Passivation of cracking catalysts

Claim 3

The method of claim 1 where the reduction zone temperature is maintained at a temperature of at least 500° C. to at least partially passivate said metal contaminant on the catalyst.

Claim 4

In a hydrocarbon cracking process of the type wherein: A. hydrocarbon feedstock containing a metal contaminant selected from the class consisting of nickel, vanadium, and iron is passed into a reaction zone having a cracking catalyst therein at cracking conditions to form cracked hydrocarbon products and wherein coke and at least some of the metal contaminant becomes deposited on the catalyst such that at least a major portion of the total of said metal contaminant deposited on the catalyst comprises only one of said metal contaminants; and B. the coke and metal contaminated catalyst is passed to a regeneration zone maintained at regeneration conditions having a regeneration gas passing therethrough whereby at least a portion of the coke is removed from the catalyst, the improvement which comprises: aa. monitoring the composition of said metal contaminant being deposited on the catalyst; bb. adding an effective passivating amount of at least one of said metal contaminants not present as the major contaminant on the catalyst; and cc. passing the catalyst through a reduction zone maintained at an elevated temperature whereby said metal contaminants are at least partially passivated to thereby decrease the rate of production of hydrogen and coke in the reaction zone, while a reducing environment is maintained in said reduction zone by the addition to the reduction zone of a material selected from the class consisting of hydrogen, carbon monoxide and mixtures thereof prior to the catalyst being returned to the reaction zone.

Claim 5

In a hydrocarbon cracking process of the type wherein: A. hydrocarbon feedstock containing a metal contaminant selected from the class consisting of nickel, vanadium, and iron is passed into a reaction zone having a cracking catalyst therein at cracking conditions to form cracked hydrocarbon products and wherein coke and at least some of the metal contaminant becomes deposited on the catalyst such that at least a major portion of the total of said metal contaminant deposited on the catalyst comprises only one of said metal contaminants; and B. the coke and metal contaminated catalyst is passed to a regeneration zone maintained at regeneration conditions having a regeneration gas passing therethrough whereby at least a portion of the coke is removed from the catalyst, the improvement which comprises: aa. monitoring the composition of said metal contaminant being deposited on the catalyst; bb. adding an effective passivating amount of at least one of said metal contaminants not present as the major contaminant on the catalyst; and cc. passing the catalyst through a reduction zone maintained at an elevated temperature whereby said metal contaminants are at least partially passivated to thereby decrease the rate of production of hydrogen and coke in the reaction zone, while a reducing environment is maintained in said reduction zone by the addition to the reduction zone of a material selected from the class consisting of hydrogen, carbon monoxide and mixtures thereof prior to the catalyst being returned to the reaction zone.

Claim 6

The process of claim 3 wherein the major portion of said metal contaminant comprises nickel and wherein the predetermined amount of metal contaminant added is selected from the class consisting of iron, vanadium and mixtures thereof.

Claim 7

The process of claim 3 wherein the reduction zone is maintained at a temperature in excess of 500° C. to at least partially passivate said metal contaminant.

Claim 8

The process of claim 5 wherein the temperature in the reduction zone is maintained within the range of about 600° C. to about 850° C.

Claim 9

The process of claim 6 further comprising the addition of a passivation agent selected from the class consisting of antimony, tin, bismuth and manganese to further passivate the catalyst.