Structured packing element having a spiral helix shape
US-2019076815-A1 · Mar 14, 2019 · US
US11167258B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11167258-B2 |
| Application number | US-201916412044-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 14, 2019 |
| Priority date | May 14, 2019 |
| Publication date | Nov 9, 2021 |
| Grant date | Nov 9, 2021 |
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In an FCC apparatus and process structured packing should be located at the very top of the stripping section in an upper region. The lower region below the structural packing may be equipped with fluidization equipment such as stripping media distributors and one or more gratings. This arrangement enables stripping of entrained hydrocarbons off the incoming catalyst immediately upon entry into the stripping section allowing the entrained hydrocarbon to exit the stripping section with minimized residence time to minimize post-riser cracking. Revamp of stripping sections with tall stripping sections should conducted in this way to improve performance and reduce down-time for equipment installation.
Opening claim text (preview).
The invention claimed is: 1. A process for separating a gaseous hydrocarbon product stream from catalyst particles comprising: contacting a hydrocarbon feed stream with catalyst particles in an elongated riser to produce gaseous hydrocarbon products; disengaging catalyst particles from said gaseous hydrocarbon products; stripping said catalyst particles with stripping media over structural packing in a hydrocarbon rich and stripping media lean environment in an upper region of a stripping section and stripping said catalyst particles with stripping media in a stripping media rich and hydrocarbon lean environment in a lower region of said stripping section; and generating a dense catalyst bed in said stripping section and a top of said structural packing being located at a top of the dense catalyst bed. 2. The process of claim 1 further comprising distributing stripping media to said lower region. 3. The process of claim 1 wherein said lower region is at least 10 feet (3 m) tall. 4. The process of claim 1 further comprising passing said catalyst particles through a grating in said lower region. 5. The process of claim 4 further comprising distributing fluidizing media above said grating. 6. The process of claim 1 further comprising limiting admittance of hydrocarbons into the lower region. 7. A process for separating a gaseous hydrocarbon product stream from catalyst particles comprising: contacting a hydrocarbon feed stream with catalyst particles in an elongated riser to produce gaseous hydrocarbon products; disengaging catalyst particles from said gaseous hydrocarbon products; stripping said catalyst particles with stripping media over structural packing in a hydrocarbon rich and stripping media lean environment in an upper region of a stripping section and stripping said catalyst particles with stripping media in a stripping media rich and hydrocarbon lean environment in a lower region of said stripping section; passing said catalyst particles through a grating in said lower region; and generating a dense catalyst bed in said stripping section and a top of said structural packing being located at a top of the dense catalyst bed. 8. The process of claim 7 further comprising distributing fluidizing media above said grating. 9. The process of claim 7 further comprising distributing stripping media to said lower region. 10. The process of claim 7 further comprising limiting admittance of hydrocarbons into the lower region. 11. The process of claim 7 wherein no more than a height of a layer of the structural packing separates a top layer of the structural packing from a top of the stripping section. 12. The process of claim 7 wherein said lower region is at least 10 feet (3 m) tall. 13. The process of claim 7 wherein said grating is located above a stripping media distributor for distributing fluidizing media below the grating in said lower region.
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