US3940281A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Asphalt composition utilizing asphaltene concentrate
Assignee: ExxonMobil Technology and Engineering Co
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Filing: 1973-11-23
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Granted: 1976-02-24
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Expires: 1993-11-23
Abstract
Abstract An asphaltene concentrate obtained by liquid hydrocarbon fractionation of an asphaltic residuum is blended with a petroleum fraction containing alkylated naphthenes and/or alkylated aromatics such as a vacuum distilled gas oil, a naphthene-aromatic fraction of a gas oil, or a solvent extract of a lubricating oil fraction, thereby producing a high quality paving composition.
Inventors
- 👤 Luke W. Corbett
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 02:35
CPC Classifications
C; C10; C10C; C10C3/00; C10C3/005
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
97 words
An asphaltic composition comprising one volume of an asphaltene concentrate containing from 40 to 90 wt. % of heptane-insoluble asphaltenes and from 10 to 60 wt. % of polar aromatics derived from an asphaltic residuum, blended with from one to four volumes of a petroleum fraction selected from the group consisting of an aromatic solvent extract of a lubricating oil fraction, said extract having a viscosity index below 30, a vacuum gas oil having a boiling range within the limits of about 600° to 1200°F. atmospheric equivalent vapor temperatures, and a naphthene-aromatic fraction of a gas oil.
Claim 2
Dependent Claim
97 words
An asphaltic composition comprising one volume of an asphaltene concentrate containing from 40 to 90 wt. % of heptane-insoluble asphaltenes and from 10 to 60 wt. % of polar aromatics derived from an asphaltic residuum, blended with from one to four volumes of a petroleum fraction selected from the group consisting of an aromatic solvent extract of a lubricating oil fraction, said extract having a viscosity index below 30, a vacuum gas oil having a boiling range within the limits of about 600° to 1200°F. atmospheric equivalent vapor temperatures, and a naphthene-aromatic fraction of a gas oil.
Claim 3
Dependent Claim
19 words
Composition as defined by claim 1 wherein said asphaltene concentrate also contains up to 10 wt. % of naphthene-aromatics.
Claim 4
Dependent Claim
31 words
Compositions as defined by claim 1 wherein said asphaltene concentrate contains from 55 to 80 wt. % of heptane insoluble asphaltenes and from 20 to 45 wt. % of polar aromatics.
Claim 5
Dependent Claim
34 words
Composition as defined by claim 1 wherein said asphaltene concentrate has been obtained by treatment of an asphaltic residuum with normal pentane or isopentane or a mixture thereof at an elevated temperature and pressure.
Claim 6
Dependent Claim
152 words
A process for preparing an asphaltic composition which comprises the steps of subjecting an asphaltic residuum to a solvent fractionation with a C 4 to C 9 hydrocarbon under conditions of elevated temperature and pressure whereby there is obtained an asphaltene concentrate containing from 40 to 90 wt. % of heptane insoluble asphaltenes and from 10 to 60 wt. % of polar aromatics; thereafter blending one volume of said concentrate with from one to four volumes of a petroleum fraction containing alkylated naphthenes and/or alkylated aromatics, said fraction being selected from the group consisting of an aromatic solvent extract of a lubricating oil, a vacuum gas oil, and a naphthene aromatic fraction of a gas oil; whereby there is obtained an asphalt of improved specification quality in lower yield based on crude oil volume as compared with an asphalt of the same penetration grade obtained from the crude oil by conventional distillation.
Claim 7
Dependent Claim
152 words
A process for preparing an asphaltic composition which comprises the steps of subjecting an asphaltic residuum to a solvent fractionation with a C 4 to C 9 hydrocarbon under conditions of elevated temperature and pressure whereby there is obtained an asphaltene concentrate containing from 40 to 90 wt. % of heptane insoluble asphaltenes and from 10 to 60 wt. % of polar aromatics; thereafter blending one volume of said concentrate with from one to four volumes of a petroleum fraction containing alkylated naphthenes and/or alkylated aromatics, said fraction being selected from the group consisting of an aromatic solvent extract of a lubricating oil, a vacuum gas oil, and a naphthene aromatic fraction of a gas oil; whereby there is obtained an asphalt of improved specification quality in lower yield based on crude oil volume as compared with an asphalt of the same penetration grade obtained from the crude oil by conventional distillation.
Claim 8
Dependent Claim
23 words
Process as defined by claim 5 wherein the hydrocarbon used in the solvent fractionation is normal pentane or isopentane or a mixture thereof.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1979-02-23 | 1979-08-25 | 1980-02-24 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-02-23 | 1983-08-25 | 1984-02-24 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-02-23 | 1987-08-25 | 1988-02-24 | $7700.00 | Window Closed / Lapsed |