US2889267A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for cracking oil
Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1953-12-31
•
Granted: 1959-06-02
•
Expires: 1973-12-31
Abstract
No abstract record available.
Inventors
- 👤 Frank T Barr
- 👤 Harvey E W Burnside
- 👤 James W Brown
- 👤 Charles E Jahnig
- 👤 Homer Z Martin
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 05:12
CPC Classifications
C; C10; C10G; C10G9/00; C10G9/28; C10G9/32
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
162 words
THE PROCESS OF COKING A HEAVY HYDROCARBON OIL, WHICH COMPRISES ESTABLISHING A FLUIDIZED BED OF FINELY DIVIDED PREHEATED SOLID PARTICLES IN A REACTION ZONE, DISTRIBUTING THE OIL AS A FILM ON SAID SOLID PARTICLES TO CRACK AND VAPROIZE IT AND FROM A CARBONACEOUS COATING ON THE PARTICLES, CONTINUOUSLY REMOVING A STREAM OF COATED PARTICULATE SOLIDS AND PASSING THEM IN DISPERSE PHASE CONTINUOUSLY UPWARD THROUGH A TRANSFER LINE HEATER AT SUFFICIENT VELOCITY TO KEEP SUBSTANTIALLY ALL THE PARTICLES ENTRAINED IN THE FORM OF A DISPERSE SOLIDS-GAS STREAM, PASSING A COMBUSTION-SUPPORTING GAS WITH SAID PARTICLES THROUGH THE HEATER TO BURN THE CARBONACEOUS COATING MATERIAL AND TO PRODUCE THE SIZE OF THE PARTICLES AND REHEAT THEM, ROUGHLY SEPARATING THE EFFUENT STREAM OF HEATED SOLIDS LEAVING THE TRANSFER LINE HEATER INTO COARSE AND FINIC PARTICLES, RECYCLING THE HOT COARSE PARTICLES DIRECTLY TO THE INLET OF THE HEATER TO MAINTAIN HIGH HEATER TEMPERATURE, AND RETURNING THE HOT FINE PARTICLES TO THE FLUIDIZED BED IN THE REACTION ZONE.
Claim 2
Dependent Claim
162 words
THE PROCESS OF COKING A HEAVY HYDROCARBON OIL, WHICH COMPRISES ESTABLISHING A FLUIDIZED BED OF FINELY DIVIDED PREHEATED SOLID PARTICLES IN A REACTION ZONE, DISTRIBUTING THE OIL AS A FILM ON SAID SOLID PARTICLES TO CRACK AND VAPROIZE IT AND FROM A CARBONACEOUS COATING ON THE PARTICLES, CONTINUOUSLY REMOVING A STREAM OF COATED PARTICULATE SOLIDS AND PASSING THEM IN DISPERSE PHASE CONTINUOUSLY UPWARD THROUGH A TRANSFER LINE HEATER AT SUFFICIENT VELOCITY TO KEEP SUBSTANTIALLY ALL THE PARTICLES ENTRAINED IN THE FORM OF A DISPERSE SOLIDS-GAS STREAM, PASSING A COMBUSTION-SUPPORTING GAS WITH SAID PARTICLES THROUGH THE HEATER TO BURN THE CARBONACEOUS COATING MATERIAL AND TO PRODUCE THE SIZE OF THE PARTICLES AND REHEAT THEM, ROUGHLY SEPARATING THE EFFUENT STREAM OF HEATED SOLIDS LEAVING THE TRANSFER LINE HEATER INTO COARSE AND FINIC PARTICLES, RECYCLING THE HOT COARSE PARTICLES DIRECTLY TO THE INLET OF THE HEATER TO MAINTAIN HIGH HEATER TEMPERATURE, AND RETURNING THE HOT FINE PARTICLES TO THE FLUIDIZED BED IN THE REACTION ZONE.
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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) | 1962-06-01 | 1962-12-01 | 1963-06-02 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1966-06-01 | 1966-12-01 | 1967-06-02 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1970-06-01 | 1970-12-01 | 1971-06-02 | $7700.00 | Window Closed / Lapsed |