Catalytic cracking process with CO2 -stripped regenerated catalyst

Claim 2

In a catalytic cracking process wherein a hydrocarbonaceous oil feed is contacted with a cracking catalyst under catalytic cracking conditions in a catalytic cracking zone whereby a carbonaceous deposit is formed on said catalyst and wherein said catalyst with said carbonaceous deposit is contacted with an oxygen- and nitrogen-containing gas in a regeneration zone to remove at least a portion of said carbonaceous deposit, said regenerated catalyst having entrained nitrogen, and wherein the regenerated catalyst is recycled to said catalytic cracking zone, the improvement which comprises: (a) contacting the regenerated catalyst having entrained nitrogen with a stripping gas comprising at least about 80 mole percent of carbon dioxide for a time sufficient to remove said entrained nitrogen from said catalyst prior to recycling the regenerated catalyst to said catalytic cracking zone, and (b) recovering from said catalytic cracking zone a C 2 -- gaseous effluent substantially free of nitrogen.

Claim 3

The process of claim 1 wherein said stripping gas comprises from about 90 to about 95 mole percent carbon dioxide.

Claim 4

The process of claim 1 wherein said stripping gas comprises less than about 5 mole percent of nitrogen.

Claim 5

The process of claim 1 wherein said stripping gas comprises less than about 1 mole percent of nitrogen.

Claim 6

The process of claim 1 wherein said stripping gas comprises less than about 15 mole percent of steam.

Claim 7

The process of claim 1 wherein said stripping gas comprises not more than about 10 mole percent of steam.

Claim 8

The process of claim 1 wherein said stripping gas comprises from about 90 to about 95 mole percent of carbon dioxide and less than about 1 mole percent of nitrogen.

Claim 9

The process of claim 1 wherein said carbon dioxide-containing gaseous mixture is a stream obtained from a steam reforming process.

Claim 10

The process of claim 1 wherein said carbon dioxide-containing gaseous mixture is a stream obtained from a partial oxidation process for the production of hydrogen.

Claim 11

The process of claim 1 wherein said contacting of regenerated catalyst and stripping gas is conducted at a temperature ranging from about 1200° to about 1400° F. and at a pressure ranging from about 15 to about 45 psig.

Claim 12

The process of claim 1 wherein said C 2 -- gaseous mixture recovered from said catalytic cracking zone effluent comprises hydrogen, carbon oxides, hydrogen sulfide, CH 4 , C 2 H 4 and C 2 H 6 , and is substantially free of nitrogen contaminant.

Claim 13

In a catalytic cracking process wherein a hydrocarbonaceous oil feed is contacted with a cracking catalyst under catalytic cracking conditions in a catalytic cracking zone whereby a carbonaceous deposit is formed on said catalyst and wherein said catalyst with said carbonaceous deposit is contacted with an oxygen and nitrogen containing gas in a regeneration zone to remove at least a portion of said carbonaceous deposit, said regenerated catalyst having entrained nitrogen, and wherein the regenerated catalyst is recycled to said catalytic cracking zone, the improvement which comprises: (a) contacting the regenerated catalyst having entrained nitrogen with a stripping gas comprising from about 90 to about 95 mole percent of carbon dioxide and less than about 1 mole percent nitrogen at a temperature ranging from about 1200° to about 1400° F. and at a pressure ranging from about 5 to about 45 psig for a time sufficient to remove said entrained nitrogen from said catalyst prior to recycling the regenerated catalyst to said catalytic cracking zone, and (b) recovering from said catalytic cracking zone a C 2 minus gaseous effluent substantially free of nitrogen.

Claim 14

In a catalytic cracking process wherein a hydrocarbonaceous oil feed is contacted with a cracking catalyst under catalytic cracking conditions in a catalytic cracking zone whereby a carbonaceous deposit is formed on said catalyst and wherein said catalyst with said carbonaceous deposit is contacted with an oxygen and nitrogen containing gas in a regeneration zone to remove at least a portion of said carbonaceous deposit, said regenerated catalyst having entrained nitrogen, and wherein the regenerated catalyst is recycled to said catalytic cracking zone, the improvement which comprises: (a) contacting the regenerated catalyst having entrained nitrogen with a stripping gas comprising from about 90 to about 95 mole percent of carbon dioxide and less than about 1 mole percent nitrogen at a temperature ranging from about 1200° to about 1400° F. and at a pressure ranging from about 5 to about 45 psig for a time sufficient to remove said entrained nitrogen from said catalyst prior to recycling the regenerated catalyst to said catalytic cracking zone, and (b) recovering from said catalytic cracking zone a C 2 minus gaseous effluent substantially free of nitrogen.

Claim 15

The process of claim 12 wherein said stripping gas comprises not more than about 10 mole percent steam.