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U.S. Department of Energy
Office of Scientific and Technical Information

Fluidized bed combustion process

Patent ·
OSTI ID:5191272
This patent describes an FCC catalyst regeneration process for regenerating coke and nitrogen containing catalyst in an FCC regenerator with a regeneration gas comprising oxygen to form hot regenerated catalyst and flue gas. It comprises adding the spent FCC catalyst to a dense bed regeneration zone, operating at dense bed regeneration zone, operating at dense bed catalyst regeneration conditions including a superficial gas velocity of from 0.05 to 4 ft/s. with a relatively reducing atmosphere to partially regenerate the catalyst; adding at least a majority of the regeneration gas to a dilute phase combustion zone underneath, and in open communication with, the dense bed zone the dilute phase combustion zone operating at dilute phase catalyst regeneration conditions including a superficial gas velocity of from 15 to 50 ft/s. to complete the regeneration of the catalyst and produce flue gas containing NO{sub x}; discharging the produced flue gas up into the reducing atmosphere of the dense bed combustion zone; withdrawing hot regenerated catalyst from a portion of the lower, dilute phase combustion zone and recycling at least a portion of this catalyst to an FCC reactor; and withdrawing flue gas with a reduced NO{sub x} content from the top of the dense bed.
Assignee:
Mobil Oil Corp., Fairfax, VA (United States)
Patent Number(s):
A; US 5106799
Application Number:
PPN: US 7-646911
OSTI ID:
5191272
Country of Publication:
United States
Language:
English