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US3616209A Expired / Lapsed US ⏱️ 0.0 years remaining

Solvent extraction process

Assignee: BP PLC
•
Filing: 1968-01-24
•
Granted: 1971-10-26
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Expires: 1988-01-24
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Abstract

Abstract Solvent extraction of a solid material which is contaminated with at least one hydrocarbon and water which comprises, in a first extraction stage consisting of one or more extraction steps, extracting a contaminated solid material with a mixture of an alcohol and a hydrocarbon with which it forms an azeotrope, the alcohol and azeotrope forming hydrocarbon respectively being employed at a ratio by volume within the range 30:70 to 70:30. Preferably in a second extraction stage consisting of one or more extraction steps, following the first extraction stage, the treated solid material from the first stage is extracted with a solvent comprising or consisting of the alcohol, thereafter recovering the treated solid material. Suitably the azeotrope-forming hydrocarbon is normal hexane. Suitably the alcohol is ethanol, propanol, isopropanol or a butanol. Suitably the process of the invention is applied to a crude or partially refined product of the growth of a micro-organism on a hydrocarbon substrate in the presence of an aqueous nutrient medium. Preferably the micro-organism is a yeast.

Inventors

  • 👤 Bernard Maurice Laine
  • 👤 Jean Claude Hondermarck
  • 👤 Robert Goux

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 16:20
CPC Classifications
B; B01; B01D; B01D3/00; B01D3/34; B01D3/36; C; C12; C12N; C12N1/00; C12N1/02

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 124 words
A process according to claim 1 wherein the extract fractions recovered from the extraction stages are fed, separately or after blending, to a distillation stage, consisting of one or more distillation steps, for the separate recovery of (a) an azeotropic mixture of the alcohol and the azeotrope-forming hydrocarbon, (b) an azeotropic mixture of the alcohol and water and (c) a residue fraction, thereafter blending part of the azeotropic mixture of the alcohol and water with part of the azeotropic mixture of the alcohol and azeotrope-forming hydrocarbon, the parts being selected to give a mixture of the alcohol and azeotrope-forming hydrocarbon containing these materials respectively at a ratio by volume in the range 30:70 to 70:30 and recycling this mixture to the first extraction stage.
Claim 2
Dependent Claim 13 words
A process according to claim 1 which the azeotrope-forming hydrocarbon is normal hexane.
Claim 3
Dependent Claim 17 words
A process according to claim 1 in which the alcohol is ethanol, propanol, isopropanol or a butanol.
Claim 4
Dependent Claim 25 words
A process according to claim 1 in which at least one solvent extraction step is carried out at a temperature in the range 30*-100* C.
Claim 5
Dependent Claim 30 words
A process according to claim 1 in which the micro-organism contains at least 20 percent of water in excess of the water present in the micro-organism in the dry state.

References Cited (Backward Citations)

No citation records indexed.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1974-10-25 1975-04-26 1975-10-26 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1978-10-25 1979-04-26 1979-10-26 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1982-10-25 1983-04-26 1983-10-26 $7700.00 Window Closed / Lapsed

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