Process for catalytically cracking metals-containing hydrocarbon feedstocks

Claim 2

In a catalytic cracking process wherein a metal contaminants-containing hydrocarbon feedstock is converted in a catalytic cracking reaction zone to more valuable hydrocarbons of lower average molecular weight and boiling point by contact with cracking catalysts particles at an elevated temperature, the improvement comprising adding one or more organic aluminum compounds into the hydrocarbon feedstock entering the catalytic cracking reaction zone, said feedstock containing between about 5 and 50 wppm of metals contaminants.

Claim 3

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

Claim 4

A process as defined in claim 1 wherein said hydrocarbon feedstock comprises a vacuum of atmospheric residual fraction.

Claim 5

A process as defined in claim 1 wherein said one or more organic aluminum compounds are added into said hydrocarbon feedstock by dissolution at a rate such that the blend of said feedstock and organic aluminum compounds contains at least one mole of aluminum, calculated as the metal, for each mole of vanadium, copper, nickel, and iron contaminants, calculated as the free metals.

Claim 6

In a process for catalytically cracking hydrocarbons the improvement comprising (1) subjecting a hydrocarbon feedstock containing between about 5 and 50 wppm of metal contaminants to catalytic cracking conditions in the presence of cracking catalyst particles, whereby said hydrocarbon feedstock is converted into a product hydrocarbon of lower average molecular weight and boiling point, and (2) utilizing cracking catalyst particles in step (1) which contain one or more aluminum components deposited on the surfaces thereof during step (1).

Claim 7

In a process for catalytically cracking hydrocarbons the improvement comprising (1) subjecting a hydrocarbon feedstock containing between about 5 and 50 wppm of metal contaminants to catalytic cracking conditions in the presence of cracking catalyst particles, whereby said hydrocarbon feedstock is converted into a product hydrocarbon of lower average molecular weight and boiling point, and (2) utilizing cracking catalyst particles in step (1) which contain one or more aluminum components deposited on the surfaces thereof during step (1).

Claim 8

A process as defined in claim 5 wherein said hydrocarbon feedstock contains metal contaminants selected from the group consisting of vanadium, iron, nickel, and copper contaminants.

Claim 9

A process as defined in claim 5 wherein said hydrocarbon feedstock comprises a residual fraction.

Claim 10

In a fluid catalytic cracking process for cracking hydrocarbons wherein catalyst particles are recirculated through (1) a catalytic cracking reaction zone wherein a metal contaminants-containing hydrocarbon feedstock is converted to a product hydrocarbon, (2) a stripping zone wherein carbonaceous material on the surface of the catalyst particles is stripped to yield more product hydrocarbon, and (3) a regeneration zone wherein remaining carbonaceous material on said catalyst surfaces is removed by combustion in the presence of a free oxygen-containing gas, the improvement wherein said feedstock comprises between 5 and 50 wppm metals contaminants and wherein aluminum components are deposited onto said catalyst particles while said particles are recirculated.

Claim 11

In a fluid catalytic cracking process for cracking hydrocarbons wherein catalyst particles are recirculated through (1) a catalytic cracking reaction zone wherein a metal contaminants-containing hydrocarbon feedstock is converted to a product hydrocarbon, (2) a stripping zone wherein carbonaceous material on the surface of the catalyst particles is stripped to yield more product hydrocarbon, and (3) a regeneration zone wherein remaining carbonaceous material on said catalyst surfaces is removed by combustion in the presence of a free oxygen-containing gas, the improvement wherein said feedstock comprises between 5 and 50 wppm metals contaminants and wherein aluminum components are deposited onto said catalyst particles while said particles are recirculated.

Claim 12

A process as defined in claim 8 wherein said hydrocarbon feedstock contains metal contaminants selected from the group consisting of vanadium, iron, nickel, and copper contaminants.

Claim 13

A process as defined in claim 9 wherein said aluminum components are deposited on said cracking catalyst particles by introducing a solution containing a dissolved aluminum component into the regeneration zone of said fluid catalytic cracking process.

Claim 14

In a process for catalytically cracking hydrocarbons in a catalytic cracking cycle comprising the alternate steps of (1) subjecting a hydrocarbon feedstock to catalytic cracking conditions in the presence of cracking catalyst particles, whereby said hydrocarbon feedstock is converted into a product hydrocarbon of lower average molecular weight and boiling point, and (2) removing carbonaceous material from the surface of said catalyst particles, the improvement comprising (a) utilizing in step (1) a hydrocarbon feedstock containing between about 5 and 50 wppm of metals contaminants, including at least some vanadium contaminants and (b) depositing aluminum components on said cracking catalyst particles while said catalyst particles are in said cracking cycle.

