US4239614A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Hydrocarbon conversion process with annular guard beds
Assignee: Honeywell UOP LLC
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Filing: 1978-12-11
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Granted: 1980-12-16
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Expires: 1998-12-11
Abstract
Abstract A hydrocarbon conversion process useful in hydroprocessing petroleum-based feedstocks. The feed stream enters the top of a reaction zone and is divided into a number of portions, each of which flows through a different annular guard bed. The feed stream enters the guard beds through both cylindrical sides and exits through the bottom of the guard beds. The feed stream is then passed through a lower and much larger catalyst bed.
Inventors
- 👤 Le Roi E. Hutchings
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 22:22
CPC Classifications
B; B01; B01J; B01J8/00; B01J8/02; B01J8/0242; B01J8/025; B01J8/04; B01J8/0446; B01J8/0476; B01J8/048; C; C10; C10G; C10G49/00; C10G49/002; B01J2208/00; B01J2208/02; B01J2208/021
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
221 words
A catalytic hydrocarbon conversion process to more efficiently prevent plugging of the inlet surface of the catalyst bed which comprises the steps of: (a) passing a feed stream comprising hydrogen and hydrocarbonaceous reactants into an upper end of a reaction zone maintained at hydrocarbon conversion conditions; (b) dividing the feed stream into a number of portions and passing each portion through one of a plurality of separated annular beds of particulate material located within the upper one-third of the reaction zone, with the annular beds of particulate material being radially spaced apart, concentric about the vertical major axis of the reaction zone and located at substantially the same vertical elevation within the reaction zone, and with the flow of the feed stream through each of the annular beds of particulate material being inward through both cylindrical sides of at lease an upper portion of the annular bed and outward through a lower portion of the annular bed; (c) recombining the portions of the feed stream at a point below the annular beds of particulate material; (d) passing the feed stream downward through a cylindrical bed of catalyst which is at least four times greater in volume than the particulate material contained within the annular beds; and, (e) removing a reaction zone effluent stream from a lower portion of the reaction zone.
Claim 2
Dependent Claim
221 words
A catalytic hydrocarbon conversion process to more efficiently prevent plugging of the inlet surface of the catalyst bed which comprises the steps of: (a) passing a feed stream comprising hydrogen and hydrocarbonaceous reactants into an upper end of a reaction zone maintained at hydrocarbon conversion conditions; (b) dividing the feed stream into a number of portions and passing each portion through one of a plurality of separated annular beds of particulate material located within the upper one-third of the reaction zone, with the annular beds of particulate material being radially spaced apart, concentric about the vertical major axis of the reaction zone and located at substantially the same vertical elevation within the reaction zone, and with the flow of the feed stream through each of the annular beds of particulate material being inward through both cylindrical sides of at lease an upper portion of the annular bed and outward through a lower portion of the annular bed; (c) recombining the portions of the feed stream at a point below the annular beds of particulate material; (d) passing the feed stream downward through a cylindrical bed of catalyst which is at least four times greater in volume than the particulate material contained within the annular beds; and, (e) removing a reaction zone effluent stream from a lower portion of the reaction zone.
Claim 3
Dependent Claim
22 words
The process of claim 1 further characterized in that the hydrocarbonaceous reactants have a 90 percent boiling point greater than 380° F.
Claim 4
Dependent Claim
35 words
The process of claim 1 further characterized in that the catalyst comprises a Group VI-A or Group VIII metal component and in that there is a net chemical consumption of hydrogen within the reaction zone.
Claim 5
Dependent Claim
30 words
The process of claim 3 further characterized in that the particulate material in the annular beds is catalyst of the same composition as that in the cylindrical bed of catalyst.
References Cited (Backward Citations)
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US3958952A
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US3996015A
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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) | 1983-12-16 | 1984-06-16 | 1984-12-16 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1987-12-16 | 1988-06-16 | 1988-12-16 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1991-12-16 | 1992-06-16 | 1992-12-16 | $7700.00 | Window Closed / Lapsed |