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Process for hydrorefining a hydrocarbon utilizing a non-stoichiometric vanadium sulfide catalyst

Assignee: Honeywell UOP LLC
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Filing: 1979-04-02
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Granted: 1980-04-22
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Expires: 1999-04-02
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Abstract

Abstract A non-stoichiometric vanadium sulfide catalyst utilized in a process for hydrorefining a hydrocarbon feed stock is prepared by (1) contacting vanadium oxide with ammonium sulfide to form an ammonium salt of vanadium sulfide and (2) the salt is neutralized with an acid in a non-oxidative atmosphere to form the vanadium sulfide catalyst. The acid used in the neutralizing step may be sulfuric acid or carbonic acid and the non-oxidative atmosphere may be hydrogen or nitrogen.

Inventors

  • 👤 John G. Gatsis

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 20:39
CPC Classifications
B; B01; B01J; B01J23/00; B01J23/16; B01J23/20; B01J23/22; C; C10; C10G; C10G45/00; C10G45/02; C10G45/14; C10G45/16

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 105 words
A process for hydrorefining a hydrocarbon charge stock which comprises reacting an admixture of said charge stock with hydrogen and with a colloidally dispersed non-stoichiometric vanadium sulfide catalyst which is prepared according to the following method: (a) contacting vandaium oxide with ammonium sulfide at a temperature and pressure sufficient to form an ammonium salt of the vanadium sulfide; (b) neutralizing with an acid, the resulting ammonium salt of the vanadium sulfide derived from step (a) in a non-oxidative atmosphere to form said vanadium sulfide catalyst; and (c) passing said vanadium sulfide catalyst from step (b) to form said admixture with said charge stock and hydrogen.
Claim 2
Dependent Claim 105 words
A process for hydrorefining a hydrocarbon charge stock which comprises reacting an admixture of said charge stock with hydrogen and with a colloidally dispersed non-stoichiometric vanadium sulfide catalyst which is prepared according to the following method: (a) contacting vandaium oxide with ammonium sulfide at a temperature and pressure sufficient to form an ammonium salt of the vanadium sulfide; (b) neutralizing with an acid, the resulting ammonium salt of the vanadium sulfide derived from step (a) in a non-oxidative atmosphere to form said vanadium sulfide catalyst; and (c) passing said vanadium sulfide catalyst from step (b) to form said admixture with said charge stock and hydrogen.
Claim 3
Dependent Claim 13 words
The process of claim 1 wherein said hydrocarbon charge stock contains pentane-insoluble asphaltenes.
Claim 4
Dependent Claim 11 words
The process of claim 1 wherein said non-oxidative atmosphere comprises hydrogen.
Claim 5
Dependent Claim 11 words
The process of claim 1 wherein said non-oxidative atmosphere comprises nitrogen.
Claim 6
Dependent Claim 11 words
The process of claim 1 wherein said acid is carbonic acid.
Claim 7
Dependent Claim 11 words
The process of claim 1 wherein said acid is sulfuric acid.

References Cited (Backward Citations)

US3622498A Cited
US3622497A Cited
US3619410A Cited
GB1327635A Cited
US4139453A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-04-22 1983-10-22 1984-04-22 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-04-22 1987-10-22 1988-04-22 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-04-22 1991-10-22 1992-04-22 $7700.00 Window Closed / Lapsed

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