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US4035287A Expired / Lapsed US ⏱️ 0.0 years remaining

Desulfurization of residual oil

Assignee: Mobil Oil AS
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Filing: 1975-08-25
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Granted: 1977-07-12
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Expires: 1995-08-25
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Abstract

Abstract A method is provided for desulfurization of oil stock, e.g. residual oil, having a minimum sulfur content of about 2 weight percent and a minimum metals content of about 50 ppm to produce a low-sulfur, high-metals content raffinate and a high-sulfur, low-metals content extract which comprises contacting said oil stock with a solvent selective for low molecular weight aromatics and having a boiling point within the range of from about 0 DEG F to about 100 DEG F and a density greater than or less than the density of the oil stock being contacted by at least 0.1 g/cc, said contacting being conducted at a temperature of from about 60 DEG F to about 212 DEG F, a solvent/oil stock volume ratio of from about 0.25 to about 10 and a pressure higher than the vapor pressure of the solvent at the contacting temperature, and separating the low-sulfur, high-metals content raffinate from the high-sulfur, low-metals content extract.

Inventors

  • 👤 Wilton F. Espenscheid
  • 👤 Tsoung-Yuan Yan

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-09 04:32
CPC Classifications
C; C10; C10G; C10G21/00; C10G21/06; C10G21/08; C10G21/10

Claims Analysis

Total Claims: 13
Claim 1
Independent Claim 103 words
A method for desulfurization of an oil stock having a minimum sulfur content of about 2 weight percent and a minimum metals content of about 50 ppm to produce a low-sulfur, high-metals content raffinate and a high-sulfur, low-metals content extract which comprises contacting said oil stock with liquid sulfur dioxide solvent at a temperature of from about 60° F. to about 212° F., a solvent/oil stock volume ratio of from about 0.25 to about 10 and a pressure higher than the vapor pressure of the solvent at the contacting temperature, and separating the low-sulfur, high-metals content raffinate from the high-sulfur, low-metals content extract.
Claim 2
Independent Claim 103 words
A method for desulfurization of an oil stock having a minimum sulfur content of about 2 weight percent and a minimum metals content of about 50 ppm to produce a low-sulfur, high-metals content raffinate and a high-sulfur, low-metals content extract which comprises contacting said oil stock with liquid sulfur dioxide solvent at a temperature of from about 60° F. to about 212° F., a solvent/oil stock volume ratio of from about 0.25 to about 10 and a pressure higher than the vapor pressure of the solvent at the contacting temperature, and separating the low-sulfur, high-metals content raffinate from the high-sulfur, low-metals content extract.
Claim 3
Dependent Claim 35 words
The method of claim 1 wherein the contacting is conducted at a temperature of from about 70° F. to about 120° F. and a solvent/oil stock volume ratio of from about 0.5 to about 3.
Claim 4
Dependent Claim 27 words
The method of claim 1 wherein said oil stock is a residual oil having a total metals content of from about 50 ppm to about 150 ppm.
Claim 5
Dependent Claim 18 words
The method of claim 3 wherein said metals content is from about 50 ppm to about 100 ppm.
Claim 6
Dependent Claim 35 words
The method of claim 3 wherein the contacting is conducted at a temperature of from about 70° F. to about 120° F. and a solvent/oil stock volume ratio of from about 0.5 to about 3.
Claim 7
Dependent Claim 35 words
The method of claim 4 wherein the contacting is conducted at a temperature of from about 70° F. to about 120° F. and a solvent/oil stock volume ratio of from about 0.5 to about 3.
Claim 8
Dependent Claim 21 words
The method of claim 1 wherein said oil stock is a high boiling range residual oil boiling above about 600° F.
Claim 9
Dependent Claim 35 words
The method of claim 7 wherein the contacting is conducted at a temperature of from about 70° F. to about 120° F. and a solvent/oil stock volume ratio of from about 0.5 to about 3.
Claim 10
Dependent Claim 39 words
The method of claim 1 wherein said oil stock comprises at least a substantial part of one obtained by fractionation of a crude oil identified as Pennsylvania, Midcontinent, Gulf Coast, West Texas, Amal, Agha Jari, Kuwait, Barco or Arabian.
Claim 11
Dependent Claim 35 words
The method of claim 9 wherein the contacting is conducted at a temperature of from about 70° F. to about 120° F. and a solvent/oil stock volume ratio of from about 0.5 to about 3.
Claim 12
Dependent Claim 21 words
The method of claim 1 wherein said oil stock is one obtained by fractionation of crude oil identified as Agha Jari.
Claim 13
Dependent Claim 35 words
The method of claim 11 wherein the contacting is conducted at a temperature of from about 70° F. to about 120° F. and a solvent/oil stock volume ratio of from about 0.5 to about 3.

References Cited (Backward Citations)

US2646390A Cited
US2866689A Cited
US2943050A Cited
US3294678A Cited
US3511774A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-07-11 1981-01-10 1981-07-12 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-07-11 1985-01-10 1985-07-12 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-07-11 1989-01-10 1989-07-12 $7700.00 Window Closed / Lapsed

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