Abstract: An FCC catalyst which not only deactivates catalyst poison metals, such as nickel, vanadium and the like, in feedstock oils, inhibits the generation of hydrogen or coke, has excellent cracking activity and bottom oil-treating ability, and can yield a gasoline and LCO fraction in high yields, but also retains the performances on a high level over long and has an improved catalyst life; and an FCC method using the catalyst. The FCC catalyst has a compound of a bivalent metal or of bivalent and trivalent metals showing an XRD pattern of a carbonate of the bivalent metal; an inorganic oxide matrix and the compound dispersed therein; or an inorganic oxide matrix and the compound dispersed therein together with a crystalline aluminosilicate zeolite, and relates to an FCC method in which at least one of the catalysts are used in combination with an FCC catalyst obtained by evenly dispersing a crystalline aluminosilicate zeolite in an inorganic oxide matrix.

Abstract: A catalyst for fluidized catalytic cracking of heavy hydrocarbon oils, which comprises a fluoride salt of a divalent or trivalent metal, wherein the fluoride salt of a divalent or trivalent metal is a compound showing an XRD pattern of a fluoride salt of a divalent or trivalent metal.

Abstract: A catalyst for fluidized catalytic cracking of a heavy hydrocarbon oil, which comprises (A) catalyst particles comprising a compound of a bivalent metal or a compound of bivalent and trivalent metals, wherein said compound shows an XRD pattern of a carbonate of the bivalent metal, and (B) catalyst particles comprising a crystalline aluminosilicate zeolite and a mixture compound of aluminum and at least one metal selected from the group consisting of the Group IVa metals of the Periodic Table.

Abstract: The present invention provides an FCC catalyst which not only deactivates catalyst poison metals, such as nickel, vanadium and the like, in feedstock oils, inhibits the generation of hydrogen or coke, has excellent cracking activity and bottom oil-treating ability, and can yield a gasoline and LCO fraction in high yields, but also retains the performances on a high level over long and has an improved catalyst life; and an FCC method using the catalyst.

Abstract: A crystalline aluminosilicate which has the following characteristics:(A) the SiO.sub.2 /Al.sub.2 O.sub.3 molar ratio as determined by chemical analysis is from 5 to 15;(B) the molar ratio of the Al content in the zeolite framework to the total Al of the aluminosilicate is from 0.3 to 0.6;(C) the unit cell dimension is 24.30 .ANG. or larger but less than 24.45 .ANG.;(D) the alkali metal content in terms of oxide is 0.02% by weight or more but less than 1% by weight in total;(E) the pore distribution yields characteristic peaks at around 50 .ANG. and at around 180 .ANG., with the volume of pores 100 .ANG. or larger but smaller than 600 .ANG. accounting for 10 to 40% of the whole pore volume; and(F) the X ray diffraction pattern thereof yields characteristic peaks of zeolite Y; and a metal modified crystalline aluminosilicate characterized by an X-ray diffraction pattern characteristic of zeolite Y, which is an ion exchanged form or a metal impregnated form containing from 0.