Abstract In fluidized bed regeneration of carbon-contaminated catalysts, such as cracking catalysts, wherein at least a portion of the oxygen-containing gas required for fluidization and burn-off of carbon deposits is introduced as a separate stream into the dense phase of the fluidized catalyst, contained in the regeneration chamber, by means of a plurality of gas discharge nozzles, affixed to at least one manifold member substantially horizontally disposed at the lower end of the regeneration chamber, catalyst attrition is reduced and backflow of catalyst particles into the nozzles is minimized by utilizing gas discharges which are restricted in internal cross-sectional area in their upstream portion connected to the manifold member and expanded in the internal cross-sectional area of their downstream portion such that (a) the numerical ratio of the difference between diameter of the downstream portion and the diameter of the upstream portion divided by the length of the downstream portion taken in the direction of gas flow does not exceed 0.18 and (b) the ratio of the diameter of the upstream portion to its length taken in direction of gas flow does not exceed 1.67.
In a process for fluidized bed regeneration of carbon-contaminated catalysts wherein at least a portion of the oxygen-containing gas required for fluidization and burn-off of carbon deposited on the catalyst particles is introduced as a separate stream into the dense phase of the fluidized catalyst bed contained in a regeneration chamber by means of a plurality of gas discharge nozzles connected to an external source of pressurized oxygen-containing gas by one or more horizontally disposed manifold members; the improvement which comprises, introducing the oxygen-containing gas at a nozzle outlet velocity in the range of about 75 to about 125 ft/sec via gas discharge nozzles which are substantially cylindrical in shape having an upstream portion and a downstream portion with a transition portion connecting the upstream and downstream portions and wherein said upstream portion is attached to said manifold member which discharge nozzles are restricted in internal cross-sectional area in their upstream portions and expanded in the internal cross-sectional area of their downstream portions such that (a) the numerical ratio of the difference between the diameter of the downstream portion and the diameter of the upstream portion divided by the length of the downstream portion taken in the direction of gas flow does not exceed 0.18 and (b) the ratio of the internal diameter of the upstream portion to its length taken in direction of gas flow does not exceed 1.67.
Claim 2
Dependent Claim
230 words
In a process for fluidized bed regeneration of carbon-contaminated catalysts wherein at least a portion of the oxygen-containing gas required for fluidization and burn-off of carbon deposited on the catalyst particles is introduced as a separate stream into the dense phase of the fluidized catalyst bed contained in a regeneration chamber by means of a plurality of gas discharge nozzles connected to an external source of pressurized oxygen-containing gas by one or more horizontally disposed manifold members; the improvement which comprises, introducing the oxygen-containing gas at a nozzle outlet velocity in the range of about 75 to about 125 ft/sec via gas discharge nozzles which are substantially cylindrical in shape having an upstream portion and a downstream portion with a transition portion connecting the upstream and downstream portions and wherein said upstream portion is attached to said manifold member which discharge nozzles are restricted in internal cross-sectional area in their upstream portions and expanded in the internal cross-sectional area of their downstream portions such that (a) the numerical ratio of the difference between the diameter of the downstream portion and the diameter of the upstream portion divided by the length of the downstream portion taken in the direction of gas flow does not exceed 0.18 and (b) the ratio of the internal diameter of the upstream portion to its length taken in direction of gas flow does not exceed 1.67.
Claim 3
Dependent Claim
24 words
The process of claim 1, wherein the downstream cross-sectional area of the gas discharge nozzles is 1.3 to 5 times the upstream cross-sectional area.
Claim 4
Dependent Claim
11 words
The process of claim 1, wherein the oxygen-containing gas is air.