Claim 15

In a process for catalytically cracking hydrocarbons in a catalytic cracking cycle comprising the alternate steps of (1) subjecting a hydrocarbon feedstock to catalytic cracking conditions in the presence of cracking catalyst particles, whereby said hydrocarbon feedstock is converted into a product hydrocarbon of lower average molecular weight and boiling point, and (2) removing carbonaceous material from the surface of said catalyst particles, the improvement comprising (a) utilizing in step (1) a hydrocarbon feedstock containing between about 5 and 50 wppm of metals contaminants, including at least some vanadium contaminants and (b) depositing aluminum components on said cracking catalyst particles while said catalyst particles are in said cracking cycle.

Claim 16

A process as defined in claim 11 wherein said cracking cycle is a fluid catalytic cracking cycle wherein catalyst particles are recirculated through (a) a catalytic cracking reaction zone wherein said hydrocarbon feedstock is subjected to said catalytic cracking conditions to yield said product hydrocarbon, (b) a stripping zone wherein carbonaceous material on the catalyst surfaces is stripped to yield more product hydrocarbons, and (c) a regeneration zone wherein remaining carbonaceous material on said catalyst surfaces is removed by combustion in the presence of a free oxygen-containing gas.

Claim 17

A process as defined in claim 5, 6, 7, 8, 9, 10, 11, or 12 wherein at least some of said aluminum components are deposited on said cracking catalyst particles by introducing into step (1) one or more organic aluminum compounds in dissolved form.

Claim 18

A process as defined in claim 13 wherein said organic aluminum compounds are selected from the group consisting of aluminum isopropoxide, aluminum s-butoxide, and aluminum acetylacetonate, and said organic aluminum compounds are dissolved in the hydrocarbon feedstock.

Claim 19

A process as defined in claim 1, 2, or 3 wherein said one or more organic compounds are added in dissolved form.

Claim 20

A process as defined in claim 15 wherein said hydrocarbon feedstock contains vanadium.

Claim 21

A process as defined in claim 15 wherein said hydrocarbon feedstock consists essentially of a residual fraction containing vanadium.

Claim 22

A process as defined in claim 1, 2, 4, 5, or 8 wherein said hydrocarbon feedstock comprises a residual fraction containing vanadium.

Claim 23

A process as defined in claim 5 or 8 wherein at least some of said aluminum components are deposited on said cracking catalyst by introducing into step (1) one or more organic aluminum compounds in dissolved form and wherein said hydrocarbon feedstock comprises a residual fraction containing vanadium.

Claim 24

A process as defined in claim 19 wherein said hydrocarbon feedstock contains metal contaminants selected from the group consisting of vanadium, copper, nickel, and iron, and said organic aluminum compounds are introduced into step (1) at a rate providing at least one mole of aluminum for each mole of vanadium, copper, nickel, and iron present in the feedstock also introduced into step (1).

Claim 25

In a fluid catalytic cracking process wherein catalyst particles are recirculated successively through a catalytic cracking reaction zone, a stream stripping zone, and a regeneration zone while a metal contaminants-containing hydrocarbon feedstock is introduced into said catalytic cracking reaction zone and therein converted to a product hydrocarbon of lower average molecular weight and lower average boiling point, the improvement wherein aluminum isopropoxide is dissolved into said hydrocarbon feedstock and said hydrocarbon feedstock comprises between about 5 and 50 wppm of metals contaminants.

Claim 26

In a fluid catalytic cracking process wherein catalyst particles are recirculated successively through a catalytic cracking reaction zone, a stream stripping zone, and a regeneration zone while a metal contaminants-containing hydrocarbon feedstock is introduced into said catalytic cracking reaction zone and therein converted to a product hydrocarbon of lower average molecular weight and lower average boiling point, the improvement wherein aluminum isopropoxide is dissolved into said hydrocarbon feedstock and said hydrocarbon feedstock comprises between about 5 and 50 wppm of metals contaminants.

Claim 27

A process as defined in claim 1, 2, 4, 5, 6, 8, 9, 10, 11, 12, or 21 wherein said hydrocarbon feedstock consists essentially of a residual fraction containing vanadium.