US4637870A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Hydrocracking with phosphomolybdic acid and phosphoric 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 Hydroconversion processes for converting oil, coal or mixtures thereof are provided utilizing a catalyst prepared by first forming an aqueous solution of phosphomolybdic acid and phosphoric acid at a specified ratio of atoms of P/Mo, and subsequently adding this solution to a hydrocarbon material, followed by heating in the presence of H2 and/or H2S to form a solid molybdenum and phosphorus-containing catalyst.
Inventors
- 👤 Roby Bearden, Jr.
- 👤 Clyde L. Aldridge
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 21:45
CPC Classifications
B; B01; B01J; B01J27/00; B01J27/14; B01J27/186; B01J27/188; B01J27/19; C; C10; C10G; C10G49/00; C10G49/02; C10G49/04; C10G49/10; C10G49/12
Claims Analysis
Total Claims: 13
Claim 1
Independent Claim
208 words
A process for hydroconverting a heavy hydrocarbonaceous oil chargestock comprising a catalyst to produce lower boiling hydrocarbon products, which comprises reacting said chargestock with hydrogen at hydroconversion conditions, including a temperature ranging from about 800 to about 900° F., said catalyst having been prepared by the steps which comprise: (a) adding phosphoric acid to an aqueous solution of phosphomolybdic acid in an amount to provide in said solution an atomic ratio of phosphorus to molybdenum ranging from 0.12:1 to 0.45:1; and, subsequently (b) forming a mixture of a hydrocarbonaceous material having a different boiling point range from said chargestock and the aqueous solution resulting from step (a), in an amount to provide in said mixture from about 0.2 to 2 weight percent molybdenum, calculated as elemental metal, based on said hydrocarbonaceous material to produce a catalyst precursor concentrate; (c) introducing at least a portion of said catalyst precursor concentrate into said chargestock; and (d) heating the mixture resulting from step (b), or the mixture resulting from step (c) in the presence of a gas selected from the group consisting of a hydrogen-containing gas, a hydrogen sulfide-containing gas and mixtures thereof at conditions to convert said phosphomolybdic acid and said phosphoric acid to a solid molybdenum and phosphorus-containing catalyst.
Claim 2
Dependent Claim
208 words
A process for hydroconverting a heavy hydrocarbonaceous oil chargestock comprising a catalyst to produce lower boiling hydrocarbon products, which comprises reacting said chargestock with hydrogen at hydroconversion conditions, including a temperature ranging from about 800 to about 900° F., said catalyst having been prepared by the steps which comprise: (a) adding phosphoric acid to an aqueous solution of phosphomolybdic acid in an amount to provide in said solution an atomic ratio of phosphorus to molybdenum ranging from 0.12:1 to 0.45:1; and, subsequently (b) forming a mixture of a hydrocarbonaceous material having a different boiling point range from said chargestock and the aqueous solution resulting from step (a), in an amount to provide in said mixture from about 0.2 to 2 weight percent molybdenum, calculated as elemental metal, based on said hydrocarbonaceous material to produce a catalyst precursor concentrate; (c) introducing at least a portion of said catalyst precursor concentrate into said chargestock; and (d) heating the mixture resulting from step (b), or the mixture resulting from step (c) in the presence of a gas selected from the group consisting of a hydrogen-containing gas, a hydrogen sulfide-containing gas and mixtures thereof at conditions to convert said phosphomolybdic acid and said phosphoric acid to a solid molybdenum and phosphorus-containing catalyst.
Claim 3
Dependent Claim
19 words
The process of claim 1 wherein prior to step (c), water is removed from said mixture of step (b).
Claim 4
Dependent Claim
29 words
The process of claim 1 wherein said phosphoric acid is added in step (a) in an amount to provide an atomic ratio of P/Mo ranging from 0.2:1 to 0.4:1.
Claim 5
Dependent Claim
23 words
The process of claim 1 wherein said heating of step (d) is conducted at a temperature ranging from about 500° to 779° F.
Claim 6
Dependent Claim
27 words
The process of claim 1 wherein in step (b), said molybdenum is present in said mixture in an amount ranging from about 0.2 to 1 weight percent.
Claim 7
Dependent Claim
24 words
The process of claim 1 wherein said heating of step (d) is conducted at a temperature ranging from about 650° to about 779° F.
Claim 8
Dependent Claim
16 words
The process of claim 1 wherein said hydrocarbonaceous material of step (b) is an atmospheric residuum.
Claim 9
Dependent Claim
66 words
The process of claim 1 wherein said catalyst precursor concentrate of step (b) is heated in the presence of said gas at conditions, including a temperature ranging from about 500° to about 779° F., to convert said phosphomolybdic acid and phosphoric acid to produce said solid catalyst and, thereafter, at least a portion of the resulting concentrate comprising said solid catalyst is introduced into said chargestock.
Claim 10
Dependent Claim
32 words
The process of claim 1 wherein said catalyst precursor concentrate of step (b) is heated to remove the water, and, thereafter, the resulting water-free catalyst precursor concentrate is introduced into said chargestock.
Claim 11
Dependent Claim
33 words
The process of claim 1 wherein said hydroconversion conditions include a temperature ranging from about 820° to about 870° F. and a hydrogen partial pressure ranging from about 50 to about 5000 psig.
Claim 12
Dependent Claim
36 words
The process of claim 1 wherein said catalyst is present in said carbonaceous chargestock in an amount to provide from about 10 to about 2000 wppm molybdenum, calculated as elemental metal, based on said carbonaceous chargestock.
Claim 13
Dependent Claim
15 words
The process of claim 1 wherein said heavy hydrocarbonaceous oil chargestock is a vacuum residuum.
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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 |