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Fluidized catalytic cracking process utilizing a C3-C4 paraffin-rich co-feed and mixed catalyst system with selective reactivation of the medium pore silicate zeolite component thereof

Patent ·
OSTI ID:7025739
This patent describes a catalytic cracking process featuring at least one riser reactor, at least one stripping unit and at least one regenerator. It comprises: catalytically cracking a C/sub 3/-C/sub 4/ paraffin-rich feed in the lower section of the riser wherein the catalyst in the lower section of the riser consists of a second component of a mixed catalyst system; cracking a heavy hydrocarbon feed in an upper section of the riser in the presence of both the first and second component of the mixed catalyst system; separating particles of spent first catalyst component from particles of second catalyst component in the stripping unit; stripping the separated particles of first catalyst component; conveying stripped, spent first catalyst component to the regenerator, the catalyst undergoing regeneration therein; conveying regenerated first catalyst component to the upper section of the riser; conveying stripped or non-stripped separated particles of second catalyst component to a reactivation zone, the catalyst undergoing reactivation therein; and conveying reactivated second catalyst component to the lower section of the riser.
Assignee:
Mobil Oil Corp., New York, NY
Patent Number(s):
US 4863585
Application Number:
PPN: US 7148199A
OSTI ID:
7025739
Country of Publication:
United States
Language:
English