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US4101415A Expired / Lapsed US ⏱️ 0.0 years remaining

Solvent deasphalting

Assignee: Phillips Petroleum Co
•
Filing: 1977-03-14
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Granted: 1978-07-18
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Expires: 1997-03-14
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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 08:08
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)

US2691621A Cited
US3311551A Cited
US3563778A Cited
US3830732A Cited

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

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