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US3203889A Expired / Lapsed US ⏱️ 0.0 years remaining

Catalytic hydrocracking process with the preliminary hydrogenation of the aromatic containing feed oil

Assignee: Universal Oil Products Co
•
Filing: 1962-11-01
•
Granted: 1965-08-31
•
Expires: 1982-11-01
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Abstract

No abstract record available.

Inventors

  • 👤 Ernest L Pollitzer
  • 👤 Haensel Vladimir

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 07:16
CPC Classifications
C; C10; C10G; C10G65/00; C10G65/02; C10G65/12; B; B01; B01J; B01J23/00; B01J23/38; B01J23/54; B01J23/56; B01J23/58; C10G45/00; C10G45/44; C10G45/46; C10G45/52; B01J23/90

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 129 words
A PROCESS FOR CONVERTING HYDROCARBONACEOUS MATERIAL CONTAINING AROMATIC COMPOUNDS INTO LOWER-BOILING HYDROCARBON PRODUCTS WHICH COMPRISES REACTING SAID HYDROCARBONACEOUS MATERIAL WITH HYDROGEN IN CONTACT WITH A NONACIDIC HYDROGENATION CATALYST, AT HYDROGENATION CONDITIONS INCLUDING A TEMPERATURE OF AT LEAST ABOUT 300* F., SELECTED TO PROVIDE A MAXIMUM CATALYST TEMPERATURE LESS THAN ABOUT 650* F. AND TO HYDROGENATE AROMATIC COMPOUNDS WITHOUT SUBSTANTIAL HYDROCRACKING OF SAID HYDROCARBONACEOUS MATERIAL; THEREAFTER REACTING THE TOTAL HYDROGENATED, SUBSTANTIALLY AROMATIC-FREE HYDROCARBONACEOUS EFFLUENT FROM THE FIRST-MENTIONED STEP WITH HYDROGEN AT HYDROCRACKING CONDITIONS INCLUDING A TEMPERATURE WITHIN THE RANGE OF FROM ABOUT 400* F. TO ABOUT 950* F., AND IN CONTACT WITH AN ACIDIC HYDROCRACKING CATALYST; THE PROCESS BEING FURTHER CHARACTERIZED IN THAT SAID HYDROGENATION CATALYST COMPRISES A PLATINUM-GROUP METALLIC COMPONENT, A NON-SILICEOUS INORGANIC OXIDE AND AT LEAST ONE METALLIC
Claim 2
Dependent Claim 129 words
A PROCESS FOR CONVERTING HYDROCARBONACEOUS MATERIAL CONTAINING AROMATIC COMPOUNDS INTO LOWER-BOILING HYDROCARBON PRODUCTS WHICH COMPRISES REACTING SAID HYDROCARBONACEOUS MATERIAL WITH HYDROGEN IN CONTACT WITH A NONACIDIC HYDROGENATION CATALYST, AT HYDROGENATION CONDITIONS INCLUDING A TEMPERATURE OF AT LEAST ABOUT 300* F., SELECTED TO PROVIDE A MAXIMUM CATALYST TEMPERATURE LESS THAN ABOUT 650* F. AND TO HYDROGENATE AROMATIC COMPOUNDS WITHOUT SUBSTANTIAL HYDROCRACKING OF SAID HYDROCARBONACEOUS MATERIAL; THEREAFTER REACTING THE TOTAL HYDROGENATED, SUBSTANTIALLY AROMATIC-FREE HYDROCARBONACEOUS EFFLUENT FROM THE FIRST-MENTIONED STEP WITH HYDROGEN AT HYDROCRACKING CONDITIONS INCLUDING A TEMPERATURE WITHIN THE RANGE OF FROM ABOUT 400* F. TO ABOUT 950* F., AND IN CONTACT WITH AN ACIDIC HYDROCRACKING CATALYST; THE PROCESS BEING FURTHER CHARACTERIZED IN THAT SAID HYDROGENATION CATALYST COMPRISES A PLATINUM-GROUP METALLIC COMPONENT, A NON-SILICEOUS INORGANIC OXIDE AND AT LEAST ONE METALLIC

References Cited (Backward Citations)

US2671754A Cited
US2971901A Cited
US3008895A Cited
US3092567A Cited
US3023158A Cited
US3132086A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1968-08-30 1969-03-01 1969-08-31 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1972-08-30 1973-03-01 1973-08-31 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1976-08-30 1977-03-01 1977-08-31 $7700.00 Window Closed / Lapsed

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