Aluminum passivation process

Claim 2

The improved process of claim 1 wherein the liquid medium is water substantially free from any contaminating metal.

Claim 3

The improved process of claim 1 wherein the liquid medium is an organic medium capable of dissolving at least a portion of said at least one aluminum-containing material.

Claim 4

The improved process of claims 1, 2 or 3 wherein at least a portion of said treated catalyst is calcined prior to being transferred to said reaction zone.

Claim 5

In a process for converting a hydrocarbon material having at least one metal contaminant selected from the group consisting of nickel, vanadium, iron and copper which comprises contacting the hydrocarbon material in a reaction zone at hydrocarbon conversion conditions with a catalyst containing a catalytically effective amount of at least one zeolite and containing about 0.75% to about 2% by weight of all of said metal contaminants to form a conversion product and a deactivated catalyst having carbonaceous deposits and containing at least a portion of said metal contaminant, and regenerating at least a portion of said deactivated catalyst to restore at least a portion of its catalytic activity by removing at least a portion of said carbonaceous deposits to form a regenerated catalyst, the improvement which comprises: contacting said regenerated catalyst with an aqueous solution having a pH in the range of about 2 to about 5 containing an effective amount of an aluminum compound passivating at least a portion of said metal contaminant therein, changing the pH of said aqueous solution to a value which will induce at least a portion of said aluminum compound to deposit on said regenerated catalyst, thereby forming a treated catalyst without removal of said at least one metal contaminant containing aluminum atoms from said aluminum compound, and transferring at least a portion of said treated catalyst to said reaction zone, whereby said treated catalyst has an improved catalytic activity beyond that otherwise achieved by removal of an equivalent amount of metal contaminants, if any, removed by the claimed process.

Claim 6

In a process for converting a hydrocarbon material having at least one metal contaminant selected from the group consisting of nickel, vanadium, iron and copper which comprises contacting the hydrocarbon material in a reaction zone at hydrocarbon conversion conditions with a catalyst containing a catalytically effective amount of at least one zeolite and containing about 0.75% to about 2% by weight of all of said metal contaminants to form a conversion product in a deactivated catalyst having carbonaceous deposits and containing at least a portion of said metal contaminants, and regenerating at least a portion of said deactivated catalyst to restore at least a portion of its catalytic activity by removing at least a portion of said carbonaceous deposits to form a regenerated catalyst, the improvement which comprises: contacting at least a portion of said regenerated catalyst with an organic medium containing an effective amount of an aluminum compound at least partially dissolved therein, seperating a treated catalyst without removal of said at least one metal contaminant, from said organic medium wherein at least a portion of the aluminum compounds from said medium have been deposited on said treated catalyst and transferring at least a portion of said treated catalyst to said reaction zone, whereby said said treated catalyst has an improved catalytic activity beyond that otherwise achieved by removal of an equivalent amount of metal contaminants, if any, removed by the claimed process.

Claim 7

The improved process of claims 5 or 6 wherein at least a portion of said treated catalyst is calcined prior to being transferred to said reaction zone.

Claim 8

In a process for converting a hydrocarbon material having at least one metal contaminant selected from the group consisting of nickel, vanadium, iron and copper which comprises contacting the hydrocarbon material in a reaction zone at hydrocarbon conversion conditions with a catalyst containing a catalytically effective amount of at least one zeolite and containing about 0.75% to about 2% by weight thereof of all of said metal contaminants to form a conversion product and a deactivated catalyst having carbonaceous deposits and containing at least a portion of said metal contaminant, and regenerating at least a portion of said deactivated catalyst to restore at least a portion of its catalytic activity by removing at least a portion of said carbonaceous deposits to form a regenerated catalyst, the improvement which comprises: introducing into said hydrocarbon material an effective amount of at least one aluminum compound at least partially soluble in said hydrocarbon material and contacting said hydrocarbon material with said catalyst in said reaction zone, whereby aluminum atoms from said at least one aluminum compound become associated with said catalyst and help maintain the catalytic activity of said catalyst without removal of any of said at least one metal contaminant.

