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US3960705A Expired / Lapsed US ⏱️ 0.0 years remaining

Conversion of foots oil to lube base stocks

Assignee: Mobil Oil AS
•
Filing: 1975-06-17
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Granted: 1976-06-01
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Expires: 1995-06-17
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Abstract

Abstract Foots oil, the by-product left when high quality wax is recovered by a solvent dewaxing process, is usually used as cracker feed stock. There is disclosed a method of converting it to higher quality lubricant base stock by subjecting such to catalytic hydroprocessing utilizing a ZSM-5 or similarly behaving zeolite catalyst under hydrogen pressure followed by distillation of the product to remove light products such as naphtha, LPG and No. 2 fuel oil therefrom.

Inventors

  • 👤 William E. Garwood
  • 👤 John J. Wise

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 23:27
CPC Classifications
C; C10; C10G; C10G35/00; C10G35/04; C10G35/06; C10G35/095; C10G2400/00; C10G2400/10

Claims Analysis

Total Claims: 3
Claim 1
Independent Claim 189 words
In the process of producing a lubricant base stock and wax from a distillate fraction boiling in the range of about 650° to 1100°F by the sequnce of processing comprising dearomatizing such distillate by solvent extraction, dewaxing said dearomatized distillate by ketone extraction to produce a first product comprising wax and a second product comprising lubricant base stock, and deoiling said first product to produce a hard wax and Foots oil; the improvement which comprises contacting said Foots oil with a crystalline aluminosilicate zeolite having a silica to alumina ratio of at least about 15, a constraint index of 1 to 12, a crystal density of not substantially below about 1.6 grams per cubic centimeter and a hydrogenation/dehydrogenation component in a proportion of up to about 10 weight percent, said contact being carried out at about 500° to 800°F, about 0.5 to 20 LHSV, under a hydrogen pressure of about 250 to 750 psig, and at a hydrogen circulation rate of about 500 to 2,500 SCFB and resolving the product of such contact into at least a lubricant base stock fraction and a light fraction comprising LPG and naphtha.
Claim 2
Dependent Claim 189 words
In the process of producing a lubricant base stock and wax from a distillate fraction boiling in the range of about 650° to 1100°F by the sequnce of processing comprising dearomatizing such distillate by solvent extraction, dewaxing said dearomatized distillate by ketone extraction to produce a first product comprising wax and a second product comprising lubricant base stock, and deoiling said first product to produce a hard wax and Foots oil; the improvement which comprises contacting said Foots oil with a crystalline aluminosilicate zeolite having a silica to alumina ratio of at least about 15, a constraint index of 1 to 12, a crystal density of not substantially below about 1.6 grams per cubic centimeter and a hydrogenation/dehydrogenation component in a proportion of up to about 10 weight percent, said contact being carried out at about 500° to 800°F, about 0.5 to 20 LHSV, under a hydrogen pressure of about 250 to 750 psig, and at a hydrogen circulation rate of about 500 to 2,500 SCFB and resolving the product of such contact into at least a lubricant base stock fraction and a light fraction comprising LPG and naphtha.
Claim 3
Dependent Claim 12 words
The process claimed in claim 1 including blending such lubricant base stocks.

References Cited (Backward Citations)

US3046218A Cited
US3597473A Cited
US3700585A Cited
US3702886A Cited
US3804746A Cited
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US3729409A Cited
US3753891A Cited
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USPTO Annuity & Maintenance Windows

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

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