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Hydrotreating process employing thermactivated catalysts comprising catalytic metals-free crystalline zeolitic molecular sieve particles dispersed in a gel matrix

Assignee: Chevron USA Inc
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Filing: 1975-11-17
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Granted: 1976-11-02
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Expires: 1995-11-17
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Abstract

Abstract Method of activating a catalyst composite comprising particles of a catalytic metals-free crystalline zeolitic molecular sieve dispersed in a gel matrix comprising silica-alumina, a Group VI hydrogenating component and a Group VIII hydrogenating component, which method comprises heating said catalyst composite in an oxygen-containing gas stream at 1200° to 1600° F. for 0.25 to 43 hours, and the catalyst composite so activated.

Inventors

  • 👤 Joseph Jaffe

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 14:46
CPC Classifications
B; B01; B01J; B01J29/00; B01J29/04; B01J29/06; B01J29/076

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 221 words
A hydrotreating process, which comprises contacting a hydrocarbon feed in a reaction zone under hydrotreating conditions with hydrogen and a 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 of 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 of said matrix, calculated as metal; B. a crystalline zeolitic molecular sieve substantially in the ammonia or hydrogen form, substantially free of any catalytic loading metal or metals, said sieve further being in particulate form and being dispersed through said matrix; said catalyst composite being further characterized by an average pore diameter below 100 Angstroms and a surface area above 200 square meters per gram; said catalyst composite being further characterized by hydrocracking activities and stabilities developed therein by heating said catalyst composite in an oxygen-containing gas stream at temperatures in the range 1200° F. to 1600° F. for 0.25 to 48 hours; and recovering hydrotreated products from said reaction zone.
Claim 2
Dependent Claim 221 words
A hydrotreating process, which comprises contacting a hydrocarbon feed in a reaction zone under hydrotreating conditions with hydrogen and a 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 of 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 of said matrix, calculated as metal; B. a crystalline zeolitic molecular sieve substantially in the ammonia or hydrogen form, substantially free of any catalytic loading metal or metals, said sieve further being in particulate form and being dispersed through said matrix; said catalyst composite being further characterized by an average pore diameter below 100 Angstroms and a surface area above 200 square meters per gram; said catalyst composite being further characterized by hydrocracking activities and stabilities developed therein by heating said catalyst composite in an oxygen-containing gas stream at temperatures in the range 1200° F. to 1600° F. for 0.25 to 48 hours; and recovering hydrotreated products from said reaction zone.
Claim 3
Dependent Claim 19 words
A process as in claim 1 further characterized in that said gel matrix further comprises a Group IV component.
Claim 4
Dependent Claim 16 words
A process as in claim 2 further characterized in that said Group IV component is titania.
Claim 5
Dependent Claim 28 words
A process as in claim 1 further characterized in that said gel matrix comprises nickel and tungsten, in the form of metal, oxide, sulfide, or any combination thereof.

References Cited (Backward Citations)

US3457191A Cited
US3433732A Cited
US3558471A Cited
US3558475A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-11-02 1980-05-03 1980-11-02 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-11-02 1984-05-03 1984-11-02 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-11-02 1988-05-03 1988-11-02 $7700.00 Window Closed / Lapsed

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