Process for reducing sox emissions from catalytic cracking units

Claim 2

In a cyclical catalytic cracking process wherein a sulfur-containing hydrocarbon feedstock is fed to a catalytic cracking reaction zone and therein contacted with cracking catalyst particles at an elevated temperature, whereby said hydrocarbon feedstock is converted to product hydrocarbons while said catalyst particles become deactivated with sulfur-containing coke deposits, and said catalyst particles are reactivated in a regeneration zone by burning said coke off said cracking catalyst particles, thereby concomitantly producing an SO x -containing flue gas, and said cracking catalyst particles are then recycled to said catalytic cracking reaction zone, the improvement comprising reducing the amount of SO x compounds carried with said flue gas by introducing into the catalytic cracking cycle one or more organic, aluminum-containing compounds in a manner such that dissolved aluminum-containing components enter the catalytic cracking reaction zone.

Claim 3

A process as defined in claim 1 wherein said organic, aluminum-containing compounds are selected from the group consisting of aluminum isopropoxide, aluminum s-butoxide, aluminum acetylacetonate, and combinations thereof.

Claim 4

In a cyclical catalytic cracking process wherein a sulfur-containing hydrocarbon feedstock is fed to a catalytic cracking reaction zone and therein contacted with cracking catalyst particles at an elevated temperature, whereby said hydrocarbon feedstock is converted to product hydrocarbons while said catalyst particles become deactivated with sulfur-containing coke deposits, and said catalyst particles are reactivated in a regeneration zone by burning said coke off said cracking catalyst particles, thereby concomitantly producing an SO x -containing flue gas, and said cracking catalyst particles are then recycled to said catalytic cracking reaction zone, the improvement comprising reducing the amount of SO x compounds carried with said flue gas by maintaining a relatively uniform dispersion of aluminum components upon the surfaces of the recycled catalyst particles by introducing in said cyclical catalytic cracking process in dissolved form one or more organic, aluminum-containing compounds.

Claim 5

In a cyclical catalytic cracking process wherein a sulfur-containing hydrocarbon feedstock is fed to a catalytic cracking reaction zone and therein contacted with cracking catalyst particles at an elevated temperature, whereby said hydrocarbon feedstock is converted to product hydrocarbons while said catalyst particles become deactivated with sulfur-containing coke deposits, and said catalyst particles are reactivated in a regeneration zone by burning said coke off said cracking catalyst particles, thereby concomitantly producing an SO x -containing flue gas, and said cracking catalyst particles are then recycled to said catalytic cracking reaction zone, the improvement comprising reducing the amount of SO x compounds carried with said flue gas by maintaining a relatively uniform dispersion of aluminum components upon the surfaces of the recycled catalyst particles by introducing in said cyclical catalytic cracking process in dissolved form one or more organic, aluminum-containing compounds.

Claim 6

A process as defined in claim 3 wherein the feed rate at which the organic, aluminum-containing compounds are introduced into the catalytic cracking cycle is such that no less than 5 lbs of SO x compounds (calculated as SO 2 ) are removed in the regeneration zone for each pound of said aluminum-containing compounds (calculated as Al 2 O 3 ) so introduced.

Claim 7

A process as defined in claim 3 wherein said aluminum containing compound is selected from the group consisting of aluminum isopropylate, aluminum s-butoxide, aluminum acetylacetonate, and combinations thereof.

