EP3087166B1 - Verwendung zur verbesserung der brennstoffeffizienz eines motors - Google Patents

Verwendung zur verbesserung der brennstoffeffizienz eines motors Download PDF

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EP3087166B1
EP3087166B1 EP14727104.3A EP14727104A EP3087166B1 EP 3087166 B1 EP3087166 B1 EP 3087166B1 EP 14727104 A EP14727104 A EP 14727104A EP 3087166 B1 EP3087166 B1 EP 3087166B1
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Prior art keywords
lubricating
oil
friction
group
friction modifier
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English (en)
French (fr)
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EP3087166A1 (de
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Dennis A. Gaal
Erik Herz
Mrugesh Nilesh PATEL
Douglas Edward Deckman
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ExxonMobil Technology and Engineering Co
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ExxonMobil Research and Engineering Co
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    • C10N2030/42—Phosphor free or low phosphor content compositions
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/40—Low content or no content compositions
    • C10N2030/45—Ash-less or low ash content
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/54—Fuel economy
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2040/00—Specified use or application for which the lubricating composition is intended
    • C10N2040/25—Internal-combustion engines
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2060/00—Chemical after-treatment of the constituents of the lubricating composition
    • C10N2060/14—Chemical after-treatment of the constituents of the lubricating composition by boron or a compound containing boron

Definitions

  • This disclosure relates to improving fuel efficiency and friction reduction properties, while maintaining or improving deposit control, in an engine lubricated with a lubricating oil by including a friction modifier mixture, in the lubricating oil.
  • Contemporary lubricants such as engine oils use mixtures of additives such as dispersants, detergents, inhibitors, viscosity index improvers and the like to provide engine cleanliness and durability under a wide range of performance conditions of temperature, pressure, and lubricant service life.
  • additives such as dispersants, detergents, inhibitors, viscosity index improvers and the like to provide engine cleanliness and durability under a wide range of performance conditions of temperature, pressure, and lubricant service life.
  • Lubricant-related performance characteristics such as high temperature deposit control and fuel economy are extremely advantageous attributes as measured by a variety of bench and engine tests. As indicated above, it is known that adding organic friction modifiers to a lubricant formulation imparts frictional benefits at low temperatures, consequently improving the lubricant fuel economy performance. At high temperatures, however, adding increased levels of organic friction modifier can invite high temperature performance issues. For example, engine deposits are undesirable consequences of high levels of friction modifier in an engine oil formulation at high temperature engine operation.
  • a major challenge in engine oil formulation is simultaneously achieving high temperature deposit control while also achieving improved fuel economy.
  • This disclosure relates in part to the use of a friction modifier mixture for improving fuel efficiency and reducing frictional properties, while maintaining or improving deposit control, in an engine lubricated with a lubricating oil having a composition comprising from 50 to 99 weight % based on the total weight of the lubricating oil of a lubricating oil base stock as a major component wherein the friction modifier mixture comprises an ethoxylated fatty acid ester and a glycerol fatty acid ester in a weight ratio of from 0.1:1 to 1:0.1 and is present in a range of from 0.1 to 1.5 weight % based on the total weight of the lubricating oil and wherein fuel efficiency and friction reduction properties are improved and deposit control is maintained or improved as compared to friction reduction properties and deposit control achieved using a lubricating engine oil containing a minor component other than the friction modifier mixture.
  • the lubricating oils of this disclosure are useful in internal combustion engines including direct injection, gasoline and diesel engines.
  • Fuel efficiency and friction reduction properties are improved and deposit control is maintained or improved as compared to friction reduction properties and deposit control achieved using a lubricating engine oil containing a minor component other than the friction modifier mixture.
  • This disclosure further relates in part to a lubricating engine oil having a composition comprising from 50 to 99 weight % based on the total weight of the lubricating oil of a lubricating oil base stock as a major component; and a friction modifier mixture comprising an ethoxylated fatty acid ester and a glycerol fatty acid ester in a weight ratio of from 0.1:1 to 1:0.1 said friction modifier mixture being present in a range of from 0.1 to 1.0 weight % based on the total weight of the lubricating oil; and wherein fuel efficiency and friction reduction properties are improved and deposit control is maintained or improved as compared to friction reduction properties and deposit control achieved using a lubricating engine oil containing a minor component other than the friction modifier mixture.
  • the lubricating oil preferably comprises a lubricating oil base stock as a major component, and a friction modifier mixture, a metal dialkyl dithio phosphate, and a viscosity index improver, as minor components.
  • the lubricating oils of this disclosure are particularly advantageous as passenger vehicle engine oil (PVEO) products.
  • the lubricating oils of this disclosure provide excellent engine protection including friction reduction and anti-wear performance. This benefit has been demonstrated for the lubricating oils of this disclosure in the Sequence VID (ASTM D7589) engine tests.
  • the lubricating oils of this disclosure provide improved fuel efficiency.
  • a lower HTHS viscosity engine oil generally provides superior fuel economy to a higher HTHS viscosity product. This benefit has been demonstrated for the lubricating oils of this disclosure in the Sequence VID Fuel Economy (ASTM D7589) engine test.
  • the lubricating engine oils of this disclosure have a composition sufficient to pass wear protection requirements of one or more engine tests selected from Sequence VID and others.
  • the lubricating engine oils containing the friction modifier mixture of this disclosure can exhibit a fuel efficiency improvement preferably greater than 10%, as determined by the Sequence VID Fuel Economy (ASTM D7589) engine test.
  • Lubricating base oils that are useful in the present disclosure are both natural oils, and synthetic oils, and unconventional oils (or mixtures thereof) can be used unrefined, refined, or rerefined (the latter is also known as reclaimed or reprocessed oil).
  • Unrefined oils are those obtained directly from a natural or synthetic source and used without added purification. These include shale oil obtained directly from retorting operations, petroleum oil obtained directly from primary distillation, and ester oil obtained directly from an esterification process. Refined oils are similar to the oils discussed for unrefined oils except refined oils are subjected to one or more purification steps to improve at least one lubricating oil property.
  • Groups I, II, III, IV and V are broad base oil stock categories developed and defined by the American Petroleum Institute (API Publication 1509; www.API.org ) to create guidelines for lubricant base oils.
  • Group I base stocks have a viscosity index of between 80 to 120 and contain greater than 0.03% sulfur and/or less than 90% saturates.
  • Group II base stocks have a viscosity index of between 80 to 120, and contain less than or equal to 0.03% sulfur and greater than or equal to 90% saturates.
  • Group III stocks have a viscosity index greater than 120 and contain less than or equal to 0.03 % sulfur and greater than 90% saturates.
  • Group IV includes polyalphaolefins (PAO).
  • Group V base stock includes base stocks not included in Groups I-IV.
  • the table below summarizes properties of each of these five groups.
  • Base Oil Properties Saturates Sulfur Viscosity Index Group I ⁇ 90 and/or >0.03% and ⁇ 80 and ⁇ 120 Group II ⁇ 90 and ⁇ 0.03% and ⁇ 80 and ⁇ 120 Group III ⁇ 90 and ⁇ 0.03% and ⁇ 120 Group IV Polyalphaolefins (PAO) Group V All other base oil stocks not included in Groups I, II, III or IV
  • Natural oils include animal oils, vegetable oils (castor oil and lard oil, for example), and mineral oils. Animal and vegetable oils possessing favorable thermal oxidative stability can be used. Of the natural oils, mineral oils are preferred. Mineral oils vary widely as to their crude source, for example, as to whether they are paraffinic, naphthenic, or mixed paraffinic-naphthenic. Oils derived from coal or shale are also useful. Natural oils vary also as to the method used for their production and purification, for example, their distillation range and whether they are straight run or cracked, hydrorefined, or solvent extracted.
  • Group II and/or Group III hydroprocessed or hydrocracked basestocks including synthetic oils such as polyalphaolefins, alkyl aromatics and synthetic esters are also well known basestock oils.
  • Synthetic oils include hydrocarbon oil.
  • Hydrocarbon oils include oils such as polymerized and interpolymerized olefins (polybutylenes, polypropylenes, propylene isobutylene copolymers, ethylene-olefin copolymers, and ethylene-alphaolefin copolymers, for example).
  • Polyalphaolefin (PAO) oil base stocks are commonly used synthetic hydrocarbon oil.
