Mineral oils: processes and products – Chemical conversion of hydrocarbons – Cracking
Patent
1991-11-05
1992-06-30
Morris, Theodore
Mineral oils: processes and products
Chemical conversion of hydrocarbons
Cracking
208121, 208147, 208155, 208156, 208157, 208161, 502 43, 422144, 422145, 422147, C10G 1100
Patent
active
051260360
ABSTRACT:
A process and apparatus for regeneration of coked catalyst used in the fluidized cracking of heavy oils is disclosed. A high efficiency catalyst regenerator, with a fast fluidized bed coke combustor, dilute phase transport riser, and second fluidized bed is used but modified so that at least some coked catalyst is added directly to the second fluidized bed. The coked catalyst can be heated by direct contact heat exchange in the second fluidized bed and then charged to the coke combustor, or the coked catalyst can be regenerated in the second fluidized bed, or some combination of both. Adding catalyst to the second fluidized bed increases the coke burning capacity of these regenerators, and/or permits a drier regeneration.
Diemler William C.
McKillop Alexander J.
Mobil Oil Corporation
Morris Theodore
Speciale Charles J.
LandOfFree
Process and apparatus for split feed of spent catalyst to high e does not yet have a rating. At this time, there are no reviews or comments for this patent.
If you have personal experience with Process and apparatus for split feed of spent catalyst to high e, we encourage you to share that experience with our LandOfFree.com community. Your opinion is very important and Process and apparatus for split feed of spent catalyst to high e will most certainly appreciate the feedback.
Profile ID: LFUS-PAI-O-1861708