Claim 8

In a fluidized catalytic cracking process comprising the cyclical steps of (1) contacting a sulfur-containing hydrocarbon feedstock stream with a bed of fluidized cracking catalyst particles in a catalytic cracking zone under conditions sufficient to produce a first product hydrocarbon stream having an average molecular weight and boiling point lower than that of the hydrocarbon feedstock stream and to further produce a stream of catalyst particles deactivated by the deposition of sulfur-containing coke upon the surfaces thereof; (2) steam stripping said catalyst particles to remove some of the sulfur-containing coke therefrom and produce a second product hydrocarbon stream; (3) removing the remainder of the sulfur-containing coke from said catalyst particles by combusting said coke in a regeneration zone in the presence of elemental oxygen, thereby reactivating said catalyst particles for the cracking reactions of step (1) and producing a SO x -containing flue gas stream; and (4) recycling the regenerated catalyst particles to step (1), said process further comprising introducing fresh catalyst particles into, and withdrawing catalyst particles from, the stream of catalyst particles recycling through steps (1) to (4) at a rate sufficient to maintain the activity and selectivity of the recycling catalyst particles for converting said hydrocarbon feedstock into said first product hydrocarbon stream in said catalytic cracking reaction zone, the improvement comprising continuously dissolving in said sulfur-containing hydrocarbon feedstock one or more organic, aluminum-containing compounds such that, when the hydrocarbon feedstock is catalytically cracked in step (1), the aluminum-containing compound or compounds are converted to compounds of aluminum dispersed relatively uniformly upon the surfaces of the catalyst particles, said dissolving of said aluminum-containing compounds being at a rate such that, under steady state conditions, the proportion of dispersed aluminum compounds (calculated as Al 2 O 3 ) maintained on the catalyst particles being recirculated through steps (1) to (4) is between about 0.1 and 10.0 catalyst weight percent while the amount of SO x compounds removed in the regenerator is no less than 5 lbs. (calculated as SO 2 ) for each pound of said aluminum-containing compounds (calculated as Al 2 O 3 ) dissolved in said feedstock.

Claim 9

In a fluidized catalytic cracking process comprising the cyclical steps of (1) contacting a sulfur-containing hydrocarbon feedstock stream with a bed of fluidized cracking catalyst particles in a catalytic cracking zone under conditions sufficient to produce a first product hydrocarbon stream having an average molecular weight and boiling point lower than that of the hydrocarbon feedstock stream and to further produce a stream of catalyst particles deactivated by the deposition of sulfur-containing coke upon the surfaces thereof; (2) steam stripping said catalyst particles to remove some of the sulfur-containing coke therefrom and produce a second product hydrocarbon stream; (3) removing the remainder of the sulfur-containing coke from said catalyst particles by combusting said coke in a regeneration zone in the presence of elemental oxygen, thereby reactivating said catalyst particles for the cracking reactions of step (1) and producing a SO x -containing flue gas stream; and (4) recycling the regenerated catalyst particles to step (1), said process further comprising introducing fresh catalyst particles into, and withdrawing catalyst particles from, the stream of catalyst particles recycling through steps (1) to (4) at a rate sufficient to maintain the activity and selectivity of the recycling catalyst particles for converting said hydrocarbon feedstock into said first product hydrocarbon stream in said catalytic cracking reaction zone, the improvement comprising continuously dissolving in said sulfur-containing hydrocarbon feedstock one or more organic, aluminum-containing compounds such that, when the hydrocarbon feedstock is catalytically cracked in step (1), the aluminum-containing compound or compounds are converted to compounds of aluminum dispersed relatively uniformly upon the surfaces of the catalyst particles, said dissolving of said aluminum-containing compounds being at a rate such that, under steady state conditions, the proportion of dispersed aluminum compounds (calculated as Al 2 O 3 ) maintained on the catalyst particles being recirculated through steps (1) to (4) is between about 0.1 and 10.0 catalyst weight percent while the amount of SO x compounds removed in the regenerator is no less than 5 lbs. (calculated as SO 2 ) for each pound of said aluminum-containing compounds (calculated as Al 2 O 3 ) dissolved in said feedstock.

Claim 10

A process as defined in claim 6 wherein said organic, aluminum-containing compound is selected from the group consisting of aluminum isopropoxide, aluminum s-butoxide, aluminum acetylacetonate, and combinations thereof.

