US20040259742A1 - Use of dispersant viscosity index improvers in exhaust gas recirculation engines - Google Patents

Use of dispersant viscosity index improvers in exhaust gas recirculation engines Download PDF

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US20040259742A1
US20040259742A1 US10/464,614 US46461403A US2004259742A1 US 20040259742 A1 US20040259742 A1 US 20040259742A1 US 46461403 A US46461403 A US 46461403A US 2004259742 A1 US2004259742 A1 US 2004259742A1
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Prior art keywords
engine
lubricating oil
oil
olefin copolymer
viscosity index
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US10/464,614
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Munmaya Mishra
David Venhaus
Charles Passut
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Afton Chemical Intangibles LLC
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Afton Chemical Intangibles LLC
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Priority to US10/464,614 priority Critical patent/US20040259742A1/en
Assigned to ETHYL CORPORATION reassignment ETHYL CORPORATION ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: MISHRA, MUNMAYA K., PASSUT, CHARLES A., VENHAUS, DAVID A.
Assigned to ETHYL CORPORATION reassignment ETHYL CORPORATION ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: MISHRA, MUNMAYA K., PASSUT, CHARLES A., VENHAUS, DAVID A.
Priority to CA002464895A priority patent/CA2464895A1/en
Priority to SG200402407A priority patent/SG122821A1/en
Priority to AU2004202270A priority patent/AU2004202270B2/en
Priority to EP04253603A priority patent/EP1489281A3/en
Priority to CNA2004100495759A priority patent/CN1573069A/en
Priority to JP2004180085A priority patent/JP2005008887A/en
Assigned to SUNTRUST BANK, AS ADMINISTRATIVE AGENT reassignment SUNTRUST BANK, AS ADMINISTRATIVE AGENT SECURITY INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: ETHYL CORPORATION
Assigned to AFTON CHEMICAL INTANGIBLES LLC reassignment AFTON CHEMICAL INTANGIBLES LLC ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: ETHYL CORPORATION
Publication of US20040259742A1 publication Critical patent/US20040259742A1/en
Assigned to SUNTRUST BANK reassignment SUNTRUST BANK SECURITY AGREEMENT Assignors: AFTON CHEMICAL INTANGIBLES LLC
Assigned to AFTON CHEMICAL INTANGIBLES LLC reassignment AFTON CHEMICAL INTANGIBLES LLC RELEASE BY SECURED PARTY (SEE DOCUMENT FOR DETAILS). Assignors: SUNTRUST BANK
Abandoned legal-status Critical Current

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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02BINTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
    • F02B47/00Methods of operating engines involving adding non-fuel substances or anti-knock agents to combustion air, fuel, or fuel-air mixtures of engines
    • F02B47/04Methods of operating engines involving adding non-fuel substances or anti-knock agents to combustion air, fuel, or fuel-air mixtures of engines the substances being other than water or steam only
    • F02B47/08Methods of operating engines involving adding non-fuel substances or anti-knock agents to combustion air, fuel, or fuel-air mixtures of engines the substances being other than water or steam only the substances including exhaust gas
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    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M133/00Lubricating compositions characterised by the additive being an organic non-macromolecular compound containing nitrogen
    • C10M133/52Lubricating compositions characterised by the additive being an organic non-macromolecular compound containing nitrogen having a carbon chain of 30 or more atoms
    • C10M133/58Heterocyclic compounds
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    • C10M135/00Lubricating compositions characterised by the additive being an organic non-macromolecular compound containing sulfur, selenium or tellurium
    • C10M135/20Thiols; Sulfides; Polysulfides
    • C10M135/22Thiols; Sulfides; Polysulfides containing sulfur atoms bound to acyclic or cycloaliphatic carbon atoms
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    • C10M135/20Thiols; Sulfides; Polysulfides
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    • C10M149/02Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
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    • C10M151/02Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02MSUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M26/00Engine-pertinent apparatus for adding exhaust gases to combustion-air, main fuel or fuel-air mixture, e.g. by exhaust gas recirculation [EGR] systems
    • F02M26/13Arrangement or layout of EGR passages, e.g. in relation to specific engine parts or for incorporation of accessories
    • F02M26/22Arrangement or layout of EGR passages, e.g. in relation to specific engine parts or for incorporation of accessories with coolers in the recirculation passage
    • F02M26/23Layout, e.g. schematics
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    • C10M2203/00Organic non-macromolecular hydrocarbon compounds and hydrocarbon fractions as ingredients in lubricant compositions
    • C10M2203/10Petroleum or coal fractions, e.g. tars, solvents, bitumen
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    • C10N2010/04Groups 2 or 12
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    • C10N2020/00Specified physical or chemical properties or characteristics, i.e. function, of component of lubricating compositions
    • C10N2020/01Physico-chemical properties
    • C10N2020/02Viscosity; Viscosity index
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    • C10N2040/00Specified use or application for which the lubricating composition is intended
    • C10N2040/25Internal-combustion engines
    • C10N2040/255Gasoline engines
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/10Internal combustion engine [ICE] based vehicles
    • Y02T10/12Improving ICE efficiencies

Definitions

  • the present invention in an embodiment relates to a cooled exhaust gas recirculation (also called recycle) engine lubricated with a lubricating oil comprising a dispersant viscosity index improver in an amount and of a type sufficient to thereby achieve acceptable reduction in oil thickening due to increased soot accumulation.
