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US3159568A Expired / Lapsed US ⏱️ 0.0 years remaining

Low pressure hydrocracking process with hydrofining of feed

Assignee: Union Oil Company of California
•
Filing: 1961-10-02
•
Granted: 1964-12-01
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Expires: 1981-10-02
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Abstract

No abstract record available.

Inventors

  • 👤 Frank C Price
  • 👤 Anthony J Tulleners
  • 👤 Cloyd P Reeg

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 07:56
CPC Classifications
C; C10; C10G; C10G65/00; C10G65/02; C10G65/12; C10G69/00; C10G69/02; C10G69/08; C10G69/10

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 250 words
AN IMPROVED, LOW-PRESSURE PROCESSES FOR HYDROCRACKING A MINERAL OIL FEEDSTOCK BOILING ABOVE THE GASOLINE RANGE AND CONTAINING ORGANIC NITROGEN COMPOUNDS, WHICH COMPRISES FIRST SUBJECTING SAID FEEDSTOCK TO CATALYTIC HYDROFINING UNDER SUBSTANTIALLY NON-CRACKING CONDITIONS IN THE PRESENCE OF ADDED HYDROGEN AND A HYDROFINING CATALYST COMPRISING A HYDROGENTING COMPONENET FROM THE CLASS CONSISTING OF THE OXIDES AND SULFIDES OF MOLYBDENUM, TUNGSTEN AND THE GROUP VIII METALS SUPPORTED ON A SUBSTANTIALLY NON-CRACKING INORGANIC OXIDE CARRIER, AND UNDER HYDROFINING CONDITIONS ADJUSTED TO GIVE A SUBSTANTIAL DECOMPOSITION OF SAID ORGANIC NITROGEN COMPOUNDS WITH RESULTANT FORMATION OF AMMONIA, SUBJECTING EFFLUENT FROM SAID HYDROFINING STEP, WITHOUT INTERVENING PURIFICATION TO REMOVE AMMONIA, TO A FIRST STAGE OF HYDROCRACKING AT A SPACE VELOCITY BETWEEN ABOUT 0.5 AND 10 IN THE PRESENCE OF A HYDROCRACKING CATALYST COMPRISING A SOLID REFRACTORY CRACKING BASE AND A GROUP VIII METAL SULFIDE HYDROGENATING COMPONENT, TREATING MIXED EFFLUENT FROM SAID FIRST STAGE OF HYDROCRACKING AND THE EFFLUENT FROM THE HEREINAFTER DEFINED SECOND STAGE OF HYDROCRACKING TO SEPARATE AMMONIA AND LOW-BOILING HYDROCARBONS THEREFROM , SUBJECTING REMAINING OIL BOILING ABOVE THE GASOLINE RANGE TO A SECOND STAGE OF HYDROCRACKING IN THE PRESENCE OF HYDROGEN AND A FIXED BED OF HYDROCRACKING CATALYST COMPRISING A SOLID REFRACTORY CRACKING BASE AND A GROUP VIII METAL HYDROGENATING COMPONENT, AND COMBINING THE EFFLUENT FROM SAID SECOND STAGE OF HYDROCRACKING WITH SAID FIRSTSTAGE HYDROCRACKING EFFLUENT TO FORM SAID MIXED EFFLUENT, EACH OF SAID HYDROFINING AND HYDROCRACKING STEPS BEING CARRIED OUT AT PRESSURES BETWEEN ABOUT 400-2,000 P.S.I.G., AND TEMPERATURES BETWEEN ABOUT 450* AND 875*F.
Claim 2
Dependent Claim 250 words
AN IMPROVED, LOW-PRESSURE PROCESSES FOR HYDROCRACKING A MINERAL OIL FEEDSTOCK BOILING ABOVE THE GASOLINE RANGE AND CONTAINING ORGANIC NITROGEN COMPOUNDS, WHICH COMPRISES FIRST SUBJECTING SAID FEEDSTOCK TO CATALYTIC HYDROFINING UNDER SUBSTANTIALLY NON-CRACKING CONDITIONS IN THE PRESENCE OF ADDED HYDROGEN AND A HYDROFINING CATALYST COMPRISING A HYDROGENTING COMPONENET FROM THE CLASS CONSISTING OF THE OXIDES AND SULFIDES OF MOLYBDENUM, TUNGSTEN AND THE GROUP VIII METALS SUPPORTED ON A SUBSTANTIALLY NON-CRACKING INORGANIC OXIDE CARRIER, AND UNDER HYDROFINING CONDITIONS ADJUSTED TO GIVE A SUBSTANTIAL DECOMPOSITION OF SAID ORGANIC NITROGEN COMPOUNDS WITH RESULTANT FORMATION OF AMMONIA, SUBJECTING EFFLUENT FROM SAID HYDROFINING STEP, WITHOUT INTERVENING PURIFICATION TO REMOVE AMMONIA, TO A FIRST STAGE OF HYDROCRACKING AT A SPACE VELOCITY BETWEEN ABOUT 0.5 AND 10 IN THE PRESENCE OF A HYDROCRACKING CATALYST COMPRISING A SOLID REFRACTORY CRACKING BASE AND A GROUP VIII METAL SULFIDE HYDROGENATING COMPONENT, TREATING MIXED EFFLUENT FROM SAID FIRST STAGE OF HYDROCRACKING AND THE EFFLUENT FROM THE HEREINAFTER DEFINED SECOND STAGE OF HYDROCRACKING TO SEPARATE AMMONIA AND LOW-BOILING HYDROCARBONS THEREFROM , SUBJECTING REMAINING OIL BOILING ABOVE THE GASOLINE RANGE TO A SECOND STAGE OF HYDROCRACKING IN THE PRESENCE OF HYDROGEN AND A FIXED BED OF HYDROCRACKING CATALYST COMPRISING A SOLID REFRACTORY CRACKING BASE AND A GROUP VIII METAL HYDROGENATING COMPONENT, AND COMBINING THE EFFLUENT FROM SAID SECOND STAGE OF HYDROCRACKING WITH SAID FIRSTSTAGE HYDROCRACKING EFFLUENT TO FORM SAID MIXED EFFLUENT, EACH OF SAID HYDROFINING AND HYDROCRACKING STEPS BEING CARRIED OUT AT PRESSURES BETWEEN ABOUT 400-2,000 P.S.I.G., AND TEMPERATURES BETWEEN ABOUT 450* AND 875*F.

References Cited (Backward Citations)

US2839450A Cited
US2945800A Cited
US2983670A Cited
US2971901A Cited
US3008895A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1967-12-01 1968-06-01 1968-12-01 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1971-12-01 1972-06-01 1972-12-01 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1975-12-01 1976-06-01 1976-12-01 $7700.00 Window Closed / Lapsed

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