  • PAOs derived from C 6 , C 8 , C 10 , C 12 , C 14 olefins or mixtures thereof may be utilized. See U.S. Patent Nos. 4,956,122 ; 4,827,064 ; and 4,827,073 .
  • the number average molecular weights of the PAOs typically vary from 250 to 3,000, although PAO's may be made in viscosities up to 100 cSt (100°C).
  • the PAOs are typically comprised of relatively low molecular weight hydrogenated polymers or oligomers of alphaolefins which include, but are not limited to, C 2 to C 32 alphaolefins with the C 8 to C 16 alphaolefins, such as 1-hexene, 1-octene, 1-decene, 1-dodecene and the like, being preferred.
  • the preferred polyalphaolefins are poly-1-hexene, poly-1-octene, poly-1-decene and poly-1-dodecene and mixtures thereof and mixed olefin-derived polyolefins.
  • the dimers of higher olefins in the range of C 14 to C 18 may be used to provide low viscosity base stocks of acceptably low volatility.
  • the PAOs may be predominantly trimers and tetramers of the starting olefins, with minor amounts of the higher oligomers, having a viscosity range of 1.5 to 12 cSt.
  • PAO fluids of particular use may include 3.0 cSt, 3.4 cSt, and/or 3.6 cSt and combinations thereof.
  • Bi-modal mixtures of PAO fluids having a viscosity range of 1.5 to 100 cSt may be used if desired.
  • the PAO fluids may be conveniently made by the polymerization of an alphaolefin in the presence of a polymerization catalyst such as the Friedel-Crafts catalysts including, for example, aluminum trichloride, boron trifluoride or complexes of boron trifluoride with water, alcohols such as ethanol, propanol or butanol, carboxylic acids or esters such as ethyl acetate or ethyl propionate.
  • a polymerization catalyst such as the Friedel-Crafts catalysts including, for example, aluminum trichloride, boron trifluoride or complexes of boron trifluoride with water, alcohols such as ethanol, propanol or butanol, carboxylic acids or esters such as ethyl acetate or ethyl propionate.
  • a polymerization catalyst such as the Friedel-Crafts catalysts including, for example, aluminum trichloride, boro
  • wax isomerate base stocks and base oils comprising hydroisomerized waxy stocks (e.g. waxy stocks such as gas oils, slack waxes, fuels hydrocracker bottoms, etc.), hydroisomerized Fischer-Tropsch waxes, Gas-to-Liquids (GTL) base stocks and base oils, and other wax isomerate hydroisomerized base stocks and base oils, or mixtures thereof Fischer-Tropsch waxes, the high boiling point residues of Fischer-Tropsch synthesis, are highly paraffinic hydrocarbons with very low sulfur content.
  • hydroisomerized waxy stocks e.g. waxy stocks such as gas oils, slack waxes, fuels hydrocracker bottoms, etc.
  • hydroisomerized Fischer-Tropsch waxes e.g. waxy stocks such as gas oils, slack waxes, fuels hydrocracker bottoms, etc.
  • GTL Gas-to-Liquids
  • Fischer-Tropsch waxes the
  • the hydroprocessing used for the production of such base stocks may use an amorphous hydrocracking/hydroisomerization catalyst, such as one of the specialized lube hydrocracking (LHDC) catalysts or a crystalline hydrocracking/hydroisomerization catalyst, preferably a zeolitic catalyst.
  • an amorphous hydrocracking/hydroisomerization catalyst such as one of the specialized lube hydrocracking (LHDC) catalysts or a crystalline hydrocracking/hydroisomerization catalyst, preferably a zeolitic catalyst.
  • LHDC specialized lube hydrocracking
  • a zeolitic catalyst preferably ZSM-48 as described in U.S. Patent No. 5,075,269 .
  • Processes for making hydrocracked/hydroisomerized distillates and hydrocracked/hydroisomerized waxes are described, for example, in U.S. Patent Nos. 2,817,693 ; 4,975,177 ; 4,92
  • Gas-to-Liquids (GTL) base oils, Fischer-Tropsch wax derived base oils, and other wax-derived hydroisomerized (wax isomerate) base oils be advantageously used in the instant disclosure, and may have useful kinematic viscosities at 100°C of 3 cSt to 50 cSt, preferably 3 cSt to 30 cSt, more preferably 3.5 cSt to 25 cSt, as exemplified by GTL 4 with kinematic viscosity of 4.0 cSt at 100°C and a viscosity index of 141.
  • Gas-to-Liquids (GTL) base oils may have useful pour points of -20°C or lower, and under some conditions may have advantageous pour points of -25°C or lower, with useful pour points of -30°C to -40°C or lower.
  • Useful compositions of Gas-to-Liquids (GTL) base oils, Fischer-Tropsch wax derived base oils, and wax-derived hydroisomerized base oils are recited in U.S. Patent Nos. 6,080,301 ; 6,090,989 , and 6,165,949 for example.
  • the hydrocarbyl aromatics can be used as base oil or base oil component and can be any hydrocarbyl molecule that contains at least 5% of its weight derived from an aromatic moiety such as a benzenoid moiety or naphthenoid moiety, or their derivatives.
  • These hydrocarbyl aromatics include alkyl benzenes, alkyl naphthalenes, alkyl diphenyl oxides, alkyl naphthols, alkyl diphenyl sulfides, alkylated bis-phenol A, alkylated thiodiphenol, and the like.
  • the aromatic can be mono-alkylated, dialkylated, polyalkylated, and the like.
  • the aromatic can be mono- or poly-functionalized.
  • the hydrocarbyl groups can also be comprised of mixtures of alkyl groups, alkenyl groups, alkynyl, cycloalkyl groups, cycloalkenyl groups and other related hydrocarbyl groups.
  • the hydrocarbyl groups can range from C 6 up to C 60 with a range of C 8 to C 20 often being preferred. A mixture of hydrocarbyl groups is often preferred, and up to three such substituents may be present.
  • the hydrocarbyl group can optionally contain sulfur, oxygen, and/or nitrogen containing substituents.
  • the aromatic group can also be derived from natural (petroleum) sources, provided at least 5% of the molecule is comprised of an above-type aromatic moiety.
  • Viscosities at 100°C of approximately 3 cSt to 50 cSt are preferred, with viscosities of approximately 3.4 cSt to 20 cSt often being more preferred for the hydrocarbyl aromatic component.
  • an alkyl naphthalene where the alkyl group is primarily comprised of 1-hexadecene is used.
  • Other alkylates of aromatics can be advantageously used.
  • Naphthalene or methyl naphthalene, for example, can be alkylated with olefins such as octene, decene, dodecene, tetradecene or higher, mixtures of similar olefins, and the like.
  • Useful concentrations of hydrocarbyl aromatic in a lubricant oil composition can be 2% to 25%, preferably 4% to 20%, and more preferably 4% to 15%, depending on the application.
  • Alkylated aromatics such as the hydrocarbyl aromatics of the present disclosure may be produced by well-known Friedel-Crafts alkylation of aromatic compounds. See Friedel-Crafts and Related Reactions, Olah, G. A. (ed.), Interscience Publishers, New York, 1963 .
  • an aromatic compound such as benzene or naphthalene
  • an olefin, alkyl halide or alcohol in the presence of a Friedel-Crafts catalyst.
  • Friedel-Crafts and Related Reactions Vol. 2, part 1, chapters 14, 17, and 18 , See Olah, G. A. (ed.), Interscience Publishers, New York, 1964.
  • catalysts are known to one skilled in the art.
  • the choice of catalyst depends on the reactivity of the starting materials and product quality requirements.
  • strong acids such as AlCl 3 , BF 3 , or HF may be used.
  • milder catalysts such as FeCl 3 or SnCl 4 are preferred.
  • Newer alkylation technology uses zeolites or solid super acids.
  • Esters comprise a useful base stock. Additive solvency and seal compatibility characteristics may be secured by the use of esters such as the esters of dibasic acids with monoalkanols and the polyol esters of monocarboxylic acids.
  • Esters of the former type include, for example, the esters of dicarboxylic acids such as phthalic acid, succinic acid, alkyl succinic acid, alkenyl succinic acid, maleic acid, azelaic acid, suberic acid, sebacic acid, fumaric acid, adipic acid, linoleic acid dimer, malonic acid, alkyl malonic acid, alkenyl malonic acid, etc., with a variety of alcohols such as butyl alcohol, hexyl alcohol, dodecyl alcohol, 2-ethylhexyl alcohol, etc.