  • a cooled exhaust gas recirculation also called recycle
  • a lubricating oil comprising a dispersant viscosity index improver in an amount and of a type sufficient to thereby achieve acceptable reduction in oil thickening due to increased soot accumulation.
  • EGR exhaust gas recirculation or recycle
  • copolymer herein is meant and included copolymers or terpolymers of ethylene and C 3 to C 23 alpha-olefin, and optionally a non-conjugated diene or triene, on which has been grafted ethylenically unsaturated carboxylic reactants.
  • the cooled EGR engines within the scope of the present invention include automotive engines, heavy and light duty diesel and gasoline truck engines, gasoline combustion engines, diesel engines, hybrid Internal Combustion/electric engines. These can include EGR engines cooled by the circulation or heat exchange of water, water/hydrocarbon blends or mixtures, water/glycol mixtures, and/or air or gas.
  • a lubricated engine comprising an exhaust gas recirculation system, whereby exhaust gases comprising soot generated in the combustion in the engine of fuel contact a lubricating oil used to lubricate said engine, wherein said lubricating oil comprises: a base oil, and at least one dispersant viscosity index improver in an amount and type sufficient to reduce the amount of oil thickening of the lubricating oil.
  • a lubricating oil produces a passing result in the Mack T-11 EGR equipped diesel engine test by maintaining a kinematic viscosity of about 20.0 or less, even at soot levels of up to about 8.9% by mass.
  • an EGR engine lubricated with a lubricating oil that contains, inter alia, a viscosity-controlling amount of a highly grafted, multi-functional olefin copolymer that comprises the reaction product of (1) an acylated olefin copolymer, wherein the acylated copolymer comprises copolymers or terpolymers of ethylene and C 3 to C 23 alpha-olefin and optionally a non-conjugated diene or triene on which has been grafted ethylenically unsaturated carboxylic reactants to a level of 0.15 to 1.0 carboxylic groups per 1000 number average molecular weight units (Mn), and (2) a polyamine compound selected from the group consisting of:
  • R 1 is hydrogen, —NH-aryl, —NH-arylalkyl, —NH-alkyl, or a branched or straight chain radical having from 4 to 24 carbon atoms that can be alkyl, alkenyl, alkoxyl, aralkyl, alkaryl, hydroxyalkyl or aminoalkyl
  • R 2 is —NH 2 , CH 2 —(CH 2 ) n —NH 2 , CH 2 -aryl-NH 2 , in which n has a value from 1 to 10
  • R 3 is hydrogen, alkyl, alkenyl, alkoxyl, aralkyl, alkaryl having from 4 to 24 carbon atoms;
  • aminothiazole from the group consisting of aminothiazole, aminobenzothiazole, aminobenzo-thiadiazole and aminoalkylthiazole;
  • R and R 1 represent hydrogen or an alkyl, alkenyl or alkoxyl radical having from 1 to 14 carbon atoms; (d) an aminoindole represented by the formula:
  • R represents hydrogen or an alkyl radical having from 1 to 14 carbon atoms
  • R is a divalent alkylene radical having 2-6 carbon atoms and R 1 is hydrogen or an alkyl radical having from 1 to 14 carbon atoms;
  • R is hydrogen or an alkyl radical having from 1 to 14 carbon atoms
  • R can be absent or is a C 1 -C 10 linear or branched hydrocarbon selected from the group consisting of alkyl, alkenyl, arylalkyl, or aryl;
  • R represents hydrogen or an alkyl or alkoxy radical having from 1 to 14 carbon atoms
  • aminoalkyl imidazoles such as 1-(2-aminoethyl) imidazole, 1-(3-aminopropyl) imidazole;
  • aminoalkyl morpholines such as 4-(3-aminopropyl) morpholine.
  • novel lubricated cooled EGR engines described herein contain lubricating compositions that comprise an oil of lubricating viscosity and a dispersant VII effective amount of the highly grafted, multi-functional olefin copolymer dispersant as described above.
  • polymers for use herein may include copolymers of ethylene and one or more C 3 to C 23 alpha-olefins.
  • Copolymers of ethylene and propylene are very effective.
  • Other alpha-olefins suitable in place of propylene to form the copolymer or to be used in combination with ethylene and propylene to form a terpolymer include 1-butene, 1-pentene, 1-hexene, 1-octene and styrene; ⁇ , ⁇ -diolefins such as 1,5-hexadiene, 1,6-heptadiene, 1,7-octadiene; branched chain alpha-olefins such as 4-methylbutene-1,5-methylpentene-1 and 6-methylheptene-1; and mixtures thereof.
