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US4528100A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for producing high yield of gas turbine fuel from residual oil

Assignee: General Electric Co
•
Filing: 1983-10-31
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Granted: 1985-07-09
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Expires: 2003-10-31
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Abstract

Abstract The acceptability of residual oil as a gas turbine fuel is greatly enhanced in a two step process which significantly decreases the vanadium content of the residual fuel. In the process, the residual oil is first broken down into an oil phase and asphaltene phase by either conventional or supercritical extraction. In this step, the majority of vanadium remains in the asphaltene phase. The vanadium is then removed from the asphaltenes by a supercritical solvent extraction process in which the vanadium free asphaltene phase is then re-dissolved in the oil for use as a gas turbine fuel. This fuel possesses significantly lower vanadium content, and thus permits gas turbine operation for greater periods of time without maintenance.

Inventors

  • 👤 Andrew S. Zarchy

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 21:05
CPC Classifications
B; B01; B01D; B01D11/00; B01D11/04; B01D11/0403; B01D11/0407; C; C10; C10G; C10G53/00; C10G53/02; C10G53/04; C10G53/06

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 93 words
A process for the treatment of residual oil comprising the steps of: treating a feed supply of said residual oil so as to produce a first extract and a first raffinate by supercritical solvent extraction using a first supercritical solvent; treating said first raffinate so as to produce a second extract and a second raffinate by supercritical solvent extraction using a second supercritical solvent, said treatment of said first raffinate operating to concentrate vanadium present in said residual feed supply in said second extract; and combining said first extract and said second raffinate.
Claim 2
Dependent Claim 93 words
A process for the treatment of residual oil comprising the steps of: treating a feed supply of said residual oil so as to produce a first extract and a first raffinate by supercritical solvent extraction using a first supercritical solvent; treating said first raffinate so as to produce a second extract and a second raffinate by supercritical solvent extraction using a second supercritical solvent, said treatment of said first raffinate operating to concentrate vanadium present in said residual feed supply in said second extract; and combining said first extract and said second raffinate.
Claim 3
Dependent Claim 26 words
The process of claim 1 in which said first supercritical solvent comprises material selected from the group consisting of carbon dioxide, hexane, propane, pentane and butane.
Claim 4
Dependent Claim 26 words
The process of claim 1 in which said second supercritical solvent comprises material selected from the group consisting of carbon dioxide, hexane, propane, pentane and butane.

References Cited (Backward Citations)

US3969196A Cited
US4125459A Cited
US4191639A Cited
US4349415A Cited
US4375387A Cited
US4358365A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1988-07-08 1989-01-07 1989-07-09 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1992-07-08 1993-01-07 1993-07-09 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1996-07-08 1997-01-07 1997-07-09 $7700.00 Window Closed / Lapsed

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