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Process for hydrogenating a solid carbonaceous material with Ni/Ti/Mo on a mangesium-deficient magnesium aluminate spinel-as catalyst

Assignee: Gulf Research and Development Co
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Filing: 1977-10-11
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Granted: 1978-09-26
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Expires: 1997-10-11
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Abstract

Abstract A process for hydrogenating a carbonaceous material using a novel hydrogenation catalyst comprising a hydrogenation metal mounted on a magnesium-deficient magnesium aluminate spinel.

Inventors

  • 👤 Donald C. Cronauer
  • 👤 William L. Kehl

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-09 07:49
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/08; C10G1/086; B; B01; B01J; B01J23/00; B01J23/16; B01J23/24; B01J23/70; B01J23/74; B01J23/76; B01J23/84; B01J23/85; B01J21/00; B01J21/005; B01J23/88; B01J23/883; Y; Y10; Y10S; Y10S502/00; Y10S502/524

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 55 words
A process for hydrogenating a carbonaceous material which comprises subjecting said carbonaceous material, together with hydrogen, under hydrogenation conditions in the presence of a catalyst comprising a magnesium-deficient magnesium aluminate spinel of the following formula: Mg.sub.x Al.sub.2 O.sub.3+x, wherein x is a number ranging from about 0.10 to about 0.40, carrying nickel, titanium and molybdenum.
Claim 2
Dependent Claim 55 words
A process for hydrogenating a carbonaceous material which comprises subjecting said carbonaceous material, together with hydrogen, under hydrogenation conditions in the presence of a catalyst comprising a magnesium-deficient magnesium aluminate spinel of the following formula: Mg.sub.x Al.sub.2 O.sub.3+x, wherein x is a number ranging from about 0.10 to about 0.40, carrying nickel, titanium and molybdenum.
Claim 3
Dependent Claim 17 words
The process of claim 1 wherein x is a number ranging from about 0.2 to about 0.3.
Claim 4
Dependent Claim 11 words
The process of claim 1 wherein said carbonaceous material is coal.
Claim 5
Dependent Claim 38 words
The process of claim 1 wherein said hydrogenation is carried out at a temperature of about 260° to about 480° C. and the pressure in the range of about 100 to about 5000 pounds per square inch gauge.
Claim 6
Dependent Claim 38 words
The process of claim 1 wherein said hydrogenation is carried out at a temperature of about 370° to about 454° C. and a pressure in the range of about 1000 to about 4000 pounds per square inch gauge.
Claim 7
Dependent Claim 47 words
The process of claim 1 wherein the catalyst has a pore volume of about 0.25 to about 0.8 cubic centimeters per gram, an average pore diameter of about 80 to about 130 A and a surface area of about 70 to about 350 square meters per gram.
Claim 8
Dependent Claim 47 words
The process of claim 1 wherein the catalyst has a pore volume of about 0.45 to about 0.8 cubic centimeters per gram, an average pore diameter of about 80 to about 115 A and a surface area of about 250 to about 300 square meters per gram.

References Cited (Backward Citations)

US3459657A Cited
US3751508A Cited
US3728252A Cited
US3619404A Cited
US4019975A Cited
US4049582A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-09-25 1982-03-27 1982-09-26 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-09-25 1986-03-27 1986-09-26 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-09-25 1990-03-27 1990-09-26 $7700.00 Window Closed / Lapsed

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