  • More complex polymer substrates may be prepared using a third component in preparing the dispersant used in the oil to lubricate the cooled EGR engines.
  • the third component generally used to prepare an interpolymer substrate is a polyene monomer selected from non-conjugated dienes and trienes.
  • the non-conjugated diene component is one having from 5 to 14 carbon atoms in the chain.
  • the diene monomer is characterized by the presence of a vinyl group in its structure and can include cyclic and bicyclo compounds.
  • dienes include 1,4-hexadiene, 1,4-cyclohexadiene, dicyclopentadiene, 5-ethylidene-2-norbornene, 5-methylene-2-norborene, 1,5-heptadiene, and 1,6-octadiene.
  • a mixture of more than one diene can be used in the preparation of the interpolymer.
  • a non-conjugated diene for preparing a terpolymer or interpolymer substrate is 1,4-hexadiene.
  • the triene component will have at least two non-conjugated double bonds, and up to about 30 carbon atoms in the chain.
  • Typical trienes useful in preparing the interpolymer of the invention are 1-isopropylidene-3 ⁇ ,4,7,7 ⁇ -tetrahydroindene, 1-isopropylidenedicyclopentadiene, dihydro-isodicyclopentadiene, and 2-(2-methylene-4-methyl-3-pentenyl)[2.2.1] bicyclo-5-heptene.
  • Ethylene-propylene or higher alpha-olefin copolymers may consist of from about 15 to 80 mole percent ethylene and from about 85 to 20 mole percent C 3 to C 23 alpha-olefin with the mole ratios being from about 35 to 75 mole percent ethylene and from about 65 to 25 mole percent of a C 3 to C 23 alpha-olefin.
  • the proportions are from 50 to 70 mole percent ethylene and 50 to 30 mole percent C 3 to C 23 alpha-olefin.
  • the proportions are from 55 to 65 mole percent ethylene and 45 to 35 mole percent C 3 to C 23 alpha-olefin.
  • Terpolymer variations of the foregoing polymers may contains from about 0.1 to 10 mole percent of a non-conjugated diene or triene.
  • polymer for the dispersant viscosity index improver used in an oil to lubricate a cooled EGR engine is a polymer selected from the group consisting of polymethacrylates, ethylene/propylene copolymers, polyisoprene or saturated polyisoprene, and polyisoprene/saturated polyisoprene copolymers.
  • the polymer substrate that is the ethylene copolymer or terpolymer
  • polymer and copolymer are used generically to encompass ethylene copolymers, terpolymers or interpolymers. These materials may contain minor amounts of other olefinic monomers so long as the basic characteristics of the ethylene copolymers are not materially changed.
  • the polymerization reaction used to form the ethylene-olefin copolymer substrate is generally carried out in the presence of a conventional Ziegler-Natta or metallocene catalyst system.
  • the polymerization medium is not specific and can include solution, slurry, or gas phase processes, as known to those skilled in the art.
  • the solvent may be any suitable inert hydrocarbon solvent that is liquid under reaction conditions for polymerization of alpha-olefins; examples of satisfactory hydrocarbon solvents include straight chain paraffins having from 5 to 8 carbon atoms, with hexane being preferred.
  • Aromatic hydrocarbons preferably aromatic hydrocarbon having a single benzene nucleus, such as benzene, toluene and the like; and saturated cyclic hydrocarbons having boiling point ranges approximating those of the straight chain paraffinic hydrocarbons and aromatic hydrocarbons described above, are particularly suitable.
  • the solvent selected may be a mixture of one or more of the foregoing hydrocarbons.
  • the liquid phase for polymerization is preferably liquid propylene. It is desirable that the polymerization medium be free of substances that will interfere with the catalyst components.
  • An ethylenically unsaturated carboxylic acid material is next grafted onto the prescribed polymer backbone to form an acylated ethylene copolymer.
  • These carboxylic reactants which are suitable for grafting onto the ethylene copolymer contain at least one ethylenic bond and at least one, preferably two, carboxylic acid or its anhydride groups or a polar group which is convertible into said carboxyl groups by oxidation or hydrolysis.
  • the carboxylic reactants are in one embodiment selected from the group consisting of acrylic, methacrylic, cinnamic, crotonic, maleic, fumaric and itaconic reactants.
  • the carboxylic reactants are selected from the group consisting of maleic acid, fumaric acid, maleic anhydride, or a mixture of two or more of these.
  • Maleic anhydride or a derivative thereof has advantages of commercial availability and ease of reaction.
  • itaconic acid or its anhydride are useful due to its reduced tendency to form a cross-linked structure during the free-radical grafting process.
  • the ethylenically unsaturated carboxylic acid materials typically can provide one or two carboxylic groups per mole of reactant to the grafted polymer. That is, methyl methacrylate can provide one carboxylic group per molecule to the grafted polymer while maleic anhydride can provide two carboxylic groups per molecule to the grafted polymer.
  • the carboxylic reactant is grafted onto the prescribed polymer backbone in an amount to provide 0.15 to 1.0 carboxylic groups per 1000 number average molecular weight units of the polymer backbone, preferably 0.3 to 0.5 carboxylic groups per 1000 number average molecular weight.
  • a copolymer substrate with Mn of 20,000 is grafted with 6 to 10 carboxylic groups per polymer chain or 3 to 5 moles of maleic anhydride per mole of polymer.
  • a copolymer with Mn of 100,000 is grafted with 30 to 50 carboxylic groups per polymer chain or 15 to 25 moles of maleic anhydride per polymer chain.
  • the minimum level of functionality is the level needed to achieve the minimum satisfactory dispersancy performance in the lubricated cooled EGR engines.
  • the grafting reaction to form the acylated olefin copolymers is generally carried out with the aid of a free-radical initiator either in solution or in bulk, as in an extruder or intensive mixing device.
  • a free-radical initiator either in solution or in bulk, as in an extruder or intensive mixing device.
  • the polymerization is carried out in hexane solution, it is economically convenient but not required herein to carry out the grafting reaction in hexane as described in U.S. Pat. Nos. 4,340,689, 4,670,515 and 4,948,842, incorporated herein by reference.
  • the resulting polymer intermediate is characterized by having carboxylic acid acylating functionality randomly within its structure.
  • the highly grafted, multi-functional olefin copolymer dispersant VIIs used to lubricate the cooled EGR engines of the present invention can be incorporated into a lubricating oil in any convenient way.
  • the highly grafted, multi-functional olefin copolymers can be added directly to the lubricating oil by dispersing or dissolving the same in the lubricating oil at the desired level of concentration. Such blending into the lubricating oil can occur at room temperature or elevated temperatures.
  • the highly grafted, multi-functional olefin copolymers can be blended with a suitable oil-soluble solvent/diluent (such as benzene, xylene, toluene, lubricating base oils and petroleum distillates) to form a concentrate, and then blending the concentrate with a lubricating oil to obtain the final formulation.
  • a suitable oil-soluble solvent/diluent such as benzene, xylene, toluene, lubricating base oils and petroleum distillates
  • Such additive concentrates will typically contain (on an active ingredient (A.I.) basis) from about 3 to about 45 wt. %, and often from about 10 to about 35 wt. %, highly grafted, multi-functional olefin copolymer additive, and more often from about 40 to 60 wt %, base oil based on the concentrate weight.
  • the highly grafted, multi-functional olefin copolymer products useful in lubricating oils to lubricate cooled EGR engines of the present invention find their primary utility in lubricating oil compositions which employ a base oil in which the additives are dissolved or dispersed.
  • base oils may be natural, synthetic or mixtures thereof.
  • Base oils suitable for use in preparing the lubricating oil compositions of the present invention include those conventionally employed as crankcase lubricating oils for spark-ignited and compression-ignited internal combustion engines, such as automobile and truck engines, marine and railroad diesel engines, and the like.
  • the additives in the form of 10 to 80 wt. % active ingredient concentrates in hydrocarbon oil, e.g. mineral lubricating oil, or other suitable solvent.
  • hydrocarbon oil e.g. mineral lubricating oil, or other suitable solvent.
  • these concentrates may be diluted with 3 to 100, e.g., 5 to 40, parts by weight of lubricating oil per part by weight of the additive package in forming finished lubricants, e.g. crankcase motor oils.
  • the purpose of concentrates is to make the handling of the various materials less difficult and awkward as well as to facilitate solution or dispersion in the final blend.
  • the highly grafted, multi-functional olefin copolymer dispersant VII would usually be employed in the form of a 10 to 50 wt. % concentrate, for example, in a lubricating oil fraction.
  • the amount of dispersant viscosity index improver in the lubricating oil in the cooled EGR engine can be from about 20 wt. % to about 18 wt. %.
  • the highly grafted, multi-functional olefin copolymer dispersant VIIs used in an oil to lubricate the cooled EGR engines of the present invention will generally be used in admixture with a lube oil basestock, comprising an oil of lubricating viscosity, including natural lubricating oils, synthetic lubricating oils and mixtures thereof.
  • Natural oils include animal oils and vegetable oils (e.g., castor, lard oil), liquid petroleum oils and hydrorefined, solvent-treated or acid-treated mineral lubricating oils of the paraffinic, naphthenic and mixed paraffinic-naphthenic types. Oils of lubricating viscosity derived from coal or shale are also useful base oils.
  • the synthetic lubricating oils used in this invention include one of any number of commonly used synthetic hydrocarbon oils, which include, but are not limited to, poly-alpha-olefins, alkylated aromatics, alkylene oxide polymers, interpolymers, copolymers and derivatives thereof where the terminal hydroxyl groups have been modified by esterification, etherification etc, esters of dicarboxylic acids and silicon-based oils.
