Patent US4605491A successfully refreshed from Google Patents.
US4605491A
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US
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FCC catalyst stripping method
Assignee: Mobil Oil AS
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Filing: 1984-07-18
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Granted: 1986-08-12
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Expires: 2004-07-18
Abstract
Abstract A method and apparatus for improving the stripping of hydrocarbons from catalyst particles in a fluidized catalytic cracking (FCC) unit. A stripper vessel has catalyst particles entering at one end and stripped catalyst particles exiting at another end. While passing through the stripper, the catalyst particles are exposed to a stripping gas, in a preferred embodiment steam, at each stage. A baffle and conduit system is provided, such that after exposure to only a portion of catalyst contained above the steam injection location in the stripper, the stripping gas and any stripped hydrocarbons are removed from any further substantial catalyst contact. The short contact time (SCT) stripper, in other embodiments, can be combined with one or more of a riser conversion zone deflector, a stripper mount in or adjacent the exhaust barrel of a separator, and/or a catalyst seal pot, all serving to reduce "residence" time of hydrocarbons with catalyst particles.
Inventors
- 👤 James H. Haddad
- 👤 Hartley Owen
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 19:20
CPC Classifications
C; C10; C10G; C10G11/00; C10G11/14; C10G11/18; B; B01; B01J; B01J8/00; B01J8/005; B01J8/0055; B01J8/18; B01J8/24; B01J8/38; B01J8/384; B01J8/386
Claims Analysis
Total Claims: 13
Claim 1
Independent Claim
148 words
A method of stripping hydrocarbons from separated catalyst in a fluid catalytic cracking process, said method comprising the steps of: passing said separated catalyst through a stripper vessel having an entrance, a catalyst exit and a stripped hydrocarbon exit: causing said separated catalyst to follow a circuitous path concentrically around a riser conversion zone while flowing from said entrance through said stripper vessel to said catalyst exit; injecting a stripping gas at a plurality of stages such that stripping gas injected at one stage is exposed to only a portion of said separated catalyst above the stripping gas injecting location and moves through said portion in a direction having a net radial component and is mixed with stripping gas from another stage when passing through said stripped hydrocarbon exit; and passing said stripping gas and hydrocarbons strippe d from said separated catalyst directly to said stripped hydrocarbon exit.
Claim 2
Independent Claim
148 words
A method of stripping hydrocarbons from separated catalyst in a fluid catalytic cracking process, said method comprising the steps of: passing said separated catalyst through a stripper vessel having an entrance, a catalyst exit and a stripped hydrocarbon exit: causing said separated catalyst to follow a circuitous path concentrically around a riser conversion zone while flowing from said entrance through said stripper vessel to said catalyst exit; injecting a stripping gas at a plurality of stages such that stripping gas injected at one stage is exposed to only a portion of said separated catalyst above the stripping gas injecting location and moves through said portion in a direction having a net radial component and is mixed with stripping gas from another stage when passing through said stripped hydrocarbon exit; and passing said stripping gas and hydrocarbons strippe d from said separated catalyst directly to said stripped hydrocarbon exit.
Claim 3
Independent Claim
176 words
A method of stripping hydrocarbons from separated catalyst in a fluid catalytic cracking process, said method comprising the steps of: passing said separated catalyst through a stripper vessel having an entrance, a catalyst exit and a stripped hydrocarbon exit; causing said separated catalyst to follow a circuitous path from said entrance through said stripper vessel to said catalyst exit; injecting a stripping gas so that it contacts with only a portion of said separated catalyst that is above the stripping gas injecting location and moves through said portion in a direction having a net radial component and located between said location and stripped hydrocarbon exit; and passing said stripping gas and hydrocarbons stripped from said separated catalyst directly to said stripped hydrocarbon exit, wherein said injecting step comprises injecting said stripping gas at a plurality of stages such that said stripping gas at one stage is exposed to only a portion of said separated catalyst and is not exposed to stripping gas from another stage in said stripper vessel when passing through said stripped hydrocarbon exit.
Claim 4
Independent Claim
176 words
A method of stripping hydrocarbons from separated catalyst in a fluid catalytic cracking process, said method comprising the steps of: passing said separated catalyst through a stripper vessel having an entrance, a catalyst exit and a stripped hydrocarbon exit; causing said separated catalyst to follow a circuitous path from said entrance through said stripper vessel to said catalyst exit; injecting a stripping gas so that it contacts with only a portion of said separated catalyst that is above the stripping gas injecting location and moves through said portion in a direction having a net radial component and located between said location and stripped hydrocarbon exit; and passing said stripping gas and hydrocarbons stripped from said separated catalyst directly to said stripped hydrocarbon exit, wherein said injecting step comprises injecting said stripping gas at a plurality of stages such that said stripping gas at one stage is exposed to only a portion of said separated catalyst and is not exposed to stripping gas from another stage in said stripper vessel when passing through said stripped hydrocarbon exit.
Claim 5
Dependent Claim
39 words
The method according to claim 2, wherein said causing step further includes the step of causing said catalyst to flow concentrically around a riser conversion zone while flowing from the entrance to the catalyst exit through said stripper vessel.
Claim 6
Independent Claim
65 words
The method according to one of claims 1, 2 or 3, wherein after said passing steps there is further provided the additional step of passing said separated catalyst through a dipleg into a catalyst seal pot including at least one drain so as to permit between 10 and 90% of catalyst flowing through ssaid stripper to flow out of said seal pot through said drain.
