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US3968023A Expired / Lapsed US ⏱️ 0.0 years remaining

Production of lubricating oils

Assignee: Mobil Oil AS
•
Filing: 1975-01-30
•
Granted: 1976-07-06
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Expires: 1995-01-30
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Abstract

Abstract Residual oils are upgraded to lube oil base stocks by a combination process involving deasphalting, solvent extraction and hydrocracking arranged to particularly promote the efficient production of lube oil products.

Inventors

  • 👤 Tsoung-Yuan Yan

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 11:39
CPC Classifications
C; C10; C10G; C10G67/00; C10G67/02; C10G67/14; C10G2400/00; C10G2400/10

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 241 words
A method for producing lube oils from an atmospheric residual oil which comprises, separating an atmospheric residual oil to recover a light vacuum gas oil, a heavy vacuum gas oil and a resid containing asphaltic material, deasphalting said resid to provide a first raffinate product thereof, solvent extraction said light vacuum gas oil to provide a second raffinate phase and a first extract phase, separating solvent from said extracted light vacuum gas oil, combining said first extract phase with said first raffinate product of said resid deasphalting operation to form a mixed oil phase comprising solvent with extracted polycyclic aromatics, using said mixed oil extract phase with solvent to remove undesired aromatics from said heavy vacuum gas oil in a second solvent extraction zone, recovering a second extract phase from said second solvent extraction zone and separating solvent from aromatics in said second extract phase, recycling solvent thus separated to said second solvent extraction zone, recovering a third raffinate phase from said second solvent extraction zone and separating solvent from an oil phase comprising said third raffinate and boiling above about 800°F., recycling solvent thus separated to said second extraction zone, passing said oil phase boiling above about 800°F. to a hydrocracking zone maintained under relatively mild hydrocracking conditions selected to enhance the yield of lube oil base products and separating a product of said hydrocracking operation boiling above about 650°F into a plurality of separate boiling range lube oil fractions.
Claim 2
Independent Claim 241 words
A method for producing lube oils from an atmospheric residual oil which comprises, separating an atmospheric residual oil to recover a light vacuum gas oil, a heavy vacuum gas oil and a resid containing asphaltic material, deasphalting said resid to provide a first raffinate product thereof, solvent extraction said light vacuum gas oil to provide a second raffinate phase and a first extract phase, separating solvent from said extracted light vacuum gas oil, combining said first extract phase with said first raffinate product of said resid deasphalting operation to form a mixed oil phase comprising solvent with extracted polycyclic aromatics, using said mixed oil extract phase with solvent to remove undesired aromatics from said heavy vacuum gas oil in a second solvent extraction zone, recovering a second extract phase from said second solvent extraction zone and separating solvent from aromatics in said second extract phase, recycling solvent thus separated to said second solvent extraction zone, recovering a third raffinate phase from said second solvent extraction zone and separating solvent from an oil phase comprising said third raffinate and boiling above about 800°F., recycling solvent thus separated to said second extraction zone, passing said oil phase boiling above about 800°F. to a hydrocracking zone maintained under relatively mild hydrocracking conditions selected to enhance the yield of lube oil base products and separating a product of said hydrocracking operation boiling above about 650°F into a plurality of separate boiling range lube oil fractions.
Claim 3
Dependent Claim 36 words
The method of claim 1 wherein fresh furfural solvent is added to said first solvent extraction zone and is cascaded with solvent removed aromatics to said second solvent extraction zone processing a heavy vacuum gas oil.
Claim 4
Dependent Claim 43 words
The method of claim 1 wherein the raffinate product of solvent refined light vacuum gas oil separated from solvent and the 650°F plus lube oil products of the hydrocracking operation are blended for the production of turbine oil and multi-grade automotive lube oils.
Claim 5
Dependent Claim 48 words
The method of claim 1 wherein the product of hydrocracking boiling above about 650°F is separated to recover a first lube oil fraction boiling in the range of 650°to 850°F, a second lube oil fraction boiling in the range of 850°-1000°F and a third fraction boiling above 1000°F.
Claim 6
Dependent Claim 17 words
The method of claim 4 wherein one or more of the separated lube oil fractions are dewaxed.

References Cited (Backward Citations)

US2886523A Cited
US2847353A Cited
US3349028A Cited
US3723295A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-07-06 1980-01-05 1980-07-06 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-07-06 1984-01-05 1984-07-06 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-07-06 1988-01-05 1988-07-06 $7700.00 Window Closed / Lapsed

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