Patent US4101415A successfully refreshed from Google Patents.
US4101415A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Solvent deasphalting
Assignee: Phillips Petroleum Co
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Filing: 1977-03-14
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Granted: 1978-07-18
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Expires: 1997-03-14
Abstract
Abstract Heavy hydrocarbon materials containing asphalt are separated into three different fractions according to chemical composition, namely, a paraffin-waxy fraction, a resin fraction, and an asphaltene-solids fraction, by a process comprising two-stage solvent treatment at different solvent-to-feed ratios and different temperatures. In another embodiment, a fourth product comprising an asphalt fraction can be produced by blending a portion of the resin fraction with a portion of the raffinate obtained from the first solvent extraction fraction stage.
Inventors
- 👤 Ralph P. Crowley
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 13:41
CPC Classifications
C; C10; C10G; C10G21/00; C10G21/003; B; B01; B01D; B01D11/00; B01D11/04; B01D11/0403; B01D11/0407; C10C; C10C1/00; C10C1/18; C10C3/00; C10C3/08
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
268 words
A process for producing a paraffinic-waxy fraction, a resin-naphthenic fraction, and a solids-asphaltene fraction from an asphalt-containing heavy hydrocarbon material which comprises the steps of: (a) contacting a hydrocarbon charge stock containing asphaltic materials and resins with a first portion of a selective solvent comprising light paraffins and mixtures thereof at a relatively low solvent-to-hydrocarbon volumetric ratio in the range of 2:1 to 10:1 and under extraction conditions of temperature and pressure sufficient to separate a first solvent-rich extract fraction containing paraffins and waxy materials and a first solvent-lean raffinate fraction containing resins, naphthenes, and asphaltene, (b) separating paraffinic waxy materials from said first solvent-rich extract phase and recovering a paraffinic waxy phase and solvent, (c) contacting said first solvent-lean raffinate fraction with a second portion of said selective solvent at a solvent-to-hydrocarbon volumetric ratio higher than said ratio in (a) and at a temperature and pressure lower than in (a) such that asphaltic solids are formed in the presence of a large excess of solvent and that substantially all soluble materials are dissolved in a second solvent-rich extract phase, (d) passing the admixture formed in (c) to a liquid-solids phase separation zone and allowing the admixture to phase separate into a heavy solids-containing phase and a solvent-hydrocarbon phase relatively free from asphaltenes, (e) separating a resin extract fraction from said solvent-hydrocarbon phase of (d) and recovering a resin fraction and solvent, and (f) passing said heavy solids-containing phase to a flashing zone and therein subjecting same to flashing conditions of temperature and pressure sufficient to separate residual solvent therefrom and yield a powdered asphaltic product comprising asphaltenes.
Claim 2
Dependent Claim
268 words
A process for producing a paraffinic-waxy fraction, a resin-naphthenic fraction, and a solids-asphaltene fraction from an asphalt-containing heavy hydrocarbon material which comprises the steps of: (a) contacting a hydrocarbon charge stock containing asphaltic materials and resins with a first portion of a selective solvent comprising light paraffins and mixtures thereof at a relatively low solvent-to-hydrocarbon volumetric ratio in the range of 2:1 to 10:1 and under extraction conditions of temperature and pressure sufficient to separate a first solvent-rich extract fraction containing paraffins and waxy materials and a first solvent-lean raffinate fraction containing resins, naphthenes, and asphaltene, (b) separating paraffinic waxy materials from said first solvent-rich extract phase and recovering a paraffinic waxy phase and solvent, (c) contacting said first solvent-lean raffinate fraction with a second portion of said selective solvent at a solvent-to-hydrocarbon volumetric ratio higher than said ratio in (a) and at a temperature and pressure lower than in (a) such that asphaltic solids are formed in the presence of a large excess of solvent and that substantially all soluble materials are dissolved in a second solvent-rich extract phase, (d) passing the admixture formed in (c) to a liquid-solids phase separation zone and allowing the admixture to phase separate into a heavy solids-containing phase and a solvent-hydrocarbon phase relatively free from asphaltenes, (e) separating a resin extract fraction from said solvent-hydrocarbon phase of (d) and recovering a resin fraction and solvent, and (f) passing said heavy solids-containing phase to a flashing zone and therein subjecting same to flashing conditions of temperature and pressure sufficient to separate residual solvent therefrom and yield a powdered asphaltic product comprising asphaltenes.
Claim 3
Dependent Claim
23 words
A process according to claim 1 wherein the solvent separated in steps (b), (e), and (f) is recycled to steps (a) and (c).
Claim 4
Dependent Claim
36 words
A process according to claim 1 wherein the solvent in steps (a) and (c) is the same and is a mixture of propane and butane and the solvent-to-hydrocarbon volumetric ratio in (c) is at least 20:1.
Claim 5
Dependent Claim
38 words
A process according to claim 1 wherein at least a portion of the first solvent-lean raffinate fraction (a) and at least a portion of the resin fraction recovered in (e) are blended to form an asphalt product fraction.
Claim 6
Dependent Claim
58 words
A process according to claim 1 wherein the solvent in steps (a) and (c) is the same and is a mixture of propane and butane and the solvent-to-hydrocarbon volumetric ratio in (c) is at least 20:1, with the further proviso that the solvent separated in steps (b), and (e), and (f) is recycled to steps (a) and (c).
Claim 7
Dependent Claim
39 words
A process according to claim 5 wherein at least a portion of said first solvent-lean raffinate fraction in (a) and at least a portion of the resin fraction recovered in (e) are blended to form an asphalt product fraction.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-07-17 | 1982-01-16 | 1982-07-18 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-07-17 | 1986-01-16 | 1986-07-18 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-07-17 | 1990-01-16 | 1990-07-18 | $7700.00 | Window Closed / Lapsed |