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US4069162A Expired / Lapsed US ⏱️ 0.0 years remaining

Haze free oil additive compositions containing polymeric viscosity index improver and process for producing said compositions

Assignee: ExxonMobil Technology and Engineering Co
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Filing: 1975-11-03
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Granted: 1978-01-17
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Expires: 1995-11-03
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Abstract

Abstract Oil compositions comprising a lubricating oil and an oil-soluble hydrocarbon polymeric viscosity index improver such as ethylene-propylene copolymers are substantially haze-free when said composition contains an anti-hazing amount of an oil-soluble strong acid containing a hydrogen dissociating moiety which has a pK of less than about 2.5, e.g. a C25 to C70 hydrocarbyl substituted sulfonic acid. The invention also relates to the process for preparing said compositions.

Inventors

  • 👤 John Brooke Gardiner
  • 👤 Max W. Hill
  • 👤 Jack Ryer

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 07:55
CPC Classifications
C; C10; C10M; C10M161/00; C10M143/00; C10M143/02; C10M177/00; C10M2203/00; C10M2203/10; C10M2203/102; C10M2205/00; C10M2205/02; C10M2205/026; C10M2205/06; C10M2205/10; C10M2207/00; C10M2207/02; C10M2207/023; C10M2207/024; C10M2207/10; C10M2207/12; C10M2207/121; C10M2207/123; C10M2207/125; C10M2207/129; C10M2207/22; C10M2209/00; C10M2209/02; C10M2209/08; C10M2209/084; C10M2209/086; C10M2211/00; C10M2211/04; C10M2211/044; C10M2211/06; C10M2215/00; C10M2215/02; C10M2215/06; C10M2215/064; C10M2215/065; C10M2215/16; C10M2215/20; C10M2215/202; C10M2219/00; C10M2219/04; C10M2219/042; C10M2219/044; C10M2219/08; C10M2219/082; C10M2219/087; C10M2219/088; C10M2219/089; C10M2221/00; C10M2221/04; C10M2221/041; C10M2223/00; C10M2223/02; C10M2223/04; C10M2223/041; C10M2223/042; C10M2223/043; C10M2223/045; C10M2223/047; C10M2223/06; C10M2223/061; C10M2223/065; C10N; C10N2010/00; C10N2010/04; C10N2020/00; C10N2020/01; C10N2070/00; C10N2070/02