  • esters include dibutyl adipate, di(2-ethylhexyl) sebacate, di-n-hexyl fumarate, dioctyl sebacate, diisooctyl azelate, diisodecyl azelate, dioctyl phthalate, didecyl phthalate, dieicosyl sebacate, etc.
  • Particularly useful synthetic esters are those which are obtained by reacting one or more polyhydric alcohols, preferably the hindered polyols (such as the neopentyl polyols, e.g., neopentyl glycol, trimethylol ethane, 2-methyl-2-propyl-1,3-propanediol, trimethylol propane, pentaerythritol and dipentaerythritol) with alkanoic acids containing at least 4 carbon atoms, preferably C 5 to C 30 acids such as saturated straight chain fatty acids including caprylic acid, capric acid, lauric acid, myristic acid, palmitic acid, stearic acid, arachic acid, and behenic acid, or the corresponding branched chain fatty acids or unsaturated fatty acids such as oleic acid, or mixtures of any of these materials.
  • the hindered polyols such as the neopentyl polyols,
  • Suitable synthetic ester components include the esters of trimethylol propane, trimethylol butane, trimethylol ethane, pentaerythritol and/or dipentaerythritol with one or more monocarboxylic acids containing from 5 to 10 carbon atoms. These esters are widely available commercially, for example, the Mobil P-41 and P-51 esters of ExxonMobil Chemical Company.
  • esters derived from renewable material such as coconut, palm, rapeseed, soy, sunflower and the like. These esters may be monoesters, di-esters, polyol esters, complex esters, or mixtures thereof. These esters are widely available commercially, for example, the Mobil P-51 ester of ExxonMobil Chemical Company.
  • Engine oil formulations containing renewable esters are included in this disclosure.
  • the renewable content of the ester is typically greater than 70 weight percent, preferably more than 80 weight percent and most preferably more than 90 weight percent.
  • Renewable esters can be preferred in combination with the friction modifier mixture.
  • Other useful fluids of lubricating viscosity include non-conventional or unconventional base stocks that have been processed, preferably catalytically, or synthesized to provide high performance lubrication characteristics.
  • Non-conventional or unconventional base stocks/base oils include one or more of a mixture of base stock(s) derived from one or more Gas-to-Liquids (GTL) materials, as well as isomerate/isodewaxate base stock(s) derived from natural wax or waxy feeds, mineral and or non-mineral oil waxy feed stocks such as slack waxes, natural waxes, and waxy stocks such as gas oils, waxy fuels hydrocracker bottoms, waxy raffinate, hydrocrackate, thermal crackates, or other mineral, mineral oil, or even non-petroleum oil derived waxy materials such as waxy materials received from coal liquefaction or shale oil, and mixtures of such base stocks.
  • GTL Gas-to-Liquids
  • GTL materials are materials that are derived via one or more synthesis, combination, transformation, rearrangement, and/or degradation/deconstructive processes from gaseous carbon-containing compounds, hydrogen-containing compounds and/or elements as feed stocks such as hydrogen, carbon dioxide, carbon monoxide, water, methane, ethane, ethylene, acetylene, propane, propylene, propyne, butane, butylenes, and butynes.
  • GTL base stocks and/or base oils are GTL materials of lubricating viscosity that are generally derived from hydrocarbons; for example, waxy synthesized hydrocarbons, that are themselves derived from simpler gaseous carbon-containing compounds, hydrogen-containing compounds and/or elements as feed stocks.
  • GTL base stock(s) and/or base oil(s) include oils boiling in the lube oil boiling range (1) separated/fractionated from synthesized GTL materials such as, for example, by distillation and subsequently subjected to a final wax processing step which involves either or both of a catalytic dewaxing process, or a solvent dewaxing process, to produce lube oils of reduced/low pour point; (2) synthesized wax isomerates, comprising, for example, hydrodewaxed or hydroisomerized cat and/or solvent dewaxed synthesized wax or waxy hydrocarbons; (3) hydrodewaxed or hydroisomerized cat and/or solvent dewaxed Fischer-Tropsch (F-T) material (i.e., hydrocarbons, waxy hydrocarbons, waxes and possible analogous oxygenates); preferably hydrodewaxed or hydroisomerized/followed by cat and/or solvent dewaxing dewaxed F-T waxy hydrocarbons, or hydrodewaxed
  • GTL base stock(s) and/or base oil(s) derived from GTL materials are characterized typically as having kinematic viscosities at 100°C of from 2 mm 2 /s to 50 mm 2 /s (ASTM D445). They are further characterized typically as having pour points of -5°C to -40°C or lower (ASTM D97). They are also characterized typically as having viscosity indices of 80 to 140 or greater (ASTM D2270).
  • GTL base stock(s) and/or base oil(s) are typically highly paraffinic (>90% saturates), and may contain mixtures of monocycloparaffins and multicycloparaffins in combination with non-cyclic isoparaffins.
  • the ratio of the naphthenic (i.e., cycloparaffin) content in such combinations varies with the catalyst and temperature used.
  • GTL base stock(s) and/or base oil(s) typically have very low sulfur and nitrogen content, generally containing less than 10 ppm, and more typically less than 5 ppm of each of these elements.
  • the sulfur and nitrogen content of GTL base stock(s) and/or base oil(s) obtained from F-T material, especially F-T wax, is essentially nil.
  • the absence of phosphorous and aromatics make this materially especially suitable for the formulation of low SAP products.
  • GTL base stock and/or base oil and/or wax isomerate base stock and/or base oil is to be understood as embracing individual fractions of such materials of wide viscosity range as recovered in the production process, mixtures of two or more of such fractions, as well as mixtures of one or two or more low viscosity fractions with one, two or more higher viscosity fractions to produce a blend wherein the blend exhibits a target kinematic viscosity.
  • the GTL material, from which the GTL base stock(s) and/or base oil(s) is/are derived is preferably an F-T material (i.e., hydrocarbons, waxy hydrocarbons, wax).
  • GTL base stock(s) and/or base oil(s) are typically highly paraffinic (>90% saturates), and may contain mixtures of monocycloparaffins and multicycloparaffins in combination with non-cyclic isoparaffins.
  • the ratio of the naphthenic (i.e., cycloparaffin) content in such combinations varies with the catalyst and temperature used.
  • GTL base stock(s) and/or base oil(s) and hydrodewaxed, or hydroisomerized/cat (and/or solvent) dewaxed base stock(s) and/or base oil(s) typically have very low sulfur and nitrogen content, generally containing less than 10 ppm, and more typically less than 5 ppm of each of these elements.
  • the sulfur and nitrogen content of GTL base stock(s) and/or base oil(s) obtained from F-T material, especially F-T wax, is essentially nil.
  • the absence of phosphorous and aromatics make this material especially suitable for the formulation of low sulfur, sulfated ash, and phosphorus (low SAP) products.
  • Base oils for use in the formulated lubricating oils useful in the present disclosure are any of the variety of oils corresponding to API Group I, Group II, Group III, Group IV, and Group V oils and mixtures thereof, preferably API Group II, Group III, Group IV, and Group V oils and mixtures thereof, more preferably the Group III to Group V base oils due to their exceptional volatility, stability, viscometric and cleanliness features.
  • Minor quantities of Group I stock such as the amount used to dilute additives for blending into formulated lube oil products, can be tolerated but should be kept to a minimum, i.e. amounts only associated with their use as diluent/carrier oil for additives used on an "as-received" basis.
  • Even in regard to the Group II stocks it is preferred that the Group II stock be in the higher quality range associated with that stock, i.e. a Group II stock having a viscosity index in the range 100 ⁇ VI ⁇ 120.
  • the base oil constitutes the major component of the engine oil lubricant composition of the present disclosure and is present in an amount ranging from 50 to 99 weight percent, preferably from 70 to 95 weight percent, and more preferably from 85 to 95 weight percent, based on the total weight of the composition.
  • the base oil may be selected from any of the synthetic or natural oils typically used as crankcase lubricating oils for spark-ignited and compression-ignited engines.
