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US4514283A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for separating and converting heavy oil asphaltenes in a field location

Assignee: Shell USA Inc
•
Filing: 1984-01-26
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Granted: 1985-04-30
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Expires: 2004-01-26
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Abstract

Abstract Viscous asphaltenic crude oils are converted to pumpable liquid oil products in field locations by precipitating and separating asphaltenes, then mildly thermally converting the asphaltenes to mobile asphaltene-conversion products that can be mixed with at least the maltene components of the crude oils to form the pumpable liquid oil products.

Inventors

  • 👤 Philip J. Closmann
  • 👤 Monroe H. Waxman
  • 👤 Charles T. Deeds

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 11:09
CPC Classifications
C; C10; C10G; C10G53/00; C10G53/02; C10G53/04; C10G55/00; C10G55/02; C10G55/04

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 182 words
A process for treating at least the relatively high boiling components of an asphaltenic viscous crude oil in a field location, in order to produce a pumpable liquid oil product, comprising: mixing the crude oil or its heavy ends with an asphaltene precipitating agent at least as effective for asphaltene precipitation as normal heptane and recovering at least a portion of the precipitated asphaltenic components of the crude oil; thermally converting the recovered asphaltenic components to non-viscous liquid asphaltenic conversion products by heating said recovered asphaltenic components at a pressure of from about one to three atmospheres for a time and temperature substantially as effective as heating said recovered asphaltenic components at substantially atmospheric pressure at from about 625° F. to 700° F. for from about one to three days; and mixing products of said conversion comprising the non-viscous liquid asphaltenic conversion products with at least the maltene components of the crude oil or its heavy ends from which asphaltenic components were precipitated in order to form a pumpable liquid oil product having a viscosity of no more than about 10,000 centipoise.
Claim 2
Dependent Claim 182 words
A process for treating at least the relatively high boiling components of an asphaltenic viscous crude oil in a field location, in order to produce a pumpable liquid oil product, comprising: mixing the crude oil or its heavy ends with an asphaltene precipitating agent at least as effective for asphaltene precipitation as normal heptane and recovering at least a portion of the precipitated asphaltenic components of the crude oil; thermally converting the recovered asphaltenic components to non-viscous liquid asphaltenic conversion products by heating said recovered asphaltenic components at a pressure of from about one to three atmospheres for a time and temperature substantially as effective as heating said recovered asphaltenic components at substantially atmospheric pressure at from about 625° F. to 700° F. for from about one to three days; and mixing products of said conversion comprising the non-viscous liquid asphaltenic conversion products with at least the maltene components of the crude oil or its heavy ends from which asphaltenic components were precipitated in order to form a pumpable liquid oil product having a viscosity of no more than about 10,000 centipoise.
Claim 3
Dependent Claim 14 words
The process of claim 1 in which the asphaltene precipitating agent is normal pentane.
Claim 4
Dependent Claim 17 words
The process of claim 1 in which the asphaltene precipitating agent is more volatile than normal pentane.
Claim 5
Dependent Claim 14 words
The process of claim 1 in which the crude oil is Peace River tar.
Claim 6
Dependent Claim 15 words
The process of claim 4 in which the asphaltenes are heated for about three days.

References Cited (Backward Citations)

US2875149A Cited
US3369992A Cited
US3775293A Cited
US4172026A Cited
US4391701A Cited
US4428824A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1988-04-29 1988-10-29 1989-04-30 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1992-04-29 1992-10-29 1993-04-30 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1996-04-29 1996-10-29 1997-04-30 $7700.00 Window Closed / Lapsed

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