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US4389378A Expired / Lapsed US ⏱️ 0.0 years remaining

Process using sulphate reagent for recovering vanadium from cokes derived from heavy oils

Assignee: Gulf Canada Ltd
•
Filing: 1981-12-24
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Granted: 1983-06-21
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Expires: 2001-12-24
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Abstract

Abstract Vanadium values are recovered from cokes and ashes derived from heavy oils by a novel process comprising heating in the presence of alkali metal sulphate, contacting the resulting solid residue with water and recovering the vanadium values dissolved therein.

Inventors

  • 👤 Lois L. McCorriston

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 12:00
CPC Classifications
C; C01; C01G; C01G31/00; C22; C22B; C22B34/00; C22B34/20; C22B34/22

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 143 words
A process for the recovery of vanadium from a sulphur-containing material of the group consisting of coke derived from oil and ash obtained from said coke, wherein said hydrocarbonaceous oil is heavy oil, in-situ oil sands bitumen or mineable oil sands bitumen, comprising: (a) mixing said material with an alkali metal sulphate reagent in a finely divided form, (b) heating the mixture in the presence of an oxidizing atmosphere at an elevated temperature below the fusion point of the reagent, (c) contacting the resulting solid residue with water, thereby forming a leach solution consisting essentially of water and sodium vanadate compounds, and (d) recovering the vanadium values from the leach solution, the amount of said alkali metal sulphate being sufficient to convert the vanadium values present in said material into alkali metal vanadate and to maintain said leach solution substantially free of reagent.
Claim 2
Dependent Claim 143 words
A process for the recovery of vanadium from a sulphur-containing material of the group consisting of coke derived from oil and ash obtained from said coke, wherein said hydrocarbonaceous oil is heavy oil, in-situ oil sands bitumen or mineable oil sands bitumen, comprising: (a) mixing said material with an alkali metal sulphate reagent in a finely divided form, (b) heating the mixture in the presence of an oxidizing atmosphere at an elevated temperature below the fusion point of the reagent, (c) contacting the resulting solid residue with water, thereby forming a leach solution consisting essentially of water and sodium vanadate compounds, and (d) recovering the vanadium values from the leach solution, the amount of said alkali metal sulphate being sufficient to convert the vanadium values present in said material into alkali metal vanadate and to maintain said leach solution substantially free of reagent.
Claim 3
Dependent Claim 17 words
A process as claimed in claim 1 wherein said material is coke derived from said hydrocarbonaceous oil.
Claim 4
Dependent Claim 19 words
A process as claimed in claim 1 wherein said material is ash derived from the combustion of said coke.
Claim 5
Dependent Claim 25 words
A process as claimed in claim 1 wherein said heating step is carried out at a temperature between substantially 500° C. and substantially 880° C.

References Cited (Backward Citations)

US831280A Cited
US2187750A Cited
GB1331932A Cited
US3792150A Cited
US4087510A Cited
US4243639A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1986-06-20 1986-12-20 1987-06-21 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1990-06-20 1990-12-20 1991-06-21 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1994-06-20 1994-12-20 1995-06-21 $7700.00 Window Closed / Lapsed

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