  • the base oil conveniently has a kinematic viscosity, according to ASTM standards, of 2.5 cSt to 12 cSt (or mm 2 /s) at 100°C and preferably of 2.5 cSt to 9 cSt (or mm 2 /s) at 100° C.
  • Mixtures of synthetic and natural base oils may be used if desired. Mixtures of Group III, IV, V may be preferable.
  • Illustrative alkoxylated fatty acid esters include, for example, polyoxyethylene stearate, fatty acid polyglycol ester, and the like. These can include polyoxypropylene stearate, polyoxybutylene stearate, polyoxyethylene isosterate, polyoxypropylene isostearate, polyoxyethylene palmitate.
  • Illustrative glycerol fatty acid esters include, for example, glycerol mono-oleate, saturated mono-, di, and tri- glyceride esters, glycerol monostearate, and the like.
  • Preferred can be the glycerol mono-oleates, glycerol dioleates, glycerol trioleates, glycerol monostearates, glycerol distearates, and glycerol tristearates and the corresponding glycerol monopalmitates, glycerol dipalmitates, and glycerol tripalmitates, and the respective isostearates, linoleates, and the like.
  • the glycerol esters can be preferred as well as mixtures containing any of these. Ethoxylated, propoxylated, butoxylated fatty acid esters of glycerol can be preferred.
  • Illustrative borated glycerol fatty acid esters include, for example, borated glycerol mono-oleate, borated saturated mono-, di, and tri- glyceride esters, borated glycerol mono-sterate, and the like.
  • the friction modifier mixture of this disclosure comprises an ethoxylated fatty acid ester and a glycerol fatty acid ester.
  • a preferred formulation of this disclosure comprises a lubricating oil base stock that includes a Group I, Group II, Group III, Group IV and/or Group V base oil and a friction modifier mixture that includes an ethoxylated fatty acid ester and a glycerol fatty acid ester.
  • Useful concentrations of friction modifier mixtures ranges from 0.1 weight percent to 1.5 weight percent, or 0.1 weight percent to 1 weight percent.
  • the weight ratio of the first friction modifier to the other friction modifier can range from 0.1:1 to 1:0.1.
  • the formulated lubricating oil useful in the present disclosure may additionally contain one or more of the other commonly used lubricating oil performance additives including but not limited to antiwear agents, dispersants, other detergents, corrosion inhibitors, rust inhibitors, metal deactivators, extreme pressure additives, anti-seizure agents, wax modifiers, viscosity index improvers, viscosity modifiers, fluid-loss additives, seal compatibility agents, organic metallic friction modifiers, lubricity agents, anti-staining agents, chromophoric agents, defoamants, demulsifiers, emulsifiers, densifiers, wetting agents, gelling agents, tackiness agents, colorants, and others.
  • the other commonly used lubricating oil performance additives including but not limited to antiwear agents, dispersants, other detergents, corrosion inhibitors, rust inhibitors, metal deactivators, extreme pressure additives, anti-seizure agents, wax modifiers, viscosity index improvers, visco
  • a metal alkylthiophosphate and more particularly a metal dialkyl dithio phosphate in which the metal constituent is zinc, or zinc dialkyl dithio phosphate is a useful component of the lubricating oils of this disclosure.
  • ZDDP can be derived from primary alcohols, secondary alcohols or mixtures thereof.
  • ZDDP compounds generally are of the formula Zn[SP(S)(OR 1 )(OR 2 )] 2 where R 1 and R 2 are C 1 -C 18 alkyl groups, preferably C 2 -C 12 alkyl groups. These alkyl groups may be straight chain or branched.
  • Alcohols used in the ZDDP can be 2-propanol, butanol, secondary butanol, pentanols, hexanols such as 4-methyl-2-pentanol, n-hexanol, n-octanol, 2-ethyl hexanol, alkylated phenols, and the like. Mixtures of secondary alcohols or of primary and secondary alcohol can be preferred. Alkyl aryl groups may also be used.
  • Preferable zinc dithiophosphates which are commercially available include secondary zinc dithiophosphates such as those available from for example, The Lubrizol Corporation under the trade designations "LZ 677A”, “LZ 1095” and “LZ 1371", from for example Chevron Oronite under the trade designation "OLOA 262" and from for example Afton Chemical under the trade designation "HITEC 7169".
  • the ZDDP is typically used in amounts of from 0.4 weight percent to 1.2 weight percent, preferably from 0.5 weight percent to 1.0 weight percent, and more preferably from 0.6 weight percent to 0.8 weight percent, based on the total weight of the lubricating oil, although more or less can often be used advantageously.
  • the ZDDP is a secondary ZDDP and present in an amount of from 0.6 to 1.0 weight percent of the total weight of the lubricating oil.
  • Low phosphorus engine oil formulations are included in this disclosure.
  • the phosphorus content is typically less than 0.12 weight percent preferably less than 0.10 weight percent and most preferably less than 0.085 weight percent. Low phosphorus can be preferred in combination with the friction modifier mixture.
  • Viscosity index improvers also known as VI improvers, viscosity modifiers, and viscosity improvers
  • VI improvers also known as VI improvers, viscosity modifiers, and viscosity improvers
  • Viscosity index improvers can be included in the lubricant compositions of this disclosure.
  • Viscosity index improvers provide lubricants with high and low temperature operability. These additives impart shear stability at elevated temperatures and acceptable viscosity at low temperatures.
  • Suitable viscosity index improvers include high molecular weight hydrocarbons, polyesters and viscosity index improver dispersants that function as both a viscosity index improver and a dispersant.
  • Typical molecular weights of these polymers are between 10,000 to 1,500,000, more typically 20,000 to 1,200,000, and even more typically between 50,000 and 1,000,000.
  • suitable viscosity index improvers are linear or star-shaped polymers and copolymers of methacrylate, butadiene, olefins, or alkylated styrenes.
  • Polyisobutylene is a commonly used viscosity index improver.
  • Another suitable viscosity index improver is polymethacrylate (copolymers of various chain length alkyl methacrylates, for example), some formulations of which also serve as pour point depressants.
  • Other suitable viscosity index improvers include copolymers of ethylene and propylene, hydrogenated block copolymers of styrene and isoprene, and polyacrylates (copolymers of various chain length acrylates, for example). Specific examples include styrene-isoprene or styrene-butadiene based polymers of 50,000 to 200,000 molecular weight.
  • Olefin copolymers are commercially available from Chevron Oronite Company LLC under the trade designation "PARATONE®” (such as “PARATONE® 8921” and “PARATONE® 8941”); from Afton Chemical Corporation under the trade designation “HiTEC®” (such as “HiTEC® 5850B”; and from The Lubrizol Corporation under the trade designation "Lubrizol® 7067C”.
  • PARATONE® such as “PARATONE® 8921” and “PARATONE® 8941”
  • HiTEC® such as “HiTEC® 5850B”
  • Lubrizol® 7067C trade designation
  • Polyisoprene polymers are commercially available from Infineum International Limited, e.g. under the trade designation "SV200”
  • diene-styrene copolymers are commercially available from Infineum International Limited, e.g. under the trade designation "SV 260”.
  • the viscosity index improvers may be used in an amount of less than 2.0 weight percent, preferably less than 1.0 weight percent, and more preferably less than 0.5 weight percent, based on the total weight of the formulated oil or lubricating engine oil. Viscosity improvers are typically added as concentrates, in large amounts of diluent oil.
  • the viscosity index improvers may be used in an amount of from 0.25 to 2.0 weight percent, preferably 0.15 to 1.0 weight percent, and more preferably 0.05 to 0.5 weight percent, based on the total weight of the formulated oil or lubricating engine oil.
  • Illustrative detergents useful in this disclosure include, for example, alkali metal detergents, alkaline earth metal detergents, or mixtures of one or more alkali metal detergents and one or more alkaline earth metal detergents.
  • a typical detergent is an anionic material that contains a long chain hydrophobic portion of the molecule and a smaller anionic or oleophobic hydrophilic portion of the molecule.
  • the anionic portion of the detergent is typically derived from an organic acid such as a sulfur acid, carboxylic acid, phosphorous acid, phenol, or mixtures thereof.
  • the counterion is typically an alkaline earth or alkali metal.
  • Salts that contain a substantially stochiometric amount of the metal are described as neutral salts and have a total base number (TBN, as measured by ASTM D2896) of from 0 to 80.
