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US3669873A Expired / Lapsed US ⏱️ 0.0 years remaining

Hydrofining-hydrocracking process

Assignee: Chevron USA Inc
•
Filing: 1970-03-31
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Granted: 1972-06-13
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Expires: 1990-03-31
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Abstract

Abstract A hydrofining-hydrocracking process which comprises contacting a hydrocarbon feed containing more than 50 parts per million of organic nitrogen and substantial amounts of materials boiling above 200* F., said feed being selected from the group consisting of petroleum distillates, solvent-deasphalted petroleum residua, shale oils and coal tar distillates, in a reaction zone with hydrogen and a catalyst, a t hydrofining-hydrocracking conditions including a temperature in the range 400* to 950* F., a pressure in the range 800 to 3,500 psig, a liquid hourly space velocity in the range 0.1 to 5.0, and a total hydrogen supply rate of 200 to 20,000 SCF of hydrogen per barrel of feedstock, removing ammonia from the effluent from said reaction zone, and recovering hydrofined and hydrocracked products from said reaction zone, said catalyst comprising: A. A gel matrix comprising: A. AT LEAST 15 WEIGHT PERCENT SILICA, B. ALUMINA, IN AN AMOUNT PROVIDING AN ALUMINA-TO-SILICA WEIGHT RATIO OF 15/85 TO 80/20, C. Nickel or cobalt, or the combination thereof, in the form of metal, oxide, sulfide or any combination thereof, in an amount of 1 to 10 weight percent, based on said matrix, calculated as metal, D. Molybdenum or tungsten, or the combination thereof, in the form of metal, oxide, sulfide or any combination thereof, in an amount of 5 to 25 weight percent, based on said matrix, calculated as metal; B. A crystalline zeolitic molecular sieve: A. CONTAINING LESS THAN 5 WEIGHT PERCENT SODIUM, B. CONTAINING IONS SELECTED FROM Mn, rare earths of atomic numbers 58 to 71, and alkaline earths Mg, Ca, Sr and Ba, C. BEING SUBSTANTIALLY FREE OF ANY CATALYTIC LOADING METALS, D. BEING IN PARTICULATE FORM AND BEING DISPERSED THROUGHOUT SAID MATRIX BY COGELATION OF SAID MATRIX AROUND SAID SIEVE; SAID CATALYST COMPOSITE BEING FURTHER CHARACTERIZED BY AN AVERAGE PORE DIAMETER BELOW 100 Angstroms and a surface area above 200 square meters per gram.

Inventors

  • 👤 Joseph Jaffe
  • 👤 James R Kittrell

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 12:56
CPC Classifications
C; C10; C10G; C10G45/00; C10G45/02; C10G45/04; C10G45/12; B; B01; B01J; B01J29/00; B01J29/04; B01J29/06; B01J29/061; C10G65/00; C10G65/02; C10G65/12

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 24 words
A process as in claim 1, wherein a gasoline product and a jet fuel product are recovered from the effluent from said reaction zone.
Claim 2
Dependent Claim 101 words
A process as in claim 2, wherein a portion of the effluent from said reaction zone boiling above the gasoline boiling range is hydrocracked in a second reaction zone in the presence of hydrogen and a hydrocracking catalyst at hydrocracking conditions including a temperature in the range 400* to 950* F., a pressure in the range 800 to 3,500 psig, a liquid hourly space velocity in the range 0.1 to 5.0, and a total hydrogen supply rate of 200 to 20,000 SCF of hydrogen per barrel of feedstock, and wherein at least one hydrocracked product is recovered from said reaction zone.

References Cited (Backward Citations)

US3267022A Cited
US3140253A Cited
US3393148A Cited
US3562144A Cited
US3459680A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1975-06-13 1975-12-13 1976-06-13 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1979-06-13 1979-12-13 1980-06-13 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1983-06-13 1983-12-13 1984-06-13 $7700.00 Window Closed / Lapsed

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