Advanced elevated feed distribution apparatus and process for large diameter FCC reactor risers

Patent metadata

Field	Value
Publication number	US-9238209-B2
Application number	US-201113029274-A
Country	US
Kind code	B2
Filing date	Feb 17, 2011
Priority date	Feb 18, 2010
Publication date	Jan 19, 2016
Grant date	Jan 19, 2016

Abstract

An FCC process and apparatus may include injecting hydrocarbon feedstock at different radial positions while at the same elevation inside a riser. Multiple distributors may be used to position the tips for injecting feedstock at multiple radial positions. The distributors with tips more deeply positioned in the riser will penetrate a dense catalyst column we discovered generates in risers of larger diameter over 1.3 meters.

First claim

The invention claimed is:

1. A fluid catalytic cracking process comprising:
passing catalyst and inert gas upwardly in a riser having a wall and an inner diameter defined by said wall of at least 1.3 meters;
injecting a hydrocarbon feedstock into said riser from at least two distributors penetrating said wall of said riser and having respective tips with at least one opening in each of said tips, said respective tips of said at least two distributors positioned at the same elevation within a margin of 0.1 inner diameters of said riser at the elevation of the feed distributors but positioned at different radial distances from said wall in said riser, said at least two distributors including an inner distributor and an outer distributor and of the total hydrocarbon feedstock injected from the inner distributor and the outer distributor, at least 8 and less than 50 wt-% is injected from the inner distributor;
cracking said hydrocarbon feedstock in the presence of said catalyst to produce a cracked stream; and
separating said catalyst from said cracked stream.

2. The process of claim 1 wherein said catalyst and inert gas pass upwardly at a rate of less than 4.7 meters per second.

3. The process of claim 2 wherein said catalyst and inert gas pass upwardly at a rate of less than 4 meters per second.

4. The process of claim 3 wherein said catalyst and inert gas pass upwardly at a rate of less than 3.3 meters per second.

5. The process of claim 1 wherein said inner diameter of said riser is less than or equal to 1.7 meters.

6. The process of claim 5 wherein said catalyst and inert gas pass upwardly at a rate of less than 4.7 meters per second.

7. The process of claim 6 wherein said catalyst and inert gas pass upwardly at a rate of less than 4 meters per second.

8. The process of claim 7 wherein said catalyst and inert gas pass upwardly at a rate of less than 3.3 meters per second.

9. A fluid catalytic cracking process comprising: passing catalyst and inert gas upwardly at a rate of less than 4.7 meters (4 feet) per second in a riser having a wall and an inner diameter defined by said wall of between 1.3 and 2.2 meters;
injecting a hydrocarbon feedstock into said riser from at least two distributors penetrating said wall of said riser and having tips and at least one opening in each of said tips, said tips positioned at the same elevation within a margin of 0.1 inner diameters of said riser at the elevation of the feed distributors but positioned at different radial distances from said wall in said riser, said at least two distributors including an inner distributor and an outer distributor and of the total hydrocarbon feedstock injected from the inner distributor and the outer distributor, at least 8 and less than 50 wt-% is injected from the inner distributor;
cracking said hydrocarbon feedstock in the presence of said catalyst to produce a cracked stream; and
separating said catalyst from said cracked stream.

10. The process of claim 9 wherein said catalyst and inert gas pass upwardly at a rate of no more than 3.3 meters per second.

11. The process of claim 10 wherein said riser has an inner diameter of less than or equal to 1.6 meters.

12. The process of claim 1 , wherein at least 8 and less than or equal to 20 wt-% of the total hydrocarbon feedstock is injected from the inner distributor.

13. The process of claim 9 , wherein at least 8 and less than or equal to 20 wt-% of the total hydrocarbon feedstock is injected from the inner distributor.

14. The process of claim 1 , wherein:
said at least two distributors include a plurality of said inner distributors and a plurality of said outer distributors,
all of said distributors are positioned at the same elevation within a margin of 0.1 inner diameters of said riser, and
wherein half of said distributors comprise said inner distributors and half of said distributors comprise said outer distributors.

15. The process of claim 9 , wherein:
said at least two distributors include a plurality of said inner distributors and a plurality of said outer distributors,
all of said distributors are positioned at the same elevation within a margin of 0.1 inner diameters of said riser, and
wherein half of said distributors comprise said inner distributors and half of said distributors comprise said outer distributors.

16. A fluid catalytic cracking process comprising:
passing catalyst and inert gas upwardly in a riser having a wall and an inner diameter defined by said wall of at least 1.3 meters;
injecting a hydrocarbon feedstock into said riser from at least two distributors having respective tips with at least one opening in each of said tips, said respective tips of said at least two distributors positioned at the same elevation within a margin of 0.25 inner diameters of said riser at the elevation of the feed distributors but positioned at different radial distances from said wall in said riser, said at least two distributors including an inner distributor and an outer distributor and of the total hydrocarbon feedstock injected from the inner distributor and the outer distributor, at least 8 and less than 50 wt-% is injected from the inner distributor;
cracking said hydrocarbon feedstock in the presence of said catalyst to produce a cracked stream; and
separating said catalyst from said cracked stream,
wherein said inner distributor and said outer distributor are arranged such that:
said tip of said inner distributor is separated from said wall of said riser by a distance S 1 , wherein S 1 is equal to between about 5% and about 45% of said inner diameter of said riser;
said tip of said outer diameter is separated from said wall of said riser by a distance S 2 ; and
the difference between said distance S 1 and said distance S 2 is equal to between about 15% and 40% of said inner diameter of said riser.

17. The process of claim 1 , wherein said inner distributor and said outer distributor are arranged such that:
said tip of said inner distributor is separated from said wall of said riser by a distance S 1 , wherein S 1 is equal to between about 5% and about 45% of said inner diameter of said riser;
said tip of said outer diameter is separated from said wall of said riser by a distance S 2 ; and
the difference between said distance S 1 and said distance S 2 is equal to between about 15% and 40% of said inner diameter of said riser.

18. The process of claim 9 , wherein said inner distributor and said outer distributor are arranged such that:
said tip of said inner distributor is separated from said wall of said riser by a distance S 1 , wherein S 1 is equal to between about 5% and about 45% of said inner diameter of said riser;
said tip of said outer diameter is separated from said wall of said riser by a distance S 2 ; and
the difference between said distance S 1 and said distance S 2 is equal to between about 15% and 40% of said inner diameter of said riser.

Assignees

• Couch Keith A
• Mehlberg Robert L
• Mostofi-Ashtiani Mohammad-Reza
• Uop Llc

Inventors

• Couch Keith A
• Mehlberg Robert L
• Mostofi-Ashtiani Mohammad-Reza

Classifications

• C10G11/18

  according to the "fluidised-bed" technique · CPC title

• B01J8/1827 Primary

  the fluidising gas being a reactant · CPC title