US4637871A
Expired / Lapsed
US
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Hydrocracking with aqueous phosphomolybdic acid
Assignee: ExxonMobil Technology and Engineering Co
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Filing: 1985-10-10
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Granted: 1987-01-20
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Expires: 2005-10-10
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.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
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| 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 |