  • the present invention is further directed to a method of improving fuel economy and fuel economy durability of a vehicle having a cooled EGR engine, wherein said method comprises adding to and operating in the crankcase of the vehicle the lubricating oil composition containing the olefin copolymer dispersant VII described herein.
  • the highly grafted, multi-functional olefin copolymers used in the oils to lubricate the cooled EGR engines of the present invention may be post-treated so as to impart additional properties necessary or desired for a specific lubricant application.
  • Post-treatment techniques are well known in the art and include boronation, phosphorylation, and maleination.
  • the EGR engine is lubricated with a lubricating oil further comprising an additive selected from the group consisting of zinc dialkyl dithiophosphates, friction modifiers, antioxidants, defoamants, surfactants, corrosion inhibitors, extreme pressure agents, detergents, and pour point depressants.
  • an additive selected from the group consisting of zinc dialkyl dithiophosphates, friction modifiers, antioxidants, defoamants, surfactants, corrosion inhibitors, extreme pressure agents, detergents, and pour point depressants.
  • an EGR engine is lubricated with an oil comprising a highly grafted, multi-functional olefin copolymer viscosity modifier, also called a viscosity index improver, comprising the reaction product of an acylated olefin copolymer and a polyamine, wherein the acylated olefin copolymer comprises an olefin copolymer having grafted thereon from 0.15 to 1.0 carboxylic groups per 1000 number average molecular weight units of olefin copolymer and wherein the olefin copolymer has a number average molecular weight of between 10,000 and 150,000.
  • a highly grafted, multi-functional olefin copolymer viscosity modifier also called a viscosity index improver
  • the lubricated cooled EGR engine of the present invention can surprisingly pass the M-11 EGR crosshead wear and dispersancy test, the T-10 test, and the Mack T-11 test (EGR equipped diesel engines).
  • Conventional lubricating oils containing certain known dispersants including Ethyl's HiTEC® 5772 dispersant and non-dispersant VIIs have not been able to pass all of these tests in cooled EGR engines.
  • the dispersant VIIs disclosed herein as useful in lubricating oils in a cooled EGR engine can be used in conjunction with other dispersants.
  • Table I shows HiTEC® 5777 alone, HiTEC® 5777 plus HiTEC® 5772, and HiTEC® 5772 alone, when used to lubricate a Cummins cooled EGR engine after 250 hours.
  • TABLE I 0.1 wt. % H5777 % Active wt. % H5772 % Active Oil Viscosity 1 5.0 1.41 0 0 25.04 2 4.5 1.27 4.0 0.76 27.03 3 3.1 0.87 3.7 0.70 33.28 4 0 0 5.35 1.01 66.73
  • the lubricated engine achieves a viscosity increase of less than 10 cSt at 100° C. at a soot level of up to 6.0% m in the Mack T-11 test.
  • Another embodiment herein provides a lubricated EGR engine wherein the lubricating oil passes the Mack T-11 test at a viscosity increase of less than 8 cSt at 100° C. at a soot level of up to 6.09% m in the Mack T-11 test.
  • a lubricated EGR engine wherein the lubricating oil has a viscosity increase of less than 10 cSt at 100° C. and up to 6.0% m soot in the Mack T-11 test.
  • Lubricating oil films containing the olefin copolymer dispersant VIIs defined herein provide excellent performance in the Mack T-11 test, reduce both high and low temperature thickening, give superior sludge performance, and give superior wear protection from soot.
  • the present invention provides a method to extend the service time between oil drains in a vehicle equipped with an exhaust gas recirculation engine up to about 60,000 miles by the addition to a lubricating oil in the engine of an olefin copolymer dispersant VII as described herein.
  • the oils containing the olefin copolymer dispersant VII as taught herein also have the following advantages when used in cooled EGR engines: excellent for building film strength and reducing wear; low treat rate of, for example, 8.5% wt. ( ⁇ 9.5% vol.) for 15W-40; strong sludge suppression performance; provides superior performance in EGR engines; good shear stability, permanent and HTHS; excellent dispersancy for soot handling and improved wear protection; allows for lower additive treat rate; and excellent used-oil low temperature viscosity properties, relative to the low temperature viscosity properties of oils not containing the olefin copolymer dispersant VII as taught herein.
  • FIG. 1 illustrates that by the use in the cooled EGR engine of a lubricating oil containing the olefin dispersant copolymer VII described herein, the oil exhibited a kinematic viscosity at 100° C. that does not increase rapidly in high soot loading, whereas the kinematic viscosity of the industry standard reference oil increases rapidly beyond the 4% soot loading level.
  • FIG. 1 shows viscosities for lubricating oils using Group I and Group II base oils.
  • a particularly useful olefin copolymer dispersant VII for addition to a lubricating oil in a cooled EGR engine is HiTEC® 5777 Dispersant available from Ethyl Corporation, Richmond, Va.
