← Back to Patent Explorer
US4637871A Expired / Lapsed US ⏱️ 0.0 years remaining

Hydrocracking with aqueous phosphomolybdic acid

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1985-10-10
•
Granted: 1987-01-20
•
Expires: 2005-10-10
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract Slurry hydroconversion processes utilizing an aqueous solution of phosphomolybdic acid as catalyst precursor, which is subsequently converted to a solid molybdenum-containing catalyst, are improved when the catalyst precursor aqueous solution comprises a specified concentration of molybdenum derived from the phosphomolybdic acid. The improved hydroconversion processes and the improved method of preparing the catalyst are provided.

Inventors

  • 👤 Roby Bearden, Jr.
  • 👤 Clyde L. Aldridge

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 16:58
CPC Classifications
C; C10; C10G; C10G47/00; C10G47/24; C10G47/26

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 205 words
In a method for preparing a catalyst wherein aqueous phosphomolybdic acid is heated in the presence of a hydrocarbonaceous material and a gas selected from the group consisting of a hydrogen-containing gas, a hydrogen sulfide-containing gas and mixtures thereof to convert said phosphomolybdic acid to a solid catalyst, the improvement which comprises: (a) forming a mixture of a first hydrocarbonaceous material comprising at least about 10 weight percent constituents boiling above about 1050° F. and said aqueous solution of phosphomolybdic acid in an amount to provide in said mixture from about 0.2 to 2 weight percent molybdenum, calculated as elemental metal, based on said first hydrocarbonaceous material, said aqueous solution comprising from about 3 to about 5 weight percent molybdenum derived from said phosphomolybdic acid to produce a catalyst precursor concentrate; (b) introducing at least a portion of said catalyst precursor concentrate into a second hydrocarbonaceous material having a different boiling point range from said first hydrocarbonaceous material; (c) heating the mixture resulting from step (a) or the mixture resulting from step (b) in the presence of a gas selected from the group consisting of hydrogen-containing gas, hydrogen sulfide-containing gas, and mixtures thereof at conditions to convert said phosphomolybdic acid to a solid molybdenum-containing catalyst.
Claim 2
Dependent Claim 205 words
In a method for preparing a catalyst wherein aqueous phosphomolybdic acid is heated in the presence of a hydrocarbonaceous material and a gas selected from the group consisting of a hydrogen-containing gas, a hydrogen sulfide-containing gas and mixtures thereof to convert said phosphomolybdic acid to a solid catalyst, the improvement which comprises: (a) forming a mixture of a first hydrocarbonaceous material comprising at least about 10 weight percent constituents boiling above about 1050° F. and said aqueous solution of phosphomolybdic acid in an amount to provide in said mixture from about 0.2 to 2 weight percent molybdenum, calculated as elemental metal, based on said first hydrocarbonaceous material, said aqueous solution comprising from about 3 to about 5 weight percent molybdenum derived from said phosphomolybdic acid to produce a catalyst precursor concentrate; (b) introducing at least a portion of said catalyst precursor concentrate into a second hydrocarbonaceous material having a different boiling point range from said first hydrocarbonaceous material; (c) heating the mixture resulting from step (a) or the mixture resulting from step (b) in the presence of a gas selected from the group consisting of hydrogen-containing gas, hydrogen sulfide-containing gas, and mixtures thereof at conditions to convert said phosphomolybdic acid to a solid molybdenum-containing catalyst.
Claim 3
Dependent Claim 19 words
The method of claim 1 wherein prior to step (b), water is removed from said mixture of step (a).
Claim 4
Dependent Claim 18 words
The method of claim 1 wherein said second hydrocarbonaceous material has a boiling point above about 430° F.
Claim 5
Dependent Claim 27 words
The method of claim 1 wherein in step (a), said molybdenum is present in said mixture in an amount ranging from about 0.2 to 1 weight percent.
Claim 6
Dependent Claim 14 words
The method of claim 1 wherein said first hydrocarbonaceous material is an atmospheric residuum.
Claim 7
Dependent Claim 27 words
The method of claim 1 wherein said heating of step (c) is conducted prior to step (b) at a temperature ranging from about 500° to 779° F.
Claim 8
Dependent Claim 24 words
The method of claim 1 wherein said gas of step (b) comprises hydrogen and from about 1 to about 90 mole percent hydrogen sulfide.
Claim 9
Dependent Claim 24 words
The method of claim 1 wherein said first hydrocarbonaceous material is an atmospheric residuum and wherein said second hydrocarbonaceous material comprises a vacuum residuum.
Claim 10
Dependent Claim 35 words
The method of claim 1 wherein said molybdenum in step (a) is present in an amount ranging from about 0.3 to 1 weight percent molybdenum, calculated as elemental metal, based on said first hydrocarbonaceous material.
Claim 11
Dependent Claim 14 words
The method of claim 1 wherein said second hydrocarbonaceous material is a hydrocarbonaceous oil.

References Cited (Backward Citations)

US3532617A Cited
US4125455A Cited
US4169101A Cited
US4077867A Cited
US4111787A Cited
US4196072A Cited
US4226742A Cited
US4244839A Cited
US4424110A Cited
US4557822A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1990-01-19 1990-07-21 1991-01-20 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1994-01-19 1994-07-21 1995-01-20 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1998-01-19 1998-07-21 1999-01-20 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag