Gas distributor nozzle system with sintered metal filter media
US-2024075443-A1 · Mar 7, 2024 · US
US9309468B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9309468-B2 |
| Application number | US-82638010-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 29, 2010 |
| Priority date | Jun 29, 2010 |
| Publication date | Apr 12, 2016 |
| Grant date | Apr 12, 2016 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
An FCC process may include a distributor disposed in a recess in a wall of the riser for distributing gaseous hydrocarbon feed to a riser. The distributor may be shielded from upwardly flowing catalyst by a shield. An array of nozzles from the distributor may extend through openings in the shield.
Opening claim text (preview).
The invention claimed is: 1. A fluid catalytic cracking process comprising: delivering catalyst to a riser having a wall and a recess in said wall surrounding said riser, wherein said recess is defined by a convex bulge in said wall; feeding gaseous hydrocarbon feed to a feed distributor disposed in said recess, said feed distributor comprising a tubular header having a round longitudinal axis, and an array of radially oriented nozzles extending from said header; and directing said gaseous feed from said radially oriented nozzles in said header towards the center of the riser into contact with said catalyst flowing upwardly in said riser. 2. The fluid catalytic cracking process of claim 1 , wherein said gaseous hydrocarbon feed is a naphtha cut. 3. The fluid catalytic cracking process of claim 1 , further comprising feeding said tubular header with said gaseous hydrocarbon feed and spraying said gaseous hydrocarbon feed from said header through said array of nozzles into said riser. 4. The fluid catalytic cracking process of claim 3 further comprising spraying said gaseous hydrocarbon feed through two rows of nozzles from said header. 5. The fluid catalytic cracking process of claim 1 , further comprising feeding an inert gas with said hydrocarbon feed to said tubular header. 6. The fluid catalytic cracking process of claim 1 , further comprising spraying said hydrocarbon feed from behind an imaginary line extending between a top innermost intersection of a bulge defining said recess and said wall and a bottom innermost intersection of said bulge defining said recess and said wall at the same radial position as the top innermost intersection. 7. The fluid catalytic cracking process of claim 6 , further comprising shielding said distributor from catalyst flowing upwardly in said riser with a shield secured to said header. 8. The fluid catalytic cracking process of claim 1 , further comprising spraying said gaseous hydrocarbon feed from a header that extends only partially around the riser. 9. The fluid catalytic cracking process of claim 1 , further comprising spraying said gaseous hydrocarbon feed from a first distributor and a second distributor disposed below said first distributor. 10. A fluid catalytic cracking process comprising: delivering catalyst to a riser having a wall and a recess defined by a convex bulge in said wall surrounding said riser, an inner diameter of the riser increasing in said convex bulge, wherein said recess is shielded to prevent said catalyst flowing upwardly in said riser from infiltrating the recess; feeding gaseous hydrocarbon feed to a feed distributor disposed in said recess; and spraying gaseous feed from nozzles in said feed distributor from behind an imaginary line extending between a top innermost intersection of a bulge defining said recess and said wall and a bottom innermost intersection of said bulge defining said recess and said wall at the same radial position as the top innermost intersection. 11. The fluid catalytic cracking process of claim 10 , further comprising feeding said distributor including a tubular header having a round longitudinal axis with said gaseous hydrocarbon feed and spraying said gaseous hydrocarbon feed from said header through an array of nozzles extending from said header into said riser. 12. The fluid catalytic cracking process of claim 11 further comprising spraying said gaseous hydrocarbon feed through two rows of nozzles from said header. 13. The fluid catalytic cracking process of claim 11 , further comprising spraying said gaseous hydrocarbon feed from said header that extends only partially around the riser. 14. The fluid catalytic cracking process of claim 11 , further comprising shielding said distributor from catalyst with a shield secured to said header. 15. The fluid catalytic cracking process of claim 10 , wherein said feed distributor is a first feed distributor and further comprising spraying said gaseous hydrocarbon feed from a second feed distributor disposed in said recess below said first feed distributor. 16. The fluid catalytic cracking process of claim 10 , wherein said gaseous hydrocarbon feed is a naphtha cut. 17. The fluid catalytic cracking process of claim 10 , wherein said recess is defined by a convex bulge in said wall. 18. The fluid catalytic cracking process of claim 10 , further comprising feeding an inert gas with said hydrocarbon feed to said distributor. 19. A fluid catalytic cracking process comprising: delivering catalyst to a riser having a wall and a recess having an upper diagonal side in said wall surrounding said riser, an inner diameter of the riser increasing in said recess, wherein the upper diagonal side tapers inwardly to decrease the diameter of said riser; feeding gaseous feed comprising a naphtha cut to a feed distributor disposed in said recess, said feed distributor comprising a tubular header having a round longitudinal axis, and an array of nozzles extending from said header; and spraying gaseous feed from said nozzles in said header into contact with said catalyst.
inside the bed, e.g. baffles · CPC title
using cyclones · CPC title
Nozzle-type feeding elements · CPC title
according to the "fluidised-bed" technique · CPC title
Retrofitting operations · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.