  • FIG. 2 illustrates the effect on viscosity measured at 25° C. of increasing weight percent of soot loading in a lubricating oil containing an olefin copolymer dispersant viscosity index improver, Ethyl's HiTEC® 5777 dispersant additive.
  • the Figure shows a curve for Group I and for Group II base oils in this low temperature Mack T-8E test.
  • the additive HiTEC® 5777 allowed the maintenance of low temperature viscosity below the 15W limit to a loading of over 6% soot in Group I base oil and to over 9% soot in Group II base oil.
  • FIG. 3 illustrates the performance in a cooled EGR engine of a lubricating oil labeled C1-4 D1 containing HiTEC® 5777 versus a standard reference oil CH-4 in the common extended T-8E test for viscosity change caused by soot loading. It is clear that the use in a cooled EGR engine of the olefin copolymer dispersant VII described herein significantly restricted the viscosity increase at higher soot levels.
  • a cooled EGR engine was lubricated with an oil containing an olefin copolymer dispersant VII prepared as follows: An acylated ethylene-propylene copolymer was prepared by free radically grafting maleic anhydride, in the presence of a solvent, onto an ethylene-propylene copolymer backbone. The acylated ethylene-propylene copolymer had a number average molecular weight of approximately 40,000 as determined by gel permeation chromatography.
  • the acylated ethylene-propylene copolymer was reacted with N-phenyl-1,4-phenylenediamine (NPPDA), in the presence of a surfactant, at 160° C. for approximately six hours.
  • NPPDA N-phenyl-1,4-phenylenediamine
  • the NPPDA was added in an amount sufficient to theoretically react with all of the grafted carboxylic groups.
  • a cooled EGR engine was lubricated with an oil containing an olefin copolymer dispersant VII prepared as follows:
  • the highly grafted, multi-functional viscosity modifier of Example II was prepared in the same manner as that of Example I.
  • acylated ethylene-propylene copolymer was reacted with N-phenyl-1,4-phenylenediamine (NPPDA), in the presence of a surfactant, at 160° C. for approximately six hours.
  • NPPDA N-phenyl-1,4-phenylenediamine
  • the NPPDA was added in an amount sufficient to theoretically react with all of the grafted carboxylic groups.
  • the olefin copolymer dispersant VII can be present in the lubricating oil in the cooled EGR engine in an amount of from 2 weight percent to about 18 weight percent. Active material range from 0.55 to 10.0% m.

Abstract

The use in a cooled exhaust gas recirculation (EGR) engine of an olefin copolymer dispersant viscosity index improver to reduce or eliminate oil thickening and sludge formation is provided. Also provided are lubricated cooled EGR engines with ability to pass rigorous oil viscosity and emission standards.

Description

    FIELD
  • The present invention in an embodiment relates to a cooled exhaust gas recirculation (also called recycle) engine lubricated with a lubricating oil comprising a dispersant viscosity index improver in an amount and of a type sufficient to thereby achieve acceptable reduction in oil thickening due to increased soot accumulation. [0001]
  • BACKGROUND
  • With the arrival of new exhaust gas recirculation or recycle (hereinafter “EGR”) cooled engines including cooled EGR engines, a problem has developed in the ability of the conventional lubricating oils to handle the resulting increased soot loading. These new engines also have more stringent NOx emission standards. It has been noted in field testing of certain Mack and Detroit Diesel trucks that the engine oils tested in the cooled EGR prototype engines exhibit undesirably excessive oil thickening because of the way soot is being generated. Increasing the treat rate of the standard dispersants in the lubricating oils has not solved the problem. [0002]
  • The art contains many disclosures on the use of polymer additives in lubricating oil compositions. Ethylene-propylene and/or other olefin copolymers and ethylene-alpha olefin non-conjugated diene terpolymers, which have been further derivatized to provide functional properties in lubricating oil compositions, illustrate this type of oil additive. [0003]
  • Therefore, what is needed is an olefin copolymer dispersant viscosity index improver for use in lubricating oils in a cooled EGR engine to thereby achieve acceptable reduction in oil thickening due to soot accumulation. Also desired is a cooled EGR engine lubricated with a lubricating oil containing such a dispersant viscosity index improver (“VII”). [0004]
  • SUMMARY OF EMBODIMENTS
  • It has been surprisingly discovered that the use in cooled EGR engines of lubricating oils containing certain olefin copolymer (“OCP”) dispersant VIIs can reduce, prevent or minimise the undesirable oil thickening that can occur in the cooled EGR engines. By “copolymer” herein is meant and included copolymers or terpolymers of ethylene and C[0005] 3 to C23 alpha-olefin, and optionally a non-conjugated diene or triene, on which has been grafted ethylenically unsaturated carboxylic reactants.
