US2544843A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Treatment of solid hydrocarbonaceous material
Assignee: Universal Oil Products Co
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Filing: 1948-01-28
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Granted: 1951-03-13
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Expires: 1968-01-28
Abstract
No abstract record available.
Inventors
- 👤 Frederick A W Leffer
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 00:10
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/02; C10B; C10B49/00; C10B49/02; C10B49/04; C10B49/06; Y; Y10; Y10S; Y10S208/00; Y10S208/952; Y10S48/00; Y10S48/04
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
300 words
A PROCESS FOR THE TREATMENT OF SOLID HYDROCARBONACEOUS MATERIAL WHICH COMPRISES CONTINUQUSLY SUPPLYING A STREAM OF FINELY DIVIDED SOLID HYDROCARBONACEOUS MATERIAL OF RELATIVELY HIGH ASH CONTENT OF A CONFINED DISTILLING ZONE AND PASSING IT IN A DENSE MASS DOWNWARDLY THROUGH SAID ZONE IN DIRECT CONTACT WITH A GASIFORM HEATSUPPLYING MEDIUM COMPRISING SUPERHEATED STREAM AT DISTILLING TEMPERATURE, WITHDRAWING A STREAM OF HOT FINELY DIVIDED DISTILLATION RESIDUE FROM SAID DISTILLING ZONE AND COMMINGLING THE SAME WITH A HOT GASEOUS FLUIDIZING MEDIUM, TRANSFERRING SAID RESIDUE STREAM FLUIDIZED IN SAID GASEOUS FLUIDIZING MEDIUM AND SUBSTANTIALLY WITHOUT INTENTIONAL COOLING TO A SEPARATE CONFINED COMBUSTION ZONE AND THEREIN BURNING SUBSTANTIALLY ALL UNDISTILLED COMBUSTIBLE MATERIAL FROM SAID DISTILLATION RESIDUE WHILE CONDUCTING THE LATTER IN A DENSE MASS DOWNWARDLY IN DIRECT CONTACT WITH A FREE OXYGENCONTAINING GAS, INTRODUCING SAID SUPERHEATED STREAM TO THE LOWER PORTION OF SAID DISTILLING ZONE AND SAID OXYGEN-CONTAINING GAS TO THE LOWER PORTION OF SAID COMBUSTION ZONE EACH AT A RATE AT WHICH THE SOLID MATERIAL IN THE DENSE MASS WITHIN EACH OF SAID ZONES IS MAINTAINED IN FINELY SUBDIVIDED AND FREELY FLOWING STATE, WITHDRAWING A VAPOROUS STREAM OF DISTILLATION PRODUCTS AND GASIFORM HEAT-SUPPLYING MEDIUM FROM THE UPPER PORTION OF SAID DISTILLING ZONE WHILE INDEPENDENTLY THEREOF DISCHARGING HOT COMBUSTION GASES FROM THE UPPER PORTION OF SAID SEPARATE COMBUSTION ZONE, PASSING A STREAM OF HIGHLY HEATED NONCOMBUSTIBLE RESIDUE FROM SAID COMBUSTION ZONE SUBSTANTIALLY WITHOUT INTENTIONAL COOLING TO A SEPARATE AND CONFINED HEATING ZONE AND THEREIN COOLING SAID NON-COMBUSTIBLE RESIDUE BY DIRECT CONTACT WITH WATER IN AN AMOUNT IN EXCESS OF THAT REQUIRED TO GENERATE SAID SUPERHEATED STEAM, CONTINUOUSLY FEEDING A STREAM OF THE RESULTANT SUPERHEATED STREAM FROM SAID HEATING ZONE DIRECTLY TO SAID DISTILLING ZONE, AND DISCHARGING A SLURRY OF FINELY DIVIDED SOLID RESIDUE AND WATER A A SUBSTANTIALLY LOWERED TEMPERATURE FROM SAID HEATING ZONE.