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 337 words
A process of decreasing haze in a composition comprising: a major amount of hydrocarbon lubricating oil; in the range of about 5 to 30 wt. %, based upon the total weight of said composition, of an oil-soluble viscosity index improver polymer which consists essentially of about 30 to 80 wt. % ethylene and propylene, said polymer being formed by a Ziegler-Natta polymerization, said polymer having a M n in the range from 700 to 500,000 and a M w /M n ratio of less than 10; and a haze forming amount, but less than 1 wt. %, based on the total weight of said composition, of an oil insoluble, haze forming material resulting from the manufacture of said polymer, which material is a disassociable metal salt of a weak organic acid having a pK of more than about 3.8, and wherein said metal is selected from the class consisting of alkaline earth metal, zinc, sodium, potassium, aluminum, vanadium, chromium, iron, manganese, cobalt, nickel, cadmium, lead, bismuth and antimony; which process comprises adding to said composition about 0.1 to about 2.5 equivalents, per equivalent of metal of said haze forming material, of an oil soluble hydrocarbyl substituted strong acid containing a hydrogen disassociating moiety and having a pK of less than about 2.5, and reacting for about 0.1 to about 20 hours at room temperature to about 250° C. said strong acid with said haze forming material to thereby decrease haze by converting said haze forming material either to an oil soluble weak acid or a volatile product, while converting the metal into an oil soluble strong acid metal salt and/or ionic complex of said strong acid, wherein said strong acid is selected from the group consisting of maleic acid, malonic acid, phosphoric acid, thiophosphoric acids, phosphonic acid, thiophosphonic acids, phosphinic acid, thiophosphinic acids, sulfonic acid, sulfuric acid, and alpha-substituted halo- or nitro- or nitrilo-carboxylic acids; and wherein the oil solubilizing hydrocarbyl group or groups of said strong acid contain from about 6 to about 40 carbon atoms.
Claim 2
Dependent Claim 337 words
A process of decreasing haze in a composition comprising: a major amount of hydrocarbon lubricating oil; in the range of about 5 to 30 wt. %, based upon the total weight of said composition, of an oil-soluble viscosity index improver polymer which consists essentially of about 30 to 80 wt. % ethylene and propylene, said polymer being formed by a Ziegler-Natta polymerization, said polymer having a M n in the range from 700 to 500,000 and a M w /M n ratio of less than 10; and a haze forming amount, but less than 1 wt. %, based on the total weight of said composition, of an oil insoluble, haze forming material resulting from the manufacture of said polymer, which material is a disassociable metal salt of a weak organic acid having a pK of more than about 3.8, and wherein said metal is selected from the class consisting of alkaline earth metal, zinc, sodium, potassium, aluminum, vanadium, chromium, iron, manganese, cobalt, nickel, cadmium, lead, bismuth and antimony; which process comprises adding to said composition about 0.1 to about 2.5 equivalents, per equivalent of metal of said haze forming material, of an oil soluble hydrocarbyl substituted strong acid containing a hydrogen disassociating moiety and having a pK of less than about 2.5, and reacting for about 0.1 to about 20 hours at room temperature to about 250° C. said strong acid with said haze forming material to thereby decrease haze by converting said haze forming material either to an oil soluble weak acid or a volatile product, while converting the metal into an oil soluble strong acid metal salt and/or ionic complex of said strong acid, wherein said strong acid is selected from the group consisting of maleic acid, malonic acid, phosphoric acid, thiophosphoric acids, phosphonic acid, thiophosphonic acids, phosphinic acid, thiophosphinic acids, sulfonic acid, sulfuric acid, and alpha-substituted halo- or nitro- or nitrilo-carboxylic acids; and wherein the oil solubilizing hydrocarbyl group or groups of said strong acid contain from about 6 to about 40 carbon atoms.
Claim 3
Dependent Claim 52 words
A process according to claim 1, wherein: said viscosity index improver has a number average molecular weight of about 10,000 to about 200,000; and said oil soluble strong acid reacts with said insoluble metal salt to form an oil soluble metal salt of said strong acid and an oil soluble weak acid.
Claim 4
Dependent Claim 36 words
A process according to claim 1, wherein said strong acid is alkaryl sulfonic acid added to said composition in an amount ranging from 0.01 to 1.0 wt. %, based on the total weight of said composition.
Claim 5
Dependent Claim 30 words
A process according to claim 2, wherein said haze forming material is a calcium salt and has a particle size ranging in diameter from about 0.01 to about 15 microns.
Claim 6
Dependent Claim 16 words
A process according to claim 4, wherein said hydrocarbyl substituted strong acid is di-dodecylbenzene sulfonic acid.
Claim 7
Dependent Claim 19 words
A process according to claim 4, wherein said hydrocarbyl substituted strong acid is di(C 13 Oxo) hydrogen acid phosphate.
Claim 8
Dependent Claim 195 words
A process for reducing haze in an oil additive concentrate comprising a major proportion of hydrocarbon lubricating oil; from 5 to 30 wt. %, based on the total weight of said concentrate, of an ethylenepropylene copolymer viscosity index improver, having a molecular weight (M n ) in the range of 700 to 500,000 and a M w /M n ratio of less than 7, said copolymer consisting essentially of about 30 to 80 wt. % ethylene and propylene and prepared by a Ziegler-Natta polymerization and particles of calcium stearate having a particle size diameter in the range of about 0.01 microns to 15 microns, which causes haze in said oil; said process comprising adding to said concentrate dialkyl substituted benzene sulfonic acid having a (M n ) of about 500 in an amount of from about 0.1 to about 2.5 equivalent per equivalent of said calcium and maintaining said oil concentrate for a period of from about 0.1 hour to about 20 hours at a temperature in the range from about room temperature to about 250° C. in order to form stearic acid and the calcium salt of said sulfonic acid, whereby haze is reduced.
Claim 9
Dependent Claim 195 words
A process for reducing haze in an oil additive concentrate comprising a major proportion of hydrocarbon lubricating oil; from 5 to 30 wt. %, based on the total weight of said concentrate, of an ethylenepropylene copolymer viscosity index improver, having a molecular weight (M n ) in the range of 700 to 500,000 and a M w /M n ratio of less than 7, said copolymer consisting essentially of about 30 to 80 wt. % ethylene and propylene and prepared by a Ziegler-Natta polymerization and particles of calcium stearate having a particle size diameter in the range of about 0.01 microns to 15 microns, which causes haze in said oil; said process comprising adding to said concentrate dialkyl substituted benzene sulfonic acid having a (M n ) of about 500 in an amount of from about 0.1 to about 2.5 equivalent per equivalent of said calcium and maintaining said oil concentrate for a period of from about 0.1 hour to about 20 hours at a temperature in the range from about room temperature to about 250° C. in order to form stearic acid and the calcium salt of said sulfonic acid, whereby haze is reduced.

References Cited (Backward Citations)

US3290244A Cited
US3412027A Cited
US3538138A Cited
US3526596A Cited
US3941834A Cited
US3897353A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-01-16 1981-07-18 1982-01-17 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-01-16 1985-07-18 1986-01-17 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-01-16 1989-07-18 1990-01-17 $7700.00 Window Closed / Lapsed

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