Claim 9

In a process for converting a hydrocarbon material having at least one metal contaminant selected from the group consisting of nickel, vanadium, iron and copper which comprises contacting the hydrocarbon material in a reaction zone at hydrocarbon conversion conditions with a catalyst containing a catalytically effective amount of at least one zeolite and containing about 0.75% to about 2% by weight thereof of all of said metal contaminants to form a conversion product and a deactivated catalyst having carbonaceous deposits and containing at least a portion of said metal contaminant, and regenerating at least a portion of said deactivated catalyst to restore at least a portion of its catalytic activity by removing at least a portion of said carbonaceous deposits to form a regenerated catalyst, the improvement which comprises: introducing into said hydrocarbon material an effective amount of at least one aluminum compound at least partially soluble in said hydrocarbon material and contacting said hydrocarbon material with said catalyst in said reaction zone, whereby aluminum atoms from said at least one aluminum compound become associated with said catalyst and help maintain the catalytic activity of said catalyst without removal of any of said at least one metal contaminant.

Claim 10

The improved process of claims 1, 3, 5 or 8 wherein said aluminum compound is selected from the group of such compounds consisting of diketonates, sulfonates, dithiophosphates, alkoxides, carboxylates having from 1 to 20 carbon atoms, organic aluminum compound having the formula R 3 Al wherein each R is selected from a group consisting of hydrocarbyl and halogen substituted hydrocarbyl materials which can contain from 1 to 20 carbon atoms, organic aluminum halides having the formula R n AlX 3-n wherein n can have values of 1 or 2, and organic oxyaluminum having the formula R n Al(R'O) 3-n wherein each R and R' individually have from hydrocarbyl and halogen substituted hydrocarbyl which can contain 1 to 20 carbon atoms and n has an integer value of from 0 to 3, carbonyls, metallocenes, hydrocarbyl and halogen substituted hydrocarbyl phosphine and phosphite complexes wherein each has 1 to 20 carbon atoms, and olefin and diolefin complexes having from 2 to 20 carbon atoms, oxalate, acetate, AlBr 3 , AlI 3 , diethylmalonate and 1-phenylsulfonate.

Claim 11

The improved process of claims 1, 2, 5 or 8 wherein said aluminum compound is selected from the group of such compounds consisting of Al(NO 3 ) 3 , Al 2 (SO 4 ) 3 , AlPO 4 , Al(C 6 H 5 O) 3 , Al(Ac) 3 wherein Ac is acetate, (NH 4 )Al(SO 4 ) 2 , (Al(BrO 3 ) 3 , Al(ClO 3 ) 3 , Al(ClO 4 ) 3 , Al(C 2 H 5 O) 3 , Al-lactate, Al-oleate and AlX 3 where each X is individually selected from the group of halogens consisting of F, Cl, Br and I.

Claim 12

In the improved process of claims 1, 2, 3, 5, 6 or 8 wherein said effective amount of said at least one aluminum compound is such that an atomic ratio of all aluminum atoms from said at least one aluminum compound to total atoms from said metal contaminant contained in said treated catalyst is in the range of about 0.05:1 to about 3:1.

Claim 13

In the improved process of claim 8, wherein said effective amount of said aluminum compound is such that an atomic ratio of all aluminum atoms from said at least one aluminum compound to all atoms of said metal contaminant in said hydrocarbon material is in the range of about 0.05:1 to about 3:1.

Claim 14

In the improved process of claims 1, 2, 3, 5, 6 or 8 wherein the effective amount of said aluminum, calculated as atomic aluminum, in moles per liter of liquid medium is within the range of about 0.03 to about 1 when the concentration of metal contaminant, calculated as its element, in the contaminated catalyst is in the range of about 0.2% by weight to about 3.5% by weight, as based upon the total weight of the catalyst.