Patent US4664889A successfully refreshed from Google Patents.
US4664889A
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Apparatus for separating hydrocarbon products from catalyst particles
Assignee: Shell USA Inc
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Filing: 1985-11-08
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Granted: 1987-05-12
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Expires: 2005-11-08
Abstract
Abstract In a fluidized catalytic cracking apparatus a mixture of hydrocarbon products and hydrocarbon catalyst particles is removed from a reactor riser (1) and introduced into a cyclone separator (2), wherein in order to strip the catalyst particles, primary steam is injected into the cyclone separator (2), and wherein, for additional stripping the catalyst particles are introduced into a stripper assembly (3) comprising at least two interconnected stripper vessels (4, 5) into which secondary steam is introduced.
Inventors
- 👤 Wiecher D. E. Steenge
- 👤 Ringnerus P. van der Werf
- 👤 Jan Haringa
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 19:02
CPC Classifications
C; C10; C10G; C10G11/00; C10G11/14; C10G11/18; B; B01; B01J; B01J8/00; B01J8/005; B01J8/18; B01J8/24; B01J8/26
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
386 words
An apparatus for separating hydrocarbon products from hydrocarbon catalyst particles which comprises a cyclone separator and interconnecting stripper assembly as defined by: (a) said cyclone separator having means defining an upper and a lower portion, exterior walls, an inlet for introducing said hydrocarbon products and said hydrocarbon catalyst particles into said cyclone separator located at said upper portion, an upper outlet in said upper portion of said separator for removing said hydrocarbon products from said cyclone separator, a bottom outlet in said cyclone separator situated in the lower portion of said cyclone separator, said bottom outlet communicating with said stripper assembly, said bottom outlet suitable for passage of separated hydrocarbon catalysts particles therethrough, a vortex stabilizer to cause separation of said hydrocarbon products from said catalyst particles located within said lower portion as to define a first annular region within said cyclone separator, first primary stripping gas inlet means comprising a plurality of orifices arranged in said first annular region which communicated with a source of primary stripping gas to provide flow of said primary stripping gas in a direction concurrent with respect to flow of said hydrocarbon particles passing through said bottom cyclone separator outlet, means defining a second annular region within said upper portion of said cyclone separator and second primary stripping gas inlet means arranged in said second annular region and (b) said stripper assembly comprising an inlet for entry of hydrocarbon catalyst particles from said cyclone separator, a first outlet for removal of gases from said stripper assembly, a second outlet for removal of the catalyst particles, means defining at least two interconnecting horizontal stripping zones, said means comprising a plurality of upright partitions of relatively decreasing heights as said partitions are situated closer to said second outlet to provide that each preceding stripping zone in said stripper assembly bed contains a larger quantity of catalyst particles than contained in a next adjacent stripping zone, wherein the first of said at least two interconnecting horizontal stripping zones communicates with said bottom outlet of said cyclone separator and the last of said at least two stripping zones communicates with a regeneration zone by means of said second outlet, wherein each of said at least two stripping zones includes secondary stripping gas inlet means for introduction of secondary stripping gas into said stripper assembly.
Claim 2
Independent Claim
386 words
An apparatus for separating hydrocarbon products from hydrocarbon catalyst particles which comprises a cyclone separator and interconnecting stripper assembly as defined by: (a) said cyclone separator having means defining an upper and a lower portion, exterior walls, an inlet for introducing said hydrocarbon products and said hydrocarbon catalyst particles into said cyclone separator located at said upper portion, an upper outlet in said upper portion of said separator for removing said hydrocarbon products from said cyclone separator, a bottom outlet in said cyclone separator situated in the lower portion of said cyclone separator, said bottom outlet communicating with said stripper assembly, said bottom outlet suitable for passage of separated hydrocarbon catalysts particles therethrough, a vortex stabilizer to cause separation of said hydrocarbon products from said catalyst particles located within said lower portion as to define a first annular region within said cyclone separator, first primary stripping gas inlet means comprising a plurality of orifices arranged in said first annular region which communicated with a source of primary stripping gas to provide flow of said primary stripping gas in a direction concurrent with respect to flow of said hydrocarbon particles passing through said bottom cyclone separator outlet, means defining a second annular region within said upper portion of said cyclone separator and second primary stripping gas inlet means arranged in said second annular region and (b) said stripper assembly comprising an inlet for entry of hydrocarbon catalyst particles from said cyclone separator, a first outlet for removal of gases from said stripper assembly, a second outlet for removal of the catalyst particles, means defining at least two interconnecting horizontal stripping zones, said means comprising a plurality of upright partitions of relatively decreasing heights as said partitions are situated closer to said second outlet to provide that each preceding stripping zone in said stripper assembly bed contains a larger quantity of catalyst particles than contained in a next adjacent stripping zone, wherein the first of said at least two interconnecting horizontal stripping zones communicates with said bottom outlet of said cyclone separator and the last of said at least two stripping zones communicates with a regeneration zone by means of said second outlet, wherein each of said at least two stripping zones includes secondary stripping gas inlet means for introduction of secondary stripping gas into said stripper assembly.
Claim 3
Dependent Claim
27 words
The apparatus of claim 1 wherein said catalyst particles have a residence time of from 50 secs to not more than 500 secs in said stripper assembly.
Claim 4
Dependent Claim
19 words
The apparatus of claim 1 wherein said vortex stabilizer is centered in said lower portion of said cyclone separator.
Claim 5
Dependent Claim
35 words
The apparatus of claim 1 wherein said vortex stabilizer is centered coaxially near the lower end of said cyclone separator to create said vortex to cause separation between said hydrocarbon products and hydrocarbon catalyst particles.
Claim 6
Dependent Claim
18 words
The apparatus of claim 1 wherein said secondary stripping gas inlet means communicates with a source of steam.
Claim 7
Dependent Claim
22 words
The apparatus of claim 1 wherein primary stripping said secondary stripping gas inlet means communicates with a source of an inert gas.
Claim 8
Dependent Claim
25 words
The apparatus of claim 1 wherein said secondary stripping gas inlet means comprises a plurality of annularly situated gas nozzles communicating with said stripping zone.
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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) | 1990-05-11 | 1990-11-10 | 1991-05-12 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-05-11 | 1994-11-10 | 1995-05-12 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-05-11 | 1998-11-10 | 1999-05-12 | $7700.00 | Window Closed / Lapsed |