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US4054512A Expired / Lapsed US ⏱️ 0.0 years remaining

Deasphalting with liquid hydrogen sulfide

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1976-10-22
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Granted: 1977-10-18
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Expires: 1996-10-22
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Abstract

Abstract An asphalt-containing mineral oil is deasphalted by contacting the oil with a liquid hydrogen sulfide deasphalting solvent for a time sufficient to remove a substantial portion of the asphalt from the oil. Utilization of liquid hydrogen sulfide as the deasphalting solvent is capable of giving high yields of deasphalted oil. In contrast to the use of aliphatic solvents for deasphalting, the hydrogen sulfide readily mixes with the heavy feed even at relatively low temperatures.

Inventors

  • 👤 John J. Dugan
  • 👤 Jackson Eng

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 14:20
CPC Classifications
C; C10; C10G; C10G21/00; C10G21/003

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 36 words
A process for deasphalting an asphalt-containing mineral oil which comprises contacting said oil with a liquid hydrogen sulfide deasphalting solvent to form two liquid-liquid immiscible phases, a solvent phase containing deasphalted oil and an asphalt phase.
Claim 2
Dependent Claim 36 words
A process for deasphalting an asphalt-containing mineral oil which comprises contacting said oil with a liquid hydrogen sulfide deasphalting solvent to form two liquid-liquid immiscible phases, a solvent phase containing deasphalted oil and an asphalt phase.
Claim 3
Dependent Claim 24 words
The process of claim 1 wherein said contacting is carried out at a temperature ranging from about -76° F to just below 212° F.
Claim 4
Dependent Claim 44 words
The process of claim 2 wherein said mineral oil is selected from the group consisting essentially of whole crude oils, topped crude oils and heavy petroleum oil fractions having an initial boiling point ranging from about 650° F to 1100° F at atmospheric pressure.
Claim 5
Dependent Claim 18 words
The process of claim 3 wherein said heavy petroleum oil fraction is a vacuum or an atmospheric residuum.
Claim 6
Dependent Claim 17 words
The process of claim 3 wherein the solvent/oil liquid volume ratio ranges from about 2 to 20.
Claim 7
Dependent Claim 63 words
A solvent deasphalting process which comprises contacting an asphalt-containing petroleum oil with a solvent consisting essentially of liquid hydrogen sulfide for a time sufficient to precipitate a substantial portion of said asphalt from said oil thereby forming two liquid-liquid immiscible phases, a solvent phase containing deasphalted oil and an asphalt phase, separating said phases and recovering a deasphalted oil from said solvent phase.
Claim 8
Dependent Claim 63 words
A solvent deasphalting process which comprises contacting an asphalt-containing petroleum oil with a solvent consisting essentially of liquid hydrogen sulfide for a time sufficient to precipitate a substantial portion of said asphalt from said oil thereby forming two liquid-liquid immiscible phases, a solvent phase containing deasphalted oil and an asphalt phase, separating said phases and recovering a deasphalted oil from said solvent phase.
Claim 9
Dependent Claim 24 words
The process of claim 6 wherein said contacting is carried out at a temperature ranging from about -76° F to just below 212° F.
Claim 10
Dependent Claim 44 words
The process of claim 7 wherein said petroleum oil is selected from the group consisting essentially of whole crude oils, topped crude oils and heavy petroleum oil fractions having an initial boiling point ranging from about 650° F to 1100° F at atmospheric pressure.
Claim 11
Dependent Claim 18 words
The process of claim 8 wherein said heavy petroleum oil fraction is a vacuum or an atmospheric residuum.
Claim 12
Dependent Claim 17 words
The process of claim 8 wherein the ratio of solvent to oil ranges from 2 to 20.

References Cited (Backward Citations)

US2163245A Cited
US3472760A Cited
US3622505A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-10-17 1981-04-18 1981-10-18 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-10-17 1985-04-18 1985-10-18 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-10-17 1989-04-18 1989-10-18 $7700.00 Window Closed / Lapsed

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