Method for treating a fluid comprising salts and system for implementing the method
US-2024278147-A1 · Aug 22, 2024 · US
US11427771B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11427771-B2 |
| Application number | US-202016827499-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 23, 2020 |
| Priority date | Mar 27, 2019 |
| Publication date | Aug 30, 2022 |
| Grant date | Aug 30, 2022 |
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A slurry separator comprising a moving blade that wipes slurry oil onto a wall of the slurry separator for separating a recovered oil stream from a concentrated residue stream has the capability of maximizing recovery of the LCO from slurry oil as well as removing both the catalyst fines as well as coke particles suspended in the slurry oil. The slurry separator can be fed directly from the main column bottoms. Advantageously, the process and apparatus can enable the FCC unit to achieve higher production of LCO and higher value clarified slurry oil more efficiently.
Opening claim text (preview).
The invention claimed is: 1. A process for catalytically cracking hydrocarbons comprising: feeding a hydrocarbon feed stream to a FCC reactor and contacting said hydrocarbon feed stream with catalyst to catalytically crack said hydrocarbon feed stream to provide a cracked stream; disengaging said catalyst from said cracked stream; fractionating said cracked stream into products including a slurry oil stream from a bottom of a main fractionation column; feeding said slurry oil stream to a slurry separator, wherein the slurry separator is fed directly from the bottom of the main fractionation column; generating a thin film of slurry oil on a wall of the slurry separator by rotating a blade held onto a shaft by spokes to wipe said slurry oil onto a wall of the slurry separator; separating said slurry oil stream into a recovered oil stream and a concentrated residue stream in said slurry separator. 2. The process of claim 1 further comprising generating centrifugal force by said rotating blade which maintains said slurry oil in contact with said heated inner wall of said slurry separator. 3. The process of claim 1 further comprising heating an inner wall of said separator to facilitate separation. 4. The process of claim 1 further comprising pulling a vacuum on said separator to facilitate separation. 5. The process of claim 1 further comprising withdrawing solids from said residue stream by a rotating augur. 6. The process of claim 3 wherein said blade has an outer edge that is spaced from said inner wall of said separator for generating a film by wiping said slurry oil stream onto said inner wall during rotation. 7. The process of claim 1 wherein said rotating blade occupies a middle section of said slurry separator and further comprising feeding said slurry oil to a first end of said slurry separator and withdrawing said concentrated residue stream from a second end of said slurry separator. 8. The process of claim 6 wherein said slurry separator comprises a double wall in the middle section of said slurry separator that comprises an annular chamber and further comprising feeding heating medium to said annular chamber at a first end of said slurry separator and withdrawing said heating medium from said second end of said slurry separator. 9. The process of claim 7 further comprising withdrawing a vaporized recovered oil from a first end of said slurry separator. 10. The process of claim 1 further comprising fractionating said cracked stream to produce a cycle oil stream in said main fractionation column and mixing said concentrated residue stream from said slurry separator with said cycle oil stream. 11. A process for catalytically cracking hydrocarbons comprising: feeding a hydrocarbon feed stream to a FCC reactor and contacting said hydrocarbon feed stream with catalyst to catalytically crack said hydrocarbon feed stream to provide a cracked stream; disengaging said catalyst from said cracked stream; fractionating said cracked stream into products including a slurry oil stream from a bottom of a main fractionation column; feeding said slurry oil stream to a slurry separator, wherein the slurry separator is fed directly from the bottom of the main fractionation column; rotating a blade to wipe said slurry oil onto a wall of the slurry separator to generate a thin film of slurry oil on a wall of the slurry separator; separating said slurry oil stream into a recovered oil stream and a concentrated residue stream in said slurry separator; and withdrawing solids from a bottom of the slurry separator. 12. The process of claim 11 further comprising heating an inner surface of said separator and pulling a vacuum on said separator to facilitate separation.
with blades or scrapers · CPC title
according to "fluidised-bed" technique (B01J8/20 takes precedence) · CPC title
with the aid of centrifugal force · CPC title
the fluidising gas being a reactant · CPC title
by two or more of a fractionation, separation or rectification step · CPC title
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