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Single riser fluidized catalytic cracking process utilizing a C/sub 3-4/ paraffin-rich CO-feed and mixed catalyst system

Patent ·
OSTI ID:5928951
A catalytic cracking process is described, employing a single riser reaction zone having a lower and an upper section, a stripping zone in which entrained hydrocarbon material is removed from catalyst and a regeneration zone in which spent cracking catalyst is regenerated, the process comprising: (a) thermally cracking a C/sub 3/-C/sub 4/ paraffin-rich feed in the lower section of the riser reaction zone to provide light olefins for conversion to products including aromatics, in the upper section of the riser; and (b) catalytically cracking a heavy hydrocarbon feed selected from the group consisting of gas oil and resid in the upper section of the riser reaction zone in the presence of a mixed catalyst composition comprising a first catalyst component and a second catalyst component wherein the first catalyst component is at least one selected from the group consisting of an amorphous cracking catalyst and a large pore crystalline zeolite cracking catalyst and, wherein the second catalyst component is at least one selected from the group consisting of zeolite Beta and a shape selective medium pore crystalline silicate zeolite, to provide gasoline boiling range components, there being at least one physical characteristic of particles of the second catalyst component which permits particles of second catalyst component to remain in the upper section of the riser reaction zone for a longer average period of time than particles of first catalyst component the physical characteristic selected from the group consisting of size, density and shape.
Assignee:
Mobil Oil Corp., New York, NY
Patent Number(s):
US 4826586
OSTI ID:
5928951
Country of Publication:
United States
Language:
English