Claim 11

In a fluidized catalytic cracking process comprising the cyclical steps of (1) contacting a sulfur-containing hydrocarbon feedstock stream with a bed of fluidized cracking catalyst particles in a catalytic cracking zone under conditions sufficient to produce a first product hydrocarbon stream having an average molecular weight and boiling point lower than that of the hydrocarbon feedstock stream and to further produce a stream of catalyst particles deactivated by the deposition of sulfur-containing coke upon the surfaces thereof; (2) steam stripping said catalyst particles to remove some of the sulfur-containing coke therefrom and produce a second product hydrocarbon stream; (3) removing the remainder of the sulfur-containing coke from said catalyst particles by combusting said coke in a regeneration zone in the presence of elemental oxygen, thereby reactivating said catalyst particles for the cracking reactions of step (1) and producing a SO x -containing flue gas stream; and (4) recycling the regenerated catalyst particles to step (1), said process further comprising introducing fresh particles to, and removing spent catalyst from, the catalyst particles recycling through steps (1) to (4) at a rate sufficient to maintain the activity and selectivity of the recycling catalyst particles for converting said hydrocarbon feedstock into said first product hydrocarbons in said catalytic cracking reaction zone, the improvement comprising maintaining a relatively uniform dispersion of solid aluminum components upon the surfaces of the catalyst particles recycled through steps (1) to (4) by introducing in said cyclical fluidized catalytic cracking process in dissolved form one or more organic, aluminum-containing compounds, said dispersion of solid aluminum components (calculated as Al 2 O 3 ) comprising between about 0.1 and 10.0 catalyst wt.%, and said dispersion alternately comprising (a) solid aluminum compounds containing both sulfur and aluminum atoms produced by reacting SO x compounds in step (3) with the components of said dispersion and (b) solid aluminum compounds made active for reacting with SO x compounds in step (3) by passing said dispersion containing said solid aluminum compounds containing both sulfur and aluminum atoms successively through steps (1) and (2).

Claim 12

In a fluidized catalytic cracking process comprising the cyclical steps of (1) contacting a sulfur-containing hydrocarbon feedstock stream with a bed of fluidized cracking catalyst particles in a catalytic cracking zone under conditions sufficient to produce a first product hydrocarbon stream having an average molecular weight and boiling point lower than that of the hydrocarbon feedstock stream and to further produce a stream of catalyst particles deactivated by the deposition of sulfur-containing coke upon the surfaces thereof; (2) steam stripping said catalyst particles to remove some of the sulfur-containing coke therefrom and produce a second product hydrocarbon stream; (3) removing the remainder of the sulfur-containing coke from said catalyst particles by combusting said coke in a regeneration zone in the presence of elemental oxygen, thereby reactivating said catalyst particles for the cracking reactions of step (1) and producing a SO x -containing flue gas stream; and (4) recycling the regenerated catalyst particles to step (1), said process further comprising introducing fresh particles to, and removing spent catalyst from, the catalyst particles recycling through steps (1) to (4) at a rate sufficient to maintain the activity and selectivity of the recycling catalyst particles for converting said hydrocarbon feedstock into said first product hydrocarbons in said catalytic cracking reaction zone, the improvement comprising maintaining a relatively uniform dispersion of solid aluminum components upon the surfaces of the catalyst particles recycled through steps (1) to (4) by introducing in said cyclical fluidized catalytic cracking process in dissolved form one or more organic, aluminum-containing compounds, said dispersion of solid aluminum components (calculated as Al 2 O 3 ) comprising between about 0.1 and 10.0 catalyst wt.%, and said dispersion alternately comprising (a) solid aluminum compounds containing both sulfur and aluminum atoms produced by reacting SO x compounds in step (3) with the components of said dispersion and (b) solid aluminum compounds made active for reacting with SO x compounds in step (3) by passing said dispersion containing said solid aluminum compounds containing both sulfur and aluminum atoms successively through steps (1) and (2).

Claim 13

A process as defined in claim 8 wherein said organic, aluminum-containing compound is selected from the group consisting of aluminum isopropoxide, aluminum s-butoxide, and aluminum acetylacetonate.