Fluidized catalytic cracking process with long residence time steam stripper

Claim 2

In a process for catalytic cracking of a sulfur containing hydrocarbon charge by contacting said charge at cracking temperature with a circulating inventory of cracking catalyst to produce cracked vapor product and spent catalyst with deposits of coke and sulfur compounds, wherein at least a portion of said spent catalyst is regenerated with an oxygen-containing gas at regeneration conditions including a regeneration temperature higher than said cracking temperature and sufficient to burn at least a portion of said coke and said sulfur deposits to generate oxides of carbon and sulfur oxides and regenerated catalyst with reduced coke content which is recycled to contact said hydrocarbon charge, the improvement comprising subjecting said spent catalyst to stripping at a temperature of 500° to 700° C with steam for about 1 to 10 minutes, said improved process being further characterized by the absence of oxygen during said stripping and the absence of any SO x removal additives on said catalyst.

Claim 3

Improved process of claim 1 wherein said steam stripping is for 1 to 5 minutes at 500° to 550° C.

Claim 4

Process of claim 1 wherein said stripping temperature is below said cracking temperature and said regeneration temperature.

Claim 5

Process of claim 1 wherein the weight ratio of steam to spent catalyst is from 1:100 to 1:10.

Claim 6

A process for the fluidized catalytic cracking of sulfur containing hydrocarbon feed comprising (a) passing to an FCC riser reactor said feed in contact with a zeolite catalyst on a support to produce a cracked product and spent catalyst contaminated with coke and sulphur compounds; (b) separating spent catalyst from reactor effluent vapors containing cracked product; (c) subjecting said spent catalyst to long residence time stripping at a temperature of 500 to 700 C., for 1 to 10 minutes, in the presence of a gas comprising steam to produce stripper vapors containing at least 10 percent of said sulfur compound contamination deposited on said catalyst during said riser cracking reaction and stripped catalyst; (d) charging said stripped catalyst to a CO afterburning regenerator wherein said spent, stripped catalyst is contacted with an oxygen containing gas at FCC regeneration conditions sufficient to convert most of said coke deposited on said catalyst to carbon dioxide to produce a regenerated catalyst; (e) returning said regenerated catalyst to said FCC riser reactor for reuse therein.

Claim 7

A process for the fluidized catalytic cracking of sulfur containing hydrocarbon feed comprising (a) passing to an FCC riser reactor said feed in contact with a zeolite catalyst on a support to produce a cracked product and spent catalyst contaminated with coke and sulphur compounds; (b) separating spent catalyst from reactor effluent vapors containing cracked product; (c) subjecting said spent catalyst to long residence time stripping at a temperature of 500 to 700 C., for 1 to 10 minutes, in the presence of a gas comprising steam to produce stripper vapors containing at least 10 percent of said sulfur compound contamination deposited on said catalyst during said riser cracking reaction and stripped catalyst; (d) charging said stripped catalyst to a CO afterburning regenerator wherein said spent, stripped catalyst is contacted with an oxygen containing gas at FCC regeneration conditions sufficient to convert most of said coke deposited on said catalyst to carbon dioxide to produce a regenerated catalyst; (e) returning said regenerated catalyst to said FCC riser reactor for reuse therein.

Claim 8

Process of claim 5 wherein long residence time stripping conditions include a temperature of 500° to 550° C., a residence time of 1 to 5 minutes, and a steam to catalyst weight ratio of 1:100 to 1:10.

Claim 9

Process of claim 5 wherein said stripping zone is a vessel separate from said FCC riser reactor and said regenerator.

Claim 10

Process of claim 5 wherein said stripping vessel is located at an elevation intermediate said FCC riser reactor and said regenerator, whereby there is a gravity flow of catalyst from said FCC riser reactor to said stripper to said regenerator.

Claim 11

Process of claim 5 wherein said stripping vessel has an upper solid-vapor disengaging space containing cyclones for separation of catalyst from stripping vapors, and wherein at least a portion of reactor effluent vapors and said stripping vapors are comingled in said stripper disengaging space, prior to entering cyclones located within said stripper.