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US2849384A Expired / Lapsed US ⏱️ 0.0 years remaining

Fluid coking process

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1954-06-30
•
Granted: 1958-08-26
•
Expires: 1974-06-30
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Abstract

No abstract record available.

Inventors

  • 👤 Jr Alexis Voorhies
  • 👤 Edward W S Nicholson

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-25 17:27
CPC Classifications
B; B01; B01J; B01J8/00; B01J8/18; B01J8/24; B01J8/38; B01J8/384; B01J8/386; C; C10; C10B; C10B55/00; C10B55/02; C10B55/04; C10B55/08; C10B55/10; C10G; C10G9/00; C10G9/28; C10G9/32

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 350 words
IN A PROCESS FOR COKING A HEAVY HYDROCARBON OIL BY CONTACTING THE OIL COKING CHARGE STOCK AT A TEMPERATURE IN THE RANGE OF 900* TO 1600*F. WITH A BODY OF COKE PARTICLES MAINTAINED IN THE FORM OF A DENSE, TURBULENT, FLUIDIZED BED IN A REACTION ZONE, REMOVING PRODUCT VAPORS FROM THE REACTION ZONE, CIRCULATING THE COKE PARTICLES THROUGH AN EXTRANEOUS HEATING ZONE WHEREIN THE PARTICLES ARE HEATED AND BACK TO THE REACTION ZONE TO SUPPLY HEAT THERETO, THE IMPROVEMENT WHICH COMPRISES THE STEPS OF INJECTING THE COKE PARTICLES FROM THE HEATING ZONE UPWARDLY AT A VELOCITY IN THE RANGE OF 0.1 TO 10 FT./SEC. INTO AN UPWARDLY DIVERGING INTERNAL PASSAGEWAY OF RESTRICTED CROSS SECTION WITHIN THE DENSE, TURBULENT, FLUIDIZED BED OF COKE PARTICLES, THE PASSAGEWAY HAVING A TOTAL INCLUDED ANGLE IN THE RANGE OF 3 TO 8*, THE PORTION OF THE FLUID BED WITHIN THE PASSAGEWAY CONTAINING 20 TO 50% OF THE TOTAL DENSE, TURBULENT, FLUIDIZED BED VOLUME AND HAVING A DENSITY OF 30 TO 45 LBS./CU. FT.; INJECTING THE OIL CHARGE STOCK INTO A LOWER PORTION OF SAID PASSAGEWAY WHEREBY THE OIL UNDERGOES CRACKING YIELDING VAPOROUS CONVERSION PRODUCTS; CIRCULATING THE COKE PARTICLES FROM THE UPPER PORTION OF THE PASSAGEWAY DOWNWARDLY AT A VELOCITY IN THE RANGE OF 0.02 TO 6 FT./SEC. THROUGH AN ANNULAR PATH OF INCREASING CROSS SECTIONAL AREA DEFINED BY SAID PASSAGEWAY AND THE CONFINES OF THE REACTION ZONE TO THE LOWER PORTION OF THE PASSAGEWAY, THE FLUIDIZED BED WITHIN THE PATH HAVING A DENSITY OF 40 TO 50 LBS./CU. FT. AND GREATER THAN THAT IN THE PASSAGEWAY; INTRODUCING AN INERT STRIPPING GAS INTO THE LOWER PORTION OF SAID PATH; PASSING THE STRIPPING GAS UPWARDLY THROUGH THE PATH, THE STRIPPING GAS HAVING AN INCREASING VELOCITY AS IT PROCEEDS UPWARDLY THROUGH SAID PATH; WITHDRAWING AT A VELOCITY IN THE RANGE OF 3 TO 10FT./SEC. AND RAPIDLY COOLING THE VAPOROUS CONVERSION PRODUCTS FROM THE UPPER PORTION OF THE BED TO A TEMPERTURE BELOW ABOUT 750*F. WITHIN 3 SECONDS TO SUBSTANTIALLY END THE CONVERSION REACTION BY LIMITING THE FREE VAPOR PASSAGEWAY ABOVE THE LEVEL OF THE DENSE, TURBULENT, FLUIDIZED BED.