  • TBN total base number
  • Many compositions are overbased, containing large amounts of a metal base that is achieved by reacting an excess of a metal compound (a metal hydroxide or oxide, for example) with an acidic gas (such as carbon dioxide).
  • a metal compound a metal hydroxide or oxide, for example
  • an acidic gas such as carbon dioxide
  • Useful detergents can be neutral, mildly overbased, or highly overbased. These detergents can be used in mixtures of neutral, overbased, highly overbased calcium salicylate, sulfonates, phenates and/or magnesium salicylate, sulfonates, phenates.
  • the TBN ranges can vary from low, medium to high TBN products, including as low as 0 to as high as 600.
  • Mixtures of low, medium, high TBN can be used, along with mixtures of calcium and magnesium metal based detergents, and including sulfonates, phenates, salicylates, and carboxylates.
  • a detergent mixture with a metal ratio of 1, in conjunction of a detergent with a metal ratio of 2, and as high as a detergent with a metal ratio of 5, can be used.
  • Borated detergents can also be used.
  • Alkaline earth phenates are another useful class of detergent. These detergents can be made by reacting alkaline earth metal hydroxide or oxide (CaO, Ca(OH) 2 , BaO, Ba(OH) 2 , MgO, Mg(OH) 2 , for example) with an alkyl phenol or sulfurized alkylphenol.
  • alkaline earth metal hydroxide or oxide Ca(OH) 2 , BaO, Ba(OH) 2 , MgO, Mg(OH) 2 , for example
  • Useful alkyl groups include straight chain or branched C 1 -C 30 alkyl groups, preferably, C 4 -C 20 or mixtures thereof. Examples of suitable phenols include isobutylphenol, 2-ethylhexylphenol, nonylphenol, dodecyl phenol, and the like.
  • starting alkylphenols may contain more than one alkyl substituent that are each independently straight chain or branched and can be used from 0.5 to 6 weight percent.
  • the sulfurized product may be obtained by methods well known in the art. These methods include heating a mixture of alkylphenol and sulfurizing agent (including elemental sulfur, sulfur halides such as sulfur dichloride, and the like) and then reacting the sulfurized phenol with an alkaline earth metal base.
  • carboxylic acids are also useful as detergents. These carboxylic acid detergents may be prepared by reacting a basic metal compound with at least one carboxylic acid and removing free water from the reaction product. These compounds may be overbased to produce the desired TBN level.
  • Detergents made from salicylic acid are one preferred class of detergents derived from carboxylic acids.
  • Useful salicylates include long chain alkyl salicylates.
  • R is an alkyl group having 1 to 30 carbon atoms
  • n is an integer from 1 to 4
  • M is an alkaline earth metal.
  • Preferred R groups are alkyl chains of at least C 11 , preferably C 13 or greater. R may be optionally substituted with substituents that do not interfere with the detergent's function.
  • M is preferably, calcium, magnesium, or barium. More preferably, M is calcium.
  • Hydrocarbyl-substituted salicylic acids may be prepared from phenols by the Kolbe reaction (see U.S. Patent No. 3,595,791 ).
  • the metal salts of the hydrocarbyl-substituted salicylic acids may be prepared by double decomposition of a metal salt in a polar solvent such as water or alcohol.
  • Alkaline earth metal phosphates are also used as detergents and are known in the art.
  • Detergents may be simple detergents or what is known as hybrid or complex detergents. The latter detergents can provide the properties of two detergents without the need to blend separate materials. See U.S. Patent No. 6,034,039 .
  • Preferred detergents include calcium phenates, calcium sulfonates, calcium salicylates, magnesium phenates, magnesium sulfonates, magnesium salicylates and other related components (including borated detergents), and mixtures thereof.
  • Preferred mixtures of detergents include magnesium sulfonate and calcium salicylate, magnesium sulfonate and calcium sulfonate, magnesium sulfonate and calcium phenate, calcium phenate and calcium salicylate, calcium phenate and calcium sulfonate, calcium phenate and magnesium salicylate, calcium phenate and magnesium phenate.
  • the detergent concentration in the lubricating oils of this disclosure can range from 1.0 to 6.0 weight percent, preferably 2.0 to 5.0 weight percent, and more preferably from 2.0 weight percent to 4.0 weight percent, based on the total weight of the lubricating oil.
  • the detergent concentrations are given on an “as delivered” basis.
  • the active detergent is delivered with a process oil.
  • the "as delivered” detergent typically contains from 20 weight percent to 80 weight percent, or from 40 weight percent to 60 weight percent, of active detergent in the "as delivered” detergent product.
  • Dispersants help keep these byproducts in solution, thus diminishing their deposition on metal surfaces.
  • Dispersants used in the formulation of the lubricating oil may be ashless or ash-forming in nature.
  • the dispersant is ashless.
  • So called ashless dispersants are organic materials that form substantially no ash upon combustion.
  • non-metal-containing or borated metal-free dispersants are considered ashless.
  • metal-containing detergents discussed above form ash upon combustion.
  • Suitable dispersants typically contain a polar group attached to a relatively high molecular weight hydrocarbon chain.
  • the polar group typically contains at least one element of nitrogen, oxygen, or phosphorus.
  • Typical hydrocarbon chains contain 50 to 400 carbon atoms.
  • a particularly useful class of dispersants are the alkenylsuccinic derivatives, typically produced by the reaction of a long chain hydrocarbyl substituted succinic compound, usually a hydrocarbyl substituted succinic anhydride, with a polyhydroxy or polyamino compound.
  • the long chain hydrocarbyl group constituting the oleophilic portion of the molecule which confers solubility in the oil, is normally a polyisobutylene group.
  • Many examples of this type of dispersant are well known commercially and in the literature. Exemplary U.S. patents describing such dispersants are U.S. Patent Nos.
  • Hydrocarbyl-substituted succinic acid and hydrocarbyl-substituted succinic anhydride derivatives are useful dispersants.
  • succinimide, succinate esters, or succinate ester amides prepared by the reaction of a hydrocarbon-substituted succinic acid compound preferably having at least 50 carbon atoms in the hydrocarbon substituent, with at least one equivalent of an alkylene amine are particularly useful, although on occasion, having a hydrocarbon substituent between 20-50 carbon atoms can be useful.
  • Succinimides are formed by the condensation reaction between hydrocarbyl substituted succinic anhydrides and amines. Molar ratios can vary depending on the polyamine. For example, the molar ratio of hydrocarbyl substituted succinic anhydride to TEPA can vary from 1:1 to 5:1. Representative examples are shown in U.S. Patent Nos. 3,087,936 ; 3,172,892 ; 3,219,666 ; 3,272,746 ; 3,322,670 ; and 3,652,616 , 3,948,800 ; and Canada Patent No. 1,094,044 .
  • Succinate esters are formed by the condensation reaction between hydrocarbyl substituted succinic anhydrides and alcohols or polyols. Molar ratios can vary depending on the alcohol or polyol used. For example, the condensation product of a hydrocarbyl substituted succinic anhydride and pentaerythritol is a useful dispersant.
  • Succinate ester amides are formed by condensation reaction between hydrocarbyl substituted succinic anhydrides and alkanol amines.
  • suitable alkanol amines include ethoxylated polyalkylpolyamines, propoxylated polyalkylpolyamines and polyalkenylpolyamines such as polyethylene polyamines.
  • propoxylated hexamethylenediamine Representative examples are shown in U.S. Patent No. 4,426,305 .
  • the molecular weight of the hydrocarbyl substituted succinic anhydrides used in the preceding paragraphs will typically range between 800 and 2,500 or more.
  • the above products can be post-reacted with various reagents such as sulfur, oxygen, formaldehyde, carboxylic acids such as oleic acid.
  • the above products can also be post reacted with boron compounds such as boric acid, borate esters or highly borated dispersants, to form borated dispersants generally having from 0.1 to 5 moles of boron per mole of dispersant reaction product.
  • Mannich base dispersants are made from the reaction of alkylphenols, formaldehyde, and amines. See U.S. Patent No. 4,767,551 . Process aids and catalysts, such as oleic acid and sulfonic acids, can also be part of the reaction mixture. Molecular weights of the alkylphenols range from 800 to 2,500. Representative examples are shown in U.S. Patent Nos. 3,697,574 ; 3,703,536 ; 3,704,308 ; 3,751,365 ; 3,756,953 ; 3,798,165 ; and 3,803,039 .