Claim 7
Independent Claim
190 words
A method of stripping hydrocarbons from separated catalyst in a fluid catalytic cracking process, said method comprising the steps of: passing a mixture, as a suspension, of hydrocarbon feed and a catalyst through a riser conversion zone contained within a reactor vessel and cracking said hydrocarbon feed in the riser conversion zone; passing said mixture through a deflection zone in which said catalyst is physically deflected towards an exit of said deflection zone; passing said mixture from said deflection zone exit to a separation zone; separating at least a portion of said catalyst from the mixture in said separation zone; passing said separated catalyst through a stripper vessel having an entrance, a catalyst exit and a stripped hydrocarbon exit; causing said separated catalyst to follow a circuitous path from said entrance through said stripper vessel to said catalyst exit; injecting a stripping gas so that it contacts with only a portion of said separated catalyst that is above the stripping gas injecting location and located between said location and stripped hydrocarbon exit; and passing said stripping gas and hydrocarbons stripped from said separated catalyst directly to said stripped hydrocarbon exit.
Claim 8
Independent Claim
190 words
A method of stripping hydrocarbons from separated catalyst in a fluid catalytic cracking process, said method comprising the steps of: passing a mixture, as a suspension, of hydrocarbon feed and a catalyst through a riser conversion zone contained within a reactor vessel and cracking said hydrocarbon feed in the riser conversion zone; passing said mixture through a deflection zone in which said catalyst is physically deflected towards an exit of said deflection zone; passing said mixture from said deflection zone exit to a separation zone; separating at least a portion of said catalyst from the mixture in said separation zone; passing said separated catalyst through a stripper vessel having an entrance, a catalyst exit and a stripped hydrocarbon exit; causing said separated catalyst to follow a circuitous path from said entrance through said stripper vessel to said catalyst exit; injecting a stripping gas so that it contacts with only a portion of said separated catalyst that is above the stripping gas injecting location and located between said location and stripped hydrocarbon exit; and passing said stripping gas and hydrocarbons stripped from said separated catalyst directly to said stripped hydrocarbon exit.
Claim 9
Independent Claim
150 words
A method of stripping hydrocarbons from separated catalyst in a fluid catalytic cracking process, said method comprising the steps of: separating a cracked hydrocarbon feed in a separator into a gaseous effluent and a separated catalyst; immediately passing said separated catalyst from said separator into an entrance of a stripper vessel having a catalyst exit and a stripped hydrocarbon exit; passing said separated catalyst through a stripper vessel having an entrance, a catalyst exit and a stripped hydrocarbon exit; causing said separated catalyst to follow a circuitous path from said entrance through said stripper vessel to said catalyst exit; injecting a stripping gas so that it contacts with only a portion of said separated catalyst that is above the stripping gas injecting location and located between said location and stripped hydrocarbon exit; and passing said stripping gas and hydrocarbons stripped from said separated catalyst directly to said stripped hydrocarbon exit.
Claim 10
Independent Claim
150 words
A method of stripping hydrocarbons from separated catalyst in a fluid catalytic cracking process, said method comprising the steps of: separating a cracked hydrocarbon feed in a separator into a gaseous effluent and a separated catalyst; immediately passing said separated catalyst from said separator into an entrance of a stripper vessel having a catalyst exit and a stripped hydrocarbon exit; passing said separated catalyst through a stripper vessel having an entrance, a catalyst exit and a stripped hydrocarbon exit; causing said separated catalyst to follow a circuitous path from said entrance through said stripper vessel to said catalyst exit; injecting a stripping gas so that it contacts with only a portion of said separated catalyst that is above the stripping gas injecting location and located between said location and stripped hydrocarbon exit; and passing said stripping gas and hydrocarbons stripped from said separated catalyst directly to said stripped hydrocarbon exit.
Claim 11
Independent Claim
146 words
A method of stripping hydrocarbons from separated catalyst in a fluid catalytic cracking process, said method comprising the steps of: passing said separated catalyst through a stripper vessel having an entrance, a catalyst exit and a stripped hydrocarbon exit; causing said separated catalyst to follow a circuitous path from said entrance through said stripper vessel to said catalyst exit; injecting a stripping gas so that it contacts with only a portion of said separated catalyst that is above the stripping gas injecting location and located between said location and stripped hydrocarbon exit; passing said stripping gas and hydrocarbons stripped from said separated catalyst directly to said stripped hydrocarbon exit; and passing said separated catalyst through a dipleg into a catalyst seal pot including at least one drain so as to permit between 10 and 90% of catalyst flowing through said stripper to flow through said drain.
Claim 12
Independent Claim
146 words
A method of stripping hydrocarbons from separated catalyst in a fluid catalytic cracking process, said method comprising the steps of: passing said separated catalyst through a stripper vessel having an entrance, a catalyst exit and a stripped hydrocarbon exit; causing said separated catalyst to follow a circuitous path from said entrance through said stripper vessel to said catalyst exit; injecting a stripping gas so that it contacts with only a portion of said separated catalyst that is above the stripping gas injecting location and located between said location and stripped hydrocarbon exit; passing said stripping gas and hydrocarbons stripped from said separated catalyst directly to said stripped hydrocarbon exit; and passing said separated catalyst through a dipleg into a catalyst seal pot including at least one drain so as to permit between 10 and 90% of catalyst flowing through said stripper to flow through said drain.
Claim 13
Independent Claim
26 words
The method according to one of claims 1, 2, 3, 4, 5, 6 or 7, wherein said injecting step comprises injecting steam as said stripping gas.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1989-08-11 | 1990-02-10 | 1990-08-12 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1993-08-11 | 1994-02-10 | 1994-08-12 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1997-08-11 | 1998-02-10 | 1998-08-12 | $7700.00 | Window Closed / Lapsed |