Claim 2
Dependent Claim
300 words
A PROCESS FOR THE TREATMENT OF SOLID HYDROCARBONACEOUS MATERIAL WHICH COMPRISES CONTINUQUSLY SUPPLYING A STREAM OF FINELY DIVIDED SOLID HYDROCARBONACEOUS MATERIAL OF RELATIVELY HIGH ASH CONTENT OF A CONFINED DISTILLING ZONE AND PASSING IT IN A DENSE MASS DOWNWARDLY THROUGH SAID ZONE IN DIRECT CONTACT WITH A GASIFORM HEATSUPPLYING MEDIUM COMPRISING SUPERHEATED STREAM AT DISTILLING TEMPERATURE, WITHDRAWING A STREAM OF HOT FINELY DIVIDED DISTILLATION RESIDUE FROM SAID DISTILLING ZONE AND COMMINGLING THE SAME WITH A HOT GASEOUS FLUIDIZING MEDIUM, TRANSFERRING SAID RESIDUE STREAM FLUIDIZED IN SAID GASEOUS FLUIDIZING MEDIUM AND SUBSTANTIALLY WITHOUT INTENTIONAL COOLING TO A SEPARATE CONFINED COMBUSTION ZONE AND THEREIN BURNING SUBSTANTIALLY ALL UNDISTILLED COMBUSTIBLE MATERIAL FROM SAID DISTILLATION RESIDUE WHILE CONDUCTING THE LATTER IN A DENSE MASS DOWNWARDLY IN DIRECT CONTACT WITH A FREE OXYGENCONTAINING GAS, INTRODUCING SAID SUPERHEATED STREAM TO THE LOWER PORTION OF SAID DISTILLING ZONE AND SAID OXYGEN-CONTAINING GAS TO THE LOWER PORTION OF SAID COMBUSTION ZONE EACH AT A RATE AT WHICH THE SOLID MATERIAL IN THE DENSE MASS WITHIN EACH OF SAID ZONES IS MAINTAINED IN FINELY SUBDIVIDED AND FREELY FLOWING STATE, WITHDRAWING A VAPOROUS STREAM OF DISTILLATION PRODUCTS AND GASIFORM HEAT-SUPPLYING MEDIUM FROM THE UPPER PORTION OF SAID DISTILLING ZONE WHILE INDEPENDENTLY THEREOF DISCHARGING HOT COMBUSTION GASES FROM THE UPPER PORTION OF SAID SEPARATE COMBUSTION ZONE, PASSING A STREAM OF HIGHLY HEATED NONCOMBUSTIBLE RESIDUE FROM SAID COMBUSTION ZONE SUBSTANTIALLY WITHOUT INTENTIONAL COOLING TO A SEPARATE AND CONFINED HEATING ZONE AND THEREIN COOLING SAID NON-COMBUSTIBLE RESIDUE BY DIRECT CONTACT WITH WATER IN AN AMOUNT IN EXCESS OF THAT REQUIRED TO GENERATE SAID SUPERHEATED STEAM, CONTINUOUSLY FEEDING A STREAM OF THE RESULTANT SUPERHEATED STREAM FROM SAID HEATING ZONE DIRECTLY TO SAID DISTILLING ZONE, AND DISCHARGING A SLURRY OF FINELY DIVIDED SOLID RESIDUE AND WATER A A SUBSTANTIALLY LOWERED TEMPERATURE FROM SAID HEATING ZONE.
References Cited (Backward Citations)
US1524784A
Cited
US1509667A
Cited
US1901169A
Cited
US1836051A
Cited
GB283259A
Cited
US1950558A
Cited
GB286404A
Cited
US1984380A
Cited
US1983943A
Cited
US1953040A
Cited
GB419444A
Cited
US2167099A
Cited
GB484050A
Cited
GB487983A
Cited
US2366057A
Cited
US2414586A
Cited
US2432135A
Cited
US2409797A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1954-03-12 | 1954-09-11 | 1955-03-13 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1958-03-12 | 1958-09-11 | 1959-03-13 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1962-03-12 | 1962-09-11 | 1963-03-13 | $7700.00 | Window Closed / Lapsed |