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U.S. Department of Energy
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Highly attrition resistant mesoporous catalytic cracking catalysts

Patent ·
OSTI ID:6418946
A catalytic cracking catalyst is described for converting a hydrocarbon feedstock at elevated temperature in the substantial absence of hydrogen, into lower average molecular weight, lower boiling hydrocarbon transportation fuel which comprises a crystalline aluminosilicate zeolite having a silica:alumina mole ratio greater than 2:1, and uniform pore diameters ranging from about 4 Angstroms to about 15 Angstroms in diameter, in concentration ranging from about 30% to about 60%, based on the total weight of the catalyst, a matrix comprised of silica and clay within which the crystalline aluminosilicate zeolite is dispersed, said matrix being characterized as porous and the pores as having a bimodal pore size distribution, as measured by mercury porosimetry, a first mode wherein from about 80% to about 90% of the pore volume measured between 45 Angstroms and 2,000 Angstroms is in pores ranging from about 160 Angstroms in diameter to about 400 Angstroms in diameter, and a second mode wherein from about 5% to about 10% of the pores are of diameter ranging above about 100 Angstroms to about 160 Angstroms, and the attrition-resistance of the catalyst, as measured by the Davison Index ranges from about 1 to about 8, wherein the silica matrix portion of said catalyst is prepared from a silica sol made via an ion-exchanged process, and an acidic silica sol prepared by the reaction of sodium silicate, an acid and an aluminum salt, and an aluminum salt of a mineral acid, and wherein the sol is not converted to a gel during catalyst preparation.
Assignee:
Exxon Research and Engineering Co., Florham Park, NJ (United States)
Patent Number(s):
A; US 5221648
Application Number:
PPN: US 7-816021
OSTI ID:
6418946
Country of Publication:
United States
Language:
English