US3962070A
Expired / Lapsed
US
⏱️ 0.0 years remaining
H-coal process: slurry oil recycle system
Assignee: HRI Inc
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Filing: 1974-01-14
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Granted: 1976-06-08
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Expires: 1994-01-14
Abstract
Abstract In the hydrogenation of particulate coal in an ebullated bed reactor to produce hydrocarbon products, the improvement which comprises removing the coarser unreacted particulate from the recycled residiuum stream from the reactor by a liquid cyclone separation, recycling the overhead stream from said cyclone separation to the reaction zone, removing finer particulate solids from an additional liquid residiuum stream and also providing a net filtrate stream which is distilled to produce hydrocarbon vapor and liquid streams and combining said liquid stream with liquid resulting from condensation and fractionation of overhead vapor from the reactor to produce a synthetic crude oil.
Inventors
- 👤 Harold H. Stotler
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 14:49
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/04; C10G1/045; C10G1/08; C10G1/083
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
127 words
In a process for the hydrogenation of coal wherein particulate coal is admixed with a liquid hydrocarbon to form a coal-oil slurry which is passed with hydrogen through a reaction zone under hydrogenation temperature and pressure conditions and the coal is hydrogenated to produce hydrocarbon products including a liquid residuum having unconverted processed solids contained therein and wherein the reactor liquid residuum concentration is maximized to reduce the yield of liquid residuum by recycling to the reaction zone a portion of said liquid residuum in the coal-oil slurry, and wherein the solids concentration in the reactor liquid is maintained below 20 weight percent, the improvement which comprises: 1. removing the coarser particulate solids from at least part of the recycled residuum stream by liquid cyclone separation; 2.
Claim 2
Dependent Claim
127 words
In a process for the hydrogenation of coal wherein particulate coal is admixed with a liquid hydrocarbon to form a coal-oil slurry which is passed with hydrogen through a reaction zone under hydrogenation temperature and pressure conditions and the coal is hydrogenated to produce hydrocarbon products including a liquid residuum having unconverted processed solids contained therein and wherein the reactor liquid residuum concentration is maximized to reduce the yield of liquid residuum by recycling to the reaction zone a portion of said liquid residuum in the coal-oil slurry, and wherein the solids concentration in the reactor liquid is maintained below 20 weight percent, the improvement which comprises: 1. removing the coarser particulate solids from at least part of the recycled residuum stream by liquid cyclone separation; 2.
Claim 3
Dependent Claim
80 words
recycling the overhead stream from said liquid cyclone separation step to the reaction zone; 3. removing by filtering finer particulate solids from an additional liquid residuum stream recycled to the reaction zone and also providing a net filtrate liquid stream; 4. subjecting the net filtrate liquid to a distillation step to produce hydrocarbon vapor and liquid streams; and 5. combining the liquid from said distillation with a liquid resulting from condensation and fractionation of the overhead vapor from the reaction
Claim 4
Dependent Claim
80 words
recycling the overhead stream from said liquid cyclone separation step to the reaction zone; 3. removing by filtering finer particulate solids from an additional liquid residuum stream recycled to the reaction zone and also providing a net filtrate liquid stream; 4. subjecting the net filtrate liquid to a distillation step to produce hydrocarbon vapor and liquid streams; and 5. combining the liquid from said distillation with a liquid resulting from condensation and fractionation of the overhead vapor from the reaction
Claim 5
Dependent Claim
60 words
zone to produce a synthetic crude oil. 2. A process as claimed in claim 1 wherein the portion of solids removed by liquid cyclone has a particle size greater than about 15 microns and wherein the portion of solids removed by filtering has a particle size less than about 15 microns and the filtration is accomplished by a rotary filter.
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) | 1979-06-08 | 1979-12-08 | 1980-06-08 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-06-08 | 1983-12-08 | 1984-06-08 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-06-08 | 1987-12-08 | 1988-06-08 | $7700.00 | Window Closed / Lapsed |