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Title: Apparatus and method for regenerating coked fluid cracking catalyst

Patent ·
OSTI ID:5393530

This patent describes a continuous counterflow two-stage method for regenrating hot coked FCC catalyst discharged from a FCC reactor, each of which stages produces a distinct flue gas. The FCC catalyst comprising an acidic cracking component and a SO/sub chi/-transfer agent. The method comprises as concurrent steps: passing the hot coked catalyst and first-stage fluidizing gas containing all of the second-stage flue gas having more than 2 volume percent residual free oxygen and an ecologically excessive concentration of NO/sub chi/ to a first-stage riser unit under conditions effective to burn off 10 to 50 percent of the coke whereby forming partially regenerated catalyst and a first-stage flue gas depleted of NO/sub chi/ and containing less than 2 volume percent of residual free oxygen; passing the partially regenerated catalyst and second-stage fluidizing gas consisting of fresh regeneration gas to a second stage riser unit under conditions effective to produce regenerated catalyst containing entrained SO/sub chi/ and a second-stage flue gas containing more than 2 volume percent of residual free oxygen and an ecologically excessive concentration of NO/sub chi/; discharging the first-stage flue gas depleted of NO/sub chi/ from the first-stage riser unit; and passing the regenerated catalyst containing entrained SO/sub chi/ back to the FCC reactor.

Assignee:
Mobil Oil Corp., New York, NY
Patent Number(s):
US 4851374
Application Number:
PPN: US 7056082A
OSTI ID:
5393530
Resource Relation:
Patent File Date: 29 May 1987
Country of Publication:
United States
Language:
English