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US3793191A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for manufacturing lubricating oil

Assignee: INST PETROLE CARBURANTS LUBRIF
•
Filing: 1972-04-06
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Granted: 1974-02-19
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Expires: 1992-04-06
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Abstract

Abstract A process for manufacturing a lubricating oil comprising a first step of passing a deasphalted crude oil distillation residue containing by weight at least 85 percent of constituents boiling above 500*C and at least 75 percent of consituents boiling above 525*C, with hydrogen over a hydrogenating catalyst with a cracking carrier at 330*-450*C, at a hydrogen partial pressure of 80-240 kg/cm2, at such a flow rate that the hydrocarbons in the resulting product boiling below 525*C amount to 70-95 percent of the initial weight of such hydrocarbons, separating the products boiling below 525*C, and recovering a first lubricating oil fraction of high V.I. and a second step of passing at least a portion of the products boiling above 525*C over a similar catalyst, at the same temperature and pressure ranges of the first step, at such a flow rate that the major part of the first zone heavy products are converted to products boiling below 525*C and separating therefrom, by distillation, a second lubricating oil fraction.

Inventors

  • 👤 A Billon
  • 👤 M Derrien

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 13:27
CPC Classifications
C; C10; C10G; C10G65/00; C10G65/02; C10G65/10; C10G2400/00; C10G2400/10

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 44 words
A process according to claim 1, wherein the operating conditions in the first catalytic zone are such that the weight of the hydrocarbons boiling below 525*C, in the resulting product, amounts to from 85 to 92 percent of the initial weight of such hydrocarbons.
Claim 2
Dependent Claim 34 words
A process according to claim 1, wherein the deasphalted residue has an initial boiling point higher than 300*C, and contains at least 90 percent by weight constituents having a boiling point higher than 500*C.
Claim 3
Dependent Claim 21 words
A process according to claim 3, wherein the deasphalted residue has a viscosity at 98.9*C of from 5 to 100 centistokes.
Claim 4
Dependent Claim 59 words
A process according to claim 4, wherein the deasphalted residue has a viscosity of from 5 to 50 centistokes at 98.9* C., a viscosity index of from 0 to 100, a maximum content of asphaltenes of 0.3 percent by weight, a nitrogen content lower than 0.3 percent by weight and a maximum Conradson carbon of 5 percent by weight.
Claim 5
Dependent Claim 48 words
A process according to claim 1, wherein the flow rate of liquid charge is from 0.1 to 2 liters per liter of catalyst per hour and the hydrogen flow rate is from 500 to 5,000 liters per liter of liquid charge in each of the two catalytic zones.
Claim 6
Dependent Claim 27 words
A process according to claim 1, further comprising blending the first and second lubricating oil fractions, so as to obtain a blend of high V.I. lubricating oils.
Claim 7
Dependent Claim 40 words
A process according to claim 1 wherein the flow rate of the liquid charge in the second catalytic zone, expressed in liters per liter of catalyst per hour, is from 1.2 to 2 times that of the first catalytic zone.
Claim 8
Dependent Claim 27 words
A process according to claim 1, wherein the temperature in the second catalytic zone is 10* to 100*C lower than the temperature in the first catalytic zone.

References Cited (Backward Citations)

US3242068A Cited
US3365390A Cited
US3560370A Cited
US3463724A Cited
US3494854A Cited
US3493493A Cited
US3684695A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1977-02-18 1977-08-20 1978-02-19 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1981-02-18 1981-08-20 1982-02-19 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1985-02-18 1985-08-20 1986-02-19 $7700.00 Window Closed / Lapsed

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