (United States) Vol. 108:1; ISSN JCTLA
Country of Publication:
United States
Language:
English