  • Typical high molecular weight aliphatic acid modified Mannich condensation products useful in this disclosure can be prepared from high molecular weight alkyl-substituted hydroxyaromatics or HNR 2 group-containing reactants.
  • Hydrocarbyl substituted amine ashless dispersant additives are well known to one skilled in the art; see, for example, U.S. Patent Nos. 3,275,554 ; 3,438,757 ; 3,565,804 ; 3,755,433 , 3,822,209 , and 5,084,197 .
  • Preferred dispersants include borated and non-borated succinimides, including those derivatives from mono-succinimides, bis-succinimides, and/or mixtures of mono- and bis-succinimides, wherein the hydrocarbyl succinimide is derived from a hydrocarbylene group such as polyisobutylene having a Mn of from 500 to 5000, or from 1000 to 3000, or 1000 to 2000, or a mixture of such hydrocarbylene groups, often with high terminal vinylic groups.
  • Other preferred dispersants include succinic acid-esters and amides, alkylphenol-polyamine-coupled Mannich adducts, their capped derivatives, and other related components.
  • Such additives may be used in an amount of 0.1 to 20 weight percent, preferably 0.5 to 8 weight percent, or more preferably 0.5 to 4 weight percent. On an active ingredient basis, such additives may be used in an amount of 0.06 to 14 weight percent, preferably 0.3 to 6 weight percent.
  • the hydrocarbon portion of the dispersant atoms can range from C60 to C400, or from C70 to C300, or from C70 to C200. These dispersants may contain both neutral and basic nitrogen, and mixtures of both. Dispersants can be end-capped by borates and/or cyclic carbonates.
  • the dispersant concentrations are given on an “as delivered” basis.
  • the active dispersant is delivered with a process oil.
  • the "as delivered” dispersant typically contains from 20 weight percent to 80 weight percent, or from 40 weight percent to 60 weight percent, of active dispersant in the "as delivered" dispersant product.
  • Antioxidants retard the oxidative degradation of base oils during service. Such degradation may result in deposits on metal surfaces, the presence of sludge, or a viscosity increase in the lubricant.
  • One skilled in the art knows a wide variety of oxidation inhibitors that are useful in lubricating oil compositions. See, Klamann in Lubricants and Related Products, op cite, and U.S. Patent Nos. 4,798,684 and 5,084,197 , for example.
  • Useful antioxidants include hindered phenols. These phenolic antioxidants may be ashless (metal-free) phenolic compounds or neutral or basic metal salts of certain phenolic compounds. Typical phenolic antioxidant compounds are the hindered phenolics which are the ones which contain a sterically hindered hydroxyl group, and these include those derivatives of dihydroxy aryl compounds in which the hydroxyl groups are in the o- or p-position to each other. Typical phenolic antioxidants include the hindered phenols substituted with C 6 + alkyl groups and the alkylene coupled derivatives of these hindered phenols.
  • phenolic materials of this type 2-t-butyl-4-heptyl phenol; 2-t-butyl-4-octyl phenol; 2-t-butyl-4-dodecyl phenol; 2,6-di-t-butyl-4-heptyl phenol; 2,6-di-t-butyl-4-dodecyl phenol; 2-methyl-6-t-butyl-4-heptyl phenol; and 2-methyl-6-t-butyl-4-dodecyl phenol.
  • Other useful hindered mono-phenolic antioxidants may include for example hindered 2,6-di-alkyl-phenolic proprionic ester derivatives.
  • Bis-phenolic antioxidants may also be advantageously used in combination with the instant disclosure.
  • ortho-coupled phenols include: 2,2'-bis(4-heptyl-6-t-butyl-phenol); 2,2'-bis(4-octyl-6-t-butyl-phenol); and 2,2'-bis(4-dodecyl-6-t-butyl-phenol).
  • Para-coupled bisphenols include for example 4,4'-bis(2,6-di-t-butyl phenol) and 4,4'-methylene-bis(2,6-di-t-butyl phenol).
  • catalytic antioxidants comprise an effective amount of a) one or more oil soluble polymetal organic compounds; and, effective amounts of b) one or more substituted N,N'-diaryl-o-phenylenediamine compounds or c) one or more hindered phenol compounds; or a combination of both b) and c).
  • Catalytic antioxidants are more fully described in U.S. Patent No. 8, 048,833 .
  • Non-phenolic oxidation inhibitors which may be used include aromatic amine antioxidants and these may be used either as such or in combination with phenolics.
  • Typical examples of non-phenolic antioxidants include: alkylated and non-alkylated aromatic amines such as aromatic monoamines of the formula R 8 R 9 R 10 N where R 8 is an aliphatic, aromatic or substituted aromatic group, R 9 is an aromatic or a substituted aromatic group, and R 10 is H, alkyl, aryl or R 11 S(O) X R 12 where R 11 is an alkylene, alkenylene, or aralkylene group, R 12 is a higher alkyl group, or an alkenyl, aryl, or alkaryl group, and x is 0, 1 or 2.
  • the aliphatic group R 8 may contain from 1 to 20 carbon atoms, and preferably contains from 6 to 12 carbon atoms.
  • the aliphatic group is a saturated aliphatic group.
  • both R 8 and R 9 are aromatic or substituted aromatic groups, and the aromatic group may be a fused ring aromatic group such as naphthyl.
  • Aromatic groups R 8 and R 9 may be joined together with other groups such as S.
  • Typical aromatic amines antioxidants have alkyl substituent groups of at least 6 carbon atoms.
  • Examples of aliphatic groups include hexyl, heptyl, octyl, nonyl, and decyl. Generally, the aliphatic groups will not contain more than 14 carbon atoms.
  • the general types of amine antioxidants useful in the present compositions include diphenylamines, phenyl naphthylamines, phenothiazines, imidodibenzyls and diphenyl phenylene diamines. Mixtures of two or more aromatic amines are also useful. Polymeric amine antioxidants can also be used.
  • aromatic amine antioxidants useful in the present disclosure include: p,p'-dioctyldiphenylamine; t-octylphenyl-alphanaphthylamine; phenyl-alphanaphthylamine; and p-octylphenyl-alphanaphthylamine.
  • Sulfurized alkyl phenols and alkali or alkaline earth metal salts thereof also are useful antioxidants.
  • Preferred antioxidants include hindered phenols, arylamines. These antioxidants may be used individually by type or in combination with one another. Such additives may be used in an amount of 0.01 to 5 weight percent, preferably 0.01 to 1.5 weight percent, more preferably zero to less than 1.5 weight percent, more preferably zero to less than 1 weight percent.
  • pour point depressants also known as lube oil flow improvers
  • pour point depressants may be added to lubricating compositions of the present disclosure to lower the minimum temperature at which the fluid will flow or can be poured.
  • suitable pour point depressants include polymethacrylates, polyacrylates, polyarylamides, condensation products of haloparaffin waxes and aromatic compounds, vinyl carboxylate polymers, and terpolymers of dialkylfumarates, vinyl esters of fatty acids and allyl vinyl ethers.
  • 1,815,022 ; 2,015,748 ; 2,191,498 ; 2,387,501 ; 2,655, 479 ; 2,666,746 ; 2,721,877 ; 2,721,878 ; and 3,250,715 describe useful pour point depressants and/or the preparation thereof.
  • Such additives may be used in an amount of 0.01 to 5 weight percent, preferably 0.01 to 1.5 weight percent.
  • Seal compatibility agents help to swell elastomeric seals by causing a chemical reaction in the fluid or physical change in the elastomer.
  • Suitable seal compatibility agents for lubricating oils include organic phosphates, alkoxysulfonlanes (C 10 alcohol, for example), aromatic esters, aromatic hydrocarbons, esters (butylbenzyl phthalate, for example), and polybutenyl succinic anhydride. Such additives may be used in an amount of 0.01 to 3 weight percent, preferably 0.01 to 2 weight percent.
  • Anti-foam agents may advantageously be added to lubricant compositions. These agents retard the formation of stable foams. Silicones and organic polymers are typical anti-foam agents. For example, polysiloxanes, such as silicon oil or polydimethyl siloxane, provide antifoam properties. Anti-foam agents are commercially available and may be used in conventional minor amounts along with other additives such as demulsifiers; usually the amount of these additives combined is less than 1 weight percent and often less than 0.1 weight percent.