  • The cooled EGR engines within the scope of the present invention include automotive engines, heavy and light duty diesel and gasoline truck engines, gasoline combustion engines, diesel engines, hybrid Internal Combustion/electric engines. These can include EGR engines cooled by the circulation or heat exchange of water, water/hydrocarbon blends or mixtures, water/glycol mixtures, and/or air or gas. [0006]
  • Many patents have taught the manufacture and use of dispersant VII materials in engine oil formulations. These patents include, for example, U.S. Pat. Nos. 6,107,257; 5,182,041; 5,188,745; 5,238,588, 4,8636,623; 5,075,383; 6,107,258; 5,556,923; and European patents EP 0922752; EP 0909805; EP 0491456; EP 0510892; EP 0338672EP 0396297; EP0549196; and EP 0417904, all of which are incorporated herein by reference in their entirety for their teaching. [0007]
  • Therefore, in an embodiment is provided herein a lubricated engine comprising an exhaust gas recirculation system, whereby exhaust gases comprising soot generated in the combustion in the engine of fuel contact a lubricating oil used to lubricate said engine, wherein said lubricating oil comprises: a base oil, and at least one dispersant viscosity index improver in an amount and type sufficient to reduce the amount of oil thickening of the lubricating oil. In this manner, a lubricating oil produces a passing result in the Mack T-11 EGR equipped diesel engine test by maintaining a kinematic viscosity of about 20.0 or less, even at soot levels of up to about 8.9% by mass. [0008]
  • It is to be understood that both the foregoing general description and the following detailed description are exemplary and explanatory only and are intended to provide further explanation of the present invention, as claimed.[0009]
  • DETAILED DESCRIPTION OF THE EMBODIMENTS
  • In an embodiment is presented herein an EGR engine lubricated with a lubricating oil that contains, inter alia, a viscosity-controlling amount of a highly grafted, multi-functional olefin copolymer that comprises the reaction product of (1) an acylated olefin copolymer, wherein the acylated copolymer comprises copolymers or terpolymers of ethylene and C[0010] 3 to C23 alpha-olefin and optionally a non-conjugated diene or triene on which has been grafted ethylenically unsaturated carboxylic reactants to a level of 0.15 to 1.0 carboxylic groups per 1000 number average molecular weight units (Mn), and (2) a polyamine compound selected from the group consisting of:
  • (a) an N-arylphenylenediamine represented by the formula: [0011]
    Figure US20040259742A1-20041223-C00001
  • in which R[0012]   1 is hydrogen, —NH-aryl, —NH-arylalkyl, —NH-alkyl, or a branched or straight chain radical having from 4 to 24 carbon atoms that can be alkyl, alkenyl, alkoxyl, aralkyl, alkaryl, hydroxyalkyl or aminoalkyl; R2 is —NH2, CH2—(CH2)n—NH2, CH2-aryl-NH2, in which n has a value from 1 to 10; and R3 is hydrogen, alkyl, alkenyl, alkoxyl, aralkyl, alkaryl having from 4 to 24 carbon atoms;
  • (b) an aminothiazole from the group consisting of aminothiazole, aminobenzothiazole, aminobenzo-thiadiazole and aminoalkylthiazole; [0013]
  • (c) an aminocarbazole represented by the formula: [0014]
    Figure US20040259742A1-20041223-C00002
  • in which R and R[0015]   1 represent hydrogen or an alkyl, alkenyl or alkoxyl radical having from 1 to 14 carbon atoms; (d) an aminoindole represented by the formula:
    Figure US20040259742A1-20041223-C00003
  • in which R represents hydrogen or an alkyl radical having from 1 to 14 carbon atoms; [0016]  
  • (e) an aminopyrrole represented by the formula: [0017]
    Figure US20040259742A1-20041223-C00004
  • in which R is a divalent alkylene radical having 2-6 carbon atoms and R[0018]   1 is hydrogen or an alkyl radical having from 1 to 14 carbon atoms;
  • (f) an amino-indazolinone represented by the formula: [0019]
    Figure US20040259742A1-20041223-C00005
  • in which R is hydrogen or an alkyl radical having from 1 to 14 carbon atoms; [0020]  
  • (g) an aminomercaptotriazole represented by the formula: [0021]
    Figure US20040259742A1-20041223-C00006
  • in which R can be absent or is a C[0022]   1-C10 linear or branched hydrocarbon selected from the group consisting of alkyl, alkenyl, arylalkyl, or aryl;
  • (h) and an aminoperimidine represented by the formula, [0023]
    Figure US20040259742A1-20041223-C00007
  • in which R represents hydrogen or an alkyl or alkoxy radical having from 1 to 14 carbon atoms; [0024]  
  • (i) aminoalkyl imidazoles, such as 1-(2-aminoethyl) imidazole, 1-(3-aminopropyl) imidazole; and [0025]
  • (j) aminoalkyl morpholines, such as 4-(3-aminopropyl) morpholine. [0026]
  • The novel lubricated cooled EGR engines described herein contain lubricating compositions that comprise an oil of lubricating viscosity and a dispersant VII effective amount of the highly grafted, multi-functional olefin copolymer dispersant as described above. [0027]
  • In an embodiment, polymers for use herein may include copolymers of ethylene and one or more C[0028] 3 to C23 alpha-olefins. Copolymers of ethylene and propylene are very effective. Other alpha-olefins suitable in place of propylene to form the copolymer or to be used in combination with ethylene and propylene to form a terpolymer include 1-butene, 1-pentene, 1-hexene, 1-octene and styrene; α,ω-diolefins such as 1,5-hexadiene, 1,6-heptadiene, 1,7-octadiene; branched chain alpha-olefins such as 4-methylbutene-1,5-methylpentene-1 and 6-methylheptene-1; and mixtures thereof.
