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US2544843A Expired / Lapsed US ⏱️ 0.0 years remaining

Treatment of solid hydrocarbonaceous material

Assignee: Universal Oil Products Co
•
Filing: 1948-01-28
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Granted: 1951-03-13
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Expires: 1968-01-28
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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.

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

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