  • Antirust additives are additives that protect lubricated metal surfaces against chemical attack by water or other contaminants. A wide variety of these are commercially available.
  • antirust additive is a polar compound that wets the metal surface preferentially, protecting it with a film of oil.
  • Another type of antirust additive absorbs water by incorporating it in a water-in-oil emulsion so that only the oil touches the metal surface.
  • Yet another type of antirust additive chemically adheres to the metal to produce a non-reactive surface.
  • suitable additives include zinc dithiophosphates, metal phenolates, basic metal sulfonates, fatty acids and amines. Such additives may be used in an amount of 0.01 to 5 weight percent, preferably 0.01 to 1.5 weight percent.
  • organic metallic friction modifiers may also be used.
  • Organic metallic friction modifiers useful in this disclosure are any materials that can alter the coefficient of friction of a surface lubricated by any lubricant or fluid containing such material(s).
  • Organic metallic friction modifiers also known as friction reducers, or lubricity agents or oiliness agents, and other such agents that change the ability of base oils, formulated lubricant compositions, or functional fluids, to modify the coefficient of friction of a lubricated surface can be effectively used in combination with the base oils or lubricant compositions of the present disclosure.
  • Organic metallic friction modifiers that lower the coefficient of friction are particularly advantageous in combination with the base oils and lube compositions of this disclosure.
  • Illustrative organic metallic friction modifiers useful in the lubricating engine oil formulations of this disclosure include, for example, molybdenum amine, molybdenum diamine, an organotungstenate, a molybdenum dithiocarbamate, molybdenum dithiophosphates, molybdenum amine complexes, molybdenum carboxylates, and the like. Similar tungsten based compounds may be preferable.
  • Useful concentrations of the organic metallic friction modifiers may range from 0.01 weight percent to 5 weight percent, or 0.1 weight percent to 2.5 weight percent.
  • Useful concentration of molybdenum can range from 25 to 700 ppm, or more preferably from 50 to 200 ppm.
  • additives When lubricating oil compositions contain one or more of the additives discussed above, the additive(s) are blended into the composition in an amount sufficient for it to perform its intended function. Typical amounts of such additives useful in the present disclosure are shown in Table 1 below.
  • the weight amounts in the table below, as well as other amounts mentioned herein, are directed to the amount of active ingredient (that is the non-diluent portion of the ingredient).
  • the weight percent (wt%) indicated below is based on the total weight of the lubricating oil composition.
  • additives are all commercially available materials. These additives may be added independently but are usually precombined in packages which can be obtained from suppliers of lubricant oil additives. Additive packages with a variety of ingredients, proportions and characteristics are available and selection of the appropriate package will take the requisite use of the ultimate composition into account.
  • the detergents used in the formulations were a petroleum derived calcium sulfonate, a synthetic calcium sulfonate, a neutral calcium salicylate, an overbased calcium salicylate, a mixed calcium salicylate, and a magnesium sulfonate.
  • the friction modifiers used in the formulations included organic friction modifiers and organic metallic friction modifiers.
  • the organic friction modifiers were an ethoxylated fatty ester and a mixed glyceride ester (mono, di and tri glyceride), mostly C14, C16, & C18, saturated.
  • the organic metallic friction modifier was a molybdenum dithiocarbamate that was held constant for a majority of the formulations.
  • the antioxidants used in the formulations were a methylene bridged bis-hindered phenol and a alkylated diphenyl amine.
  • Bench testing was conducted for formulations of this disclosure.
  • the bench testing included the following: kinematic viscosity (KV) at 100°C measured by ASTM D445; integrated mini traction machine (MTM) friction at 140°C measured as described below; and thermo-oxidation engine oil simulation (TEOST 33C) measured by ASTM D6335.
  • KV kinematic viscosity
  • MTM integrated mini traction machine
  • TEOST 33C thermo-oxidation engine oil simulation
  • the Mini Traction Machine is a fully automated instrument manufactured by PCS Instruments and identified as Model MTM.
  • the test specimens and apparatus configuration are such that realistic pressure, temperature and speed can be attained without requiring very large loads, motors or structures.
  • a small sample of fluid (50 milliliters) is placed in a test cell and the machine automatically runs either through a range of speeds, slide-to-roll ratios, temperatures and loads, or at specifically set temperature, slide-to-roll ratio and speed range to generate information regarding the friction performance of a test fluid without further operator intervention.
  • the working of the MTM is known and familiar to those of skill in the art.
  • Fig. 1 provides formulation details in weight percent based on the total weight percent of the formulation.
  • a synthetic oil was used as baseline and contained both organic metallic and organic friction modifiers to allow for comparison of the different chemistries. Additional cleanliness and average integrated MTM Stribeck friction data were also collected on oil containing only organic metallic friction modifier, Comparative Example 3, as well as no friction modifier, Comparative Example 2, to provide a reference. All other components were the same across all three blends with the differences being made up by base oil.
  • Fig. 1 summarizes the three oils considered baseline comparison oils for the 0W-20 oils of this disclosure and their respective TEOST 33C and average integrated friction coefficient from MTM Stribeck measurements at 140°C.
  • an integration method (the trapezoidal rule) was employed for each curve individually and an average integrated Stribeck friction coefficient and standard deviation for all 4 traces, run back-to-back, was calculated.
  • the average integrated Stribeck friction coefficient provides a measure of the friction an engine will see during operation (albeit at different ratios to those calculated).
  • the MTM integrated area value listed in this disclosure has been calculated using this method.
  • FIG. 3 shows a comparison of the MTM performance for the baseline oil with mixed glyceride ester and an organic metallic friction modifier versus that of a blend with a 1% treat of ethoxylated fatty ester and no mixed glyceride ester or an organic metallic friction modifier.
  • Fig. 4 shows the TEOST 33C performance for a number of blends with ethoxylated fatty ester, mixed glyceride ester, or a combination of both.
  • Fig. 4 shows multiple formulation changes which were made to reduce the TEOST 33C deposits with minimal impact on the friction reduction benefit for ethoxylated fatty ester.
  • the MTM results show that the friction is reduced with the combination of ethoxylated fatty ester and mixed glyceride ester versus the performance of the baseline formulation.
  • Inventive Example 1 thus shows that the use of mixed friction modifier chemistries is unexpectedly used to improve deposits, while maintaining or reducing friction.
  • Inventive Example 2 improve TEOST 33C performance compared to Comparative Example 4 and Comparative Example 5. While these modifications, such as an increase in overbased detergent or dispersant, are expected to have a significant detrimental impact on MTM friction performance, Inventive Example 2 shows that they surprisingly maintain the same level of friction benefit obtained in Inventive Example 1.
  • Fig. 5 shows formulation details in weight percent based on the total weight percent of the formulation, of various formulations.
  • Fig. 5 also shows the results of bench testing of the formulations using thermo-oxidation engine oil simulation TEOST 33C and MTM friction coefficient.
  • the concentrations in weight percent of the friction modifiers ethoxylated fatty ester and mixed glyceride ester
  • the weight percent of the remaining ingredients remains the same.
  • the detergent used in the formulations was an overbased calcium salicylate.
  • the friction modifiers used in the formulations included organic friction modifiers.
  • the organic friction modifiers were an ethoxylated fatty ester and a mixed glyceride ester.
  • An organic metallic friction modifier i.e., molybdenum dithiocarbamate was also used in the formulations.
  • PIB dispersants antioxidants, antiwear agents, and pour point depressants were also used in the formulations.
  • Fig. 6 shows formulation details in weight percent based on the total weight percent of the formulation, of various formulations.
  • Fig. 6 also shows the results of bench testing of the formulations using thermo-oxidation engine oil simulation (TEOST 33C) measured by ASTM D6335 and MTM friction.
  • TEOST 33C thermo-oxidation engine oil simulation
  • Inventive Examples 21 through Inventive Example 28 demonstrate that a treatment of overbased calcium salicylate detergent of from 0.5 wt% to 2.5 wt%, and a treatment of PIB dispersant of from 2.0 wt% to 5.0 wt% may be used in combination with the mixed friction modifier chemistries to achieve deposit and/or friction benefits.