  • More complex polymer substrates, often designated as interpolymers, may be prepared using a third component in preparing the dispersant used in the oil to lubricate the cooled EGR engines. The third component generally used to prepare an interpolymer substrate is a polyene monomer selected from non-conjugated dienes and trienes. The non-conjugated diene component is one having from 5 to 14 carbon atoms in the chain. In one embodiment, the diene monomer is characterized by the presence of a vinyl group in its structure and can include cyclic and bicyclo compounds. Representative dienes include 1,4-hexadiene, 1,4-cyclohexadiene, dicyclopentadiene, 5-ethylidene-2-norbornene, 5-methylene-2-norborene, 1,5-heptadiene, and 1,6-octadiene. A mixture of more than one diene can be used in the preparation of the interpolymer. In another embodiment, a non-conjugated diene for preparing a terpolymer or interpolymer substrate is 1,4-hexadiene. [0029]
  • The triene component will have at least two non-conjugated double bonds, and up to about 30 carbon atoms in the chain. Typical trienes useful in preparing the interpolymer of the invention are 1-isopropylidene-3α,4,7,7α-tetrahydroindene, 1-isopropylidenedicyclopentadiene, dihydro-isodicyclopentadiene, and 2-(2-methylene-4-methyl-3-pentenyl)[2.2.1] bicyclo-5-heptene. [0030]
  • Ethylene-propylene or higher alpha-olefin copolymers may consist of from about 15 to 80 mole percent ethylene and from about 85 to 20 mole percent C[0031] 3 to C23 alpha-olefin with the mole ratios being from about 35 to 75 mole percent ethylene and from about 65 to 25 mole percent of a C3 to C23 alpha-olefin. In another embodiment, the proportions are from 50 to 70 mole percent ethylene and 50 to 30 mole percent C3 to C23 alpha-olefin. In yet another example, the proportions are from 55 to 65 mole percent ethylene and 45 to 35 mole percent C3 to C23 alpha-olefin.
  • Terpolymer variations of the foregoing polymers may contains from about 0.1 to 10 mole percent of a non-conjugated diene or triene. [0032]
  • Also useful herein as the polymer for the dispersant viscosity index improver used in an oil to lubricate a cooled EGR engine is a polymer selected from the group consisting of polymethacrylates, ethylene/propylene copolymers, polyisoprene or saturated polyisoprene, and polyisoprene/saturated polyisoprene copolymers. [0033]
  • The polymer substrate, that is the ethylene copolymer or terpolymer, can be an oil-soluble, linear or branched polymer having a number average molecular weight from about 20,000 to 150,000 as determined by gel permeation chromatography and universal calibration standardization, with a number average molecular weight range of 30,000 to 110,000. [0034]
  • The terms polymer and copolymer are used generically to encompass ethylene copolymers, terpolymers or interpolymers. These materials may contain minor amounts of other olefinic monomers so long as the basic characteristics of the ethylene copolymers are not materially changed. [0035]
  • The polymerization reaction used to form the ethylene-olefin copolymer substrate is generally carried out in the presence of a conventional Ziegler-Natta or metallocene catalyst system. The polymerization medium is not specific and can include solution, slurry, or gas phase processes, as known to those skilled in the art. When solution polymerization is employed, the solvent may be any suitable inert hydrocarbon solvent that is liquid under reaction conditions for polymerization of alpha-olefins; examples of satisfactory hydrocarbon solvents include straight chain paraffins having from 5 to 8 carbon atoms, with hexane being preferred. Aromatic hydrocarbons, preferably aromatic hydrocarbon having a single benzene nucleus, such as benzene, toluene and the like; and saturated cyclic hydrocarbons having boiling point ranges approximating those of the straight chain paraffinic hydrocarbons and aromatic hydrocarbons described above, are particularly suitable. The solvent selected may be a mixture of one or more of the foregoing hydrocarbons. When slurry polymerization is employed, the liquid phase for polymerization is preferably liquid propylene. It is desirable that the polymerization medium be free of substances that will interfere with the catalyst components. [0036]
  • An ethylenically unsaturated carboxylic acid material is next grafted onto the prescribed polymer backbone to form an acylated ethylene copolymer. These carboxylic reactants which are suitable for grafting onto the ethylene copolymer contain at least one ethylenic bond and at least one, preferably two, carboxylic acid or its anhydride groups or a polar group which is convertible into said carboxyl groups by oxidation or hydrolysis. The carboxylic reactants