Passivating metals on cracking catalysts with antimony compounds

Claim 2

A process for catalytic cracking of hydrocarbons wherein a. a hydrocarbon feed is introduced into a cracking zone, b. said feed is contacted in said cracking zone with the cracking catalyst under cracking conditions whereby the feed is cracked, c. the cracked feed is removed from said cracking zone for further processing, and d. metals deposited on said cracking catalyst and tending to deactivate said cracking catalyst are passivated by contacting said cracking catalyst with an antimony compound having the general formula ##STR4## wherein the radicals R which can be the same or different are hydrocarbyl radicals having from 1 to about 18 carbon atoms per molecule.

Claim 3

A process in accordance with claim 1 wherein said antimony compound is added to said hydrocarbon feed.

Claim 4

A process in accordance with claim 2 wherein said antimony compound is metered to the hydrocarbon feedstock until a predetermined level of said compound on the catalyst is reached and wherein thereafter the antimony compound is metered to the feedstock in a quantity sufficient to maintain said level.

Claim 5

A process in accordance with claim 3 wherein the antimony compound initially is fed to the hydrocarbon feedstock in a quantity in the range of about 0.1 to 15,000 ppm based on the hydrocarbon feedstock.

Claim 6

A process in accordance with claim 1 wherein the entire number of carbon atoms per molecule of antimony compound is between 6 and about 90.

Claim 7

A proess in accordance with claim 1 wherein the radicals R are selected from the group consisting of alkyl or cycloalkyl radicals having 2 to about 10 carbon atoms per radical, substituted or unsubstituted cyclopentyl and cyclohexyl radicals, and substituted and unsubstituted phenyl radicals.

Claim 8

A process in accordance with claim 1 wherein said antimony compound comprises about 6 to about 21 weight percent antimony.

Claim 9

A process in accordance with claim 1 wherein said antimony compound is used in a quantity of up to about 1.5 weight percent of the catalyst to be treated.

Claim 10

A process in accordance with claim 2 wherein said antimony compound is added to the hydrocarbon feed upstream of a pump feeding said feed into the cracking zone.

Claim 11

In a process for catalytic cracking of hydrocarbons, wherein a hydrocarbon feed is introduced into a cracking zone, said feed is contacted in said cracking zone with a cracking catalyst under cracking conditions whereby the feed is cracked, wherein the cracked feed is removed from the cracking zone for further processing, wherein the cracking catalyst is circulated from the cracking zone to a regeneration zone and back, the improvement comprising passivating contaminating metals deposited on said catalyst by contacting said catalyst with an antimony compound having the general formula ##STR5## wherein the R groups which can be the same or different are hydrocarbyl radicals each containing from 1 to about 18 carbon atoms.

Claim 12

In a process for catalytic cracking of hydrocarbons, wherein a hydrocarbon feed is introduced into a cracking zone, said feed is contacted in said cracking zone with a cracking catalyst under cracking conditions whereby the feed is cracked, wherein the cracked feed is removed from the cracking zone for further processing, wherein the cracking catalyst is circulated from the cracking zone to a regeneration zone and back, the improvement comprising passivating contaminating metals deposited on said catalyst by contacting said catalyst with an antimony compound having the general formula ##STR5## wherein the R groups which can be the same or different are hydrocarbyl radicals each containing from 1 to about 18 carbon atoms.

Claim 13

The process of claim 10 wherein the antimony compound is added to the hydrocarbon feed to the cracking zone.