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US4455216A Expired / Lapsed US ⏱️ 0.0 years remaining

Polarity gradient extraction method

Assignee: Mobil Oil AS
•
Filing: 1980-12-04
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Granted: 1984-06-19
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Expires: 2000-12-04
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Abstract

Abstract An improved method for recovering and deasphalting tar sands comprises the use of at least two solvents in an extraction column to establish a liquid polarity gradient within it.

Inventors

  • 👤 Philip J. Angevine
  • 👤 Michael B. Carroll
  • 👤 Stuart S. Shih
  • 👤 Samuel A. Tabak

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-09 03:02
CPC Classifications
B; B01; B01D; B01D11/00; B01D11/02; B01D11/0203; C; C10; C10G; C10G1/00; C10G1/04

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 113 words
A process for recovering and deasphalting tar sands in an extraction column comprising contacting said tar sands with solvent under conditions to produce bitumen as an overhead phase, wherein in said process said tar sands are contacted with at least two polar solvents, said polar solvents being selected from the group consisting of a hydrocarbon containing 3 to 7 carbon atoms, mixtures thereof or a 200° F.-300° F. naphtha fraction, the least polar of which is injected into said column at a point nearest the bitumen taken-off stream point and the most polar of which is injected into said column at a point nearest the exit point of by-product comprising sand and asphalt.
Claim 2
Dependent Claim 113 words
A process for recovering and deasphalting tar sands in an extraction column comprising contacting said tar sands with solvent under conditions to produce bitumen as an overhead phase, wherein in said process said tar sands are contacted with at least two polar solvents, said polar solvents being selected from the group consisting of a hydrocarbon containing 3 to 7 carbon atoms, mixtures thereof or a 200° F.-300° F. naphtha fraction, the least polar of which is injected into said column at a point nearest the bitumen taken-off stream point and the most polar of which is injected into said column at a point nearest the exit point of by-product comprising sand and asphalt.
Claim 3
Dependent Claim 35 words
The process of claim 1 wherein said least polar solvent is a mixture of C 3 and C 4 hydrocarbons and said most polar solvent is a mixture of C 4 and C 5 hydrocarbons.
Claim 4
Dependent Claim 19 words
The process of claim 1 wherein the least polar solvent is n-pentane and the most polar solvent is toluene.
Claim 5
Dependent Claim 13 words
The process of claim 1 wherein the total solvent/tar sands ratio exceeds 0.5:1.
Claim 6
Dependent Claim 19 words
The process of claim 4 wherein said ratio is in the range of from about 1:1 to about 10:1.
Claim 7
Dependent Claim 17 words
The process of claim 1 wherein the temperature ranges from about -30° F. to about 400° F.
Claim 8
Dependent Claim 17 words
The process of claim 1 wherein the column pressure ranges from about 0 to about 2,000 psig.

References Cited (Backward Citations)

US2871180A Cited
US3321394A Cited
US4046668A Cited
US4189376A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1987-06-19 1987-12-19 1988-06-19 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1991-06-19 1991-12-19 1992-06-19 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1995-06-19 1995-12-19 1996-06-19 $7700.00 Window Closed / Lapsed

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