  • the lubricating engine oil formulations in Figure 7 are combinations of additives and base stocks and are expected to have kinematic viscosity at 100°C around 6 cSt and high temperature high shear (10 -6 s -1 ) viscosity at 150°C around 2.0 cP.
  • the lubricating engine oil formulations of Examples 1, 2, 3, 4, and 5 are expected to have phosphorus levels around 650 ppm, while Example 6 will have around 350 ppm phosphorus and Example 7 will have around 1300 ppm phosphorus.
  • the lubricating engine oil formulations of Examples 1, 4, 5, 6, 7 are expected to have molybdenum levels around 800 ppm while Example 2 will have around 0 ppm of molybdenum and Example 3 will have around 275 ppm of molybdenum.
  • the lubricant formulations of Examples 1, 2, 3, 6, 7 are expected to have TBN values around 9 while Example 4 will have a TBN value of around 6 and Example 5 will have a TBN value of around 15.
  • the lubricant formulations of Examples 1, 2, 3, 6, 7 are expected to have ash levels around 0.95% while the formulations in example 5 will have around 0.6% ash and example 6 will have around 1.6% ash.
  • the lubricating engine oil formulations in Figure 8 are combinations of additives and base stocks and are expected to have kinematic viscosities at 100°C of around 8 cSt and high temperature high shear (10 -6 s -1 ) viscosity at 150°C of around 2.6 cP.
  • the lubricating engine oil formulations of Examples 8, 9, 10, 11, 12 are expected to have phosphorus levels of around 650ppm while Example 13 will have around 350 ppm Phosphorus and Example 14 will have around 1300 ppm Phosphorus.
  • the lubricating engine oil formulations of Examples 8, 11, 12, 13, 14 are expected to have molybdenum levels of around 800 ppm while Example 9 will have around 0 ppm of molybdenum and Example 10 will have around 275 ppm of molybdenum.
  • the lubricant formulations of Examples 8, 9, 10, 13, 14 are expected to have TBN values of around 9 while Example 11 will have a TBN value of around 6 and Example 12 will have a TBN value of around 15.
  • the lubricant formulations of Examples 8, 9, 10, 13, 14 are expected to have ash levels of around 0.95% while the formulations in example 11 will have around 0.6% ash and example 12 will have around 1.6% ash.
  • the lubricating engine oil formulations in Figure 9 are combinations of additives and base stocks and are expected to have kinematic viscosity at 100°C around 10 cSt and high temperature high shear (10 -6 s -1 ) viscosity at 150°C of around 3.0 cP.
  • the lubricating engine oil formulations of Examples 15, 16, 17, 18, 19 are expected to have phosphorus levels of around 650 ppm while Example 20 will have around 350 ppm phosphorus and Example 21 will have around 1300 ppm phosphorus.
  • the lubricating engine oil formulations of Examples 15, 18, 19, 20, 21 are expected to have molybdenum levels of around 800 ppm while Example 16 will have around 0 ppm of molybdenum and Example 17 will have around 275 ppm of molybdenum.
  • the lubricant formulations of Examples 15, 16, 17, 20, 21 are expected to have TBN values of around 9 while Example 18 will have a TBN value of around 6 and Example 19 will have a TBN value of around 15.
  • the lubricant formulations of Examples 15, 16, 17, 20, 21 are expected to have ash levels of around 0.95% while the formulations in example 18 will have around 0.6% ash and example 19 will have around 1.6% ash.

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  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Lubricants (AREA)
  • Lubrication Of Internal Combustion Engines (AREA)

Claims (7)

  1. Verwendung einer Reibungsmodifizierermischung zur Verbesserung der Kraftstoffeffizienz und zur Herabsetzung der Reibungseigenschaften, während die Kontrolle von Ablagerungen erhalten bleibt oder verbessert wird, in einem Motor, der mit einem Schmieröl mit einer Zusammensetzung geschmiert wird, die 50 bis 99 Gew.%, bezogen auf das Gesamtgewicht des Schmieröls, von einem Schmierölbasismaterial als Hauptkomponente umfasst, bei der die Reibungsmodifizierermischung einen ethoxylierten Fettsäureester und einen Glycerinfettsäureester in einem Gewichtsverhältnis von 0,1:1 bis 1:0,1 umfasst und in einem Bereich von 0,1 bis 1,5 Gew.% vorhanden ist, bezogen auf das Gesamtgewicht des Schmieröls, und bei der Kraftstoffeffizienz und Reibungsherabsetzungseigenschaften verbessert werden und die Kontrolle von Ablagerungen erhalten bleibt oder verbessert wird, verglichen mit den Reibungsherabsetzungseigenschaften und der Kontrolle von Ablagerungen, die unter Verwendung eines Schmieröls erreicht werden, das eine geringfügige Komponente enthält, die von der Reibungsmodifizierermischung verschieden ist.
  2. Verwendung nach Anspruch 1, bei der das Schmierölbasismaterial ein Basisöl der Gruppe I, Gruppe II, Gruppe III, Gruppe IV oder Gruppe V umfasst.
  3. Verwendung nach den Ansprüchen 1 und 2, bei der im Vergleich mit Kraftstoffeffizienz, die unter Verwendung eines Motorschmieröls erreicht wird, das eine geringfügige Komponente enthält, die von der Reibungsmodifizierermischung verschieden ist, das Motorschmieröl, welches die Reibungsmodifizierermischung enthält, eine Kraftstoffeffizienz, FEI-Summe, größer als 1,1X zeigt, bestimmt durch einen Motortest gemäß "Sequence VID Fuel Economy" (ASTM D7589) .
  4. Motorschmieröl mit einer Zusammensetzung, die 50 bis 99 Gew.%, bezogen auf das Gesamtgewicht des Schmieröls, von einem Schmierölbasismaterial als Hauptkomponente und eine Reibungsmodifizierermischung umfasst, die einen ethoxylierten Fettsäureester und einen Glycerinfettsäureester in einem Gewichtsverhältnis von 0,1:1 bis 1:0,1 umfasst, wobei die Reibungsmodifizierermischung in einem Bereich von 0,1 bis 1,0 Gew.% vorhanden ist, bezogen auf das Gesamtgewicht des Schmieröls, und wobei Kraftstoffeffizienz und Reibungsherabsetzungseigenschaften verbessert werden und die Kontrolle von Ablagerungen erhalten bleibt oder verbessert wird, verglichen mit den Reibungsherabsetzungseigenschaften und der Kontrolle von Ablagerungen, die unter Verwendung eines Motorschmieröls erreicht werden, das eine geringfügige Komponente enthält, die von der Reibungsmodifizierermischung verschieden ist.
  5. Motorschmieröl nach Anspruch 4, bei dem das Schmierölbasismaterial ein Basisöl der Gruppe I, Gruppe II, Gruppe III, Gruppe IV oder Gruppe V umfasst.
  6. Motorschmieröl nach den Ansprüchen 4 und 5, bei dem im Vergleich mit der Kraftstoffeffizienz, die unter Verwendung eines Motorschmieröls erreicht wird, das eine geringfügige Komponente enthält, die von der Reibungsmodifizierermischung verschieden ist, das Motorschmieröl, welches die Reibungsmodifizierermischung enthält, eine Kraftstoffeffizienz, FEI-Summe, größer als 1,1X zeigt, bestimmt durch einen Motortest gemäß "Sequence VID Fuel Economy" (ASTM D7589) .
  7. Motorschmieröl nach den Ansprüchen 4 bis 6 oder Verwendung nach den Ansprüchen 1 bis 3, wobei in Reibungsmessungen des Schmieröls mittels Minitraktionsmaschine (MTM) im Stribeck-Modus bei 140°C der integrierte Stribeck-Reibungskoeffizient des Schmieröls in der MTM herabgesetzt ist, verglichen mit dem integrierten Stribeck-Reibungskoeffizienten eines Schmieröls, das eine geringfügige Komponente enthält, die von der Reibungsmodifizierermischung verschieden ist, und wobei in Ablagerungsmessungen des Schmieröls mittels thermooxidativer Motorölsimulation (TEOST 33C), gemessen gemäß ASTM D6335, die Menge an Gesamtablagerungen herabgesetzt wird oder erhalten bleibt, verglichen mit der Menge an Gesamtablagerungen in einem Schmieröl, das eine geringfügige Komponente enthält, die von der Reibungsmodifizierermischung verschieden ist.
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