US4292171A
Expired / Lapsed
US
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Magnetically stabilized, fluidized beds
Assignee: ExxonMobil Technology and Engineering Co
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Filing: 1980-03-19
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Granted: 1981-09-29
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Expires: 2000-03-19
Abstract
Abstract A hydrocarbon conversion process wherein a hydrocarbon feedstock is contacted with a magnetically stabilized fluid bed of particulate solids comprising a mixture of separate, discrete (a) magnetizable substantially non-catalytic particles, and (b) non-magnetizable catalytic particles. The particulate solids mixture is withdrawn from the magnetically stabilized, fluidized bed and separated into magnetizable, substantially non-catalytic particles and non-magnetizable catalyst particles. The non-magnetizable catalytic particles are thereafter regenerated and returned to the hydrocarbon conversion zone. The separated magnetizable, substantially non-catalytic particles are subjected to heat transfer prior to their return to the conversion zone.
Inventors
- 👤 Francis X. Mayer
- 👤 William F. Arey, Jr.
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 12:57
CPC Classifications
C; C10; C10G; C10G11/00; C10G11/14; C10G11/18; B; B01; B01J; B01J8/00; B01J8/18; B01J8/24; B01J8/42
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
163 words
In a hydrocarbon conversion process wherein fluidizable particulate catalyst solids are circulated between a fluidized bed reaction zone in which said particulate catalyst solids are contacted with a hydrocarbon feedstock resulting in the deposition of coke on said catalyst solids and a fluidized bed regeneration zone in which the catalyst particles having coke deposited thereon are contacted with an oxygen-containing gas to remove said coke by combustion, the improvement which comprises (a) introducing into said reaction zone particulate solids having ferromagnetic properties so that said hydrocarbon feedstock is contacted with a particulate solids mixture containing a plurality of separate, discrete ( 1) magnetizable substantially non-catalytic particles, and (2) non-magnetizable catalytic particles; (b) applying a magnetic field to said reaction zone to form a magnetically stabilized fluid bed in said reaction zone; (c) withdrawing said particulate solids mixture from the reaction zone; (d) separating said magnetizable substantially non-catalytic particles from said non-magnetizable catalytic particles; and introducing said non-magnetizable catalytic particles into said regeneration zone.
Claim 2
Dependent Claim
163 words
In a hydrocarbon conversion process wherein fluidizable particulate catalyst solids are circulated between a fluidized bed reaction zone in which said particulate catalyst solids are contacted with a hydrocarbon feedstock resulting in the deposition of coke on said catalyst solids and a fluidized bed regeneration zone in which the catalyst particles having coke deposited thereon are contacted with an oxygen-containing gas to remove said coke by combustion, the improvement which comprises (a) introducing into said reaction zone particulate solids having ferromagnetic properties so that said hydrocarbon feedstock is contacted with a particulate solids mixture containing a plurality of separate, discrete ( 1) magnetizable substantially non-catalytic particles, and (2) non-magnetizable catalytic particles; (b) applying a magnetic field to said reaction zone to form a magnetically stabilized fluid bed in said reaction zone; (c) withdrawing said particulate solids mixture from the reaction zone; (d) separating said magnetizable substantially non-catalytic particles from said non-magnetizable catalytic particles; and introducing said non-magnetizable catalytic particles into said regeneration zone.
Claim 3
Dependent Claim
20 words
In the hydrocarbon conversion process of claim 1, the improvement comprising circulating said magnetizable particles to a heat exchange means.
Claim 4
Dependent Claim
41 words
In the hydrocarbon conversion process of claim 2, the improvement comprising contacting said magnetizable solids with the combustion gases from said regeneration zone to heat said magnetizable solids and thereafter introducing said heated magnetizable solids into said fluidized bed reaction zone.
Claim 5
Dependent Claim
29 words
In the hydrocarbon conversion process of claim 2, the improvement wherein said magnetic field is uniform and oriented substantially axially to the flow of fluid in said reaction zone.
Claim 6
Dependent Claim
37 words
In the hydrocarbon conversion process of claim 4, the improvement wherein said particulate solids mixture comprises 5 to 50 vol. % of the magnetizable non-catalytic particles and 50 to 95 vol. % of the non-magnetizable catalytic particles.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1984-09-28 | 1985-03-30 | 1985-09-29 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-09-28 | 1989-03-30 | 1989-09-29 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-09-28 | 1993-03-30 | 1993-09-29 | $7700.00 | Window Closed / Lapsed |