Claim 2
Dependent Claim 350 words
IN A PROCESS FOR COKING A HEAVY HYDROCARBON OIL BY CONTACTING THE OIL COKING CHARGE STOCK AT A TEMPERATURE IN THE RANGE OF 900* TO 1600*F. WITH A BODY OF COKE PARTICLES MAINTAINED IN THE FORM OF A DENSE, TURBULENT, FLUIDIZED BED IN A REACTION ZONE, REMOVING PRODUCT VAPORS FROM THE REACTION ZONE, CIRCULATING THE COKE PARTICLES THROUGH AN EXTRANEOUS HEATING ZONE WHEREIN THE PARTICLES ARE HEATED AND BACK TO THE REACTION ZONE TO SUPPLY HEAT THERETO, THE IMPROVEMENT WHICH COMPRISES THE STEPS OF INJECTING THE COKE PARTICLES FROM THE HEATING ZONE UPWARDLY AT A VELOCITY IN THE RANGE OF 0.1 TO 10 FT./SEC. INTO AN UPWARDLY DIVERGING INTERNAL PASSAGEWAY OF RESTRICTED CROSS SECTION WITHIN THE DENSE, TURBULENT, FLUIDIZED BED OF COKE PARTICLES, THE PASSAGEWAY HAVING A TOTAL INCLUDED ANGLE IN THE RANGE OF 3 TO 8*, THE PORTION OF THE FLUID BED WITHIN THE PASSAGEWAY CONTAINING 20 TO 50% OF THE TOTAL DENSE, TURBULENT, FLUIDIZED BED VOLUME AND HAVING A DENSITY OF 30 TO 45 LBS./CU. FT.; INJECTING THE OIL CHARGE STOCK INTO A LOWER PORTION OF SAID PASSAGEWAY WHEREBY THE OIL UNDERGOES CRACKING YIELDING VAPOROUS CONVERSION PRODUCTS; CIRCULATING THE COKE PARTICLES FROM THE UPPER PORTION OF THE PASSAGEWAY DOWNWARDLY AT A VELOCITY IN THE RANGE OF 0.02 TO 6 FT./SEC. THROUGH AN ANNULAR PATH OF INCREASING CROSS SECTIONAL AREA DEFINED BY SAID PASSAGEWAY AND THE CONFINES OF THE REACTION ZONE TO THE LOWER PORTION OF THE PASSAGEWAY, THE FLUIDIZED BED WITHIN THE PATH HAVING A DENSITY OF 40 TO 50 LBS./CU. FT. AND GREATER THAN THAT IN THE PASSAGEWAY; INTRODUCING AN INERT STRIPPING GAS INTO THE LOWER PORTION OF SAID PATH; PASSING THE STRIPPING GAS UPWARDLY THROUGH THE PATH, THE STRIPPING GAS HAVING AN INCREASING VELOCITY AS IT PROCEEDS UPWARDLY THROUGH SAID PATH; WITHDRAWING AT A VELOCITY IN THE RANGE OF 3 TO 10FT./SEC. AND RAPIDLY COOLING THE VAPOROUS CONVERSION PRODUCTS FROM THE UPPER PORTION OF THE BED TO A TEMPERTURE BELOW ABOUT 750*F. WITHIN 3 SECONDS TO SUBSTANTIALLY END THE CONVERSION REACTION BY LIMITING THE FREE VAPOR PASSAGEWAY ABOVE THE LEVEL OF THE DENSE, TURBULENT, FLUIDIZED BED.

References Cited (Backward Citations)

US2418003A Cited
US2445328A Cited
US2649358A Cited
US2582711A Cited
US2485315A Cited
US2687992A Cited
US2623010A Cited
US2706704A Cited
US2698672A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1961-08-25 1962-02-24 1962-08-26 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1965-08-25 1966-02-24 1966-08-26 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1969-08-25 1970-02-24 1970-08-26 $7700.00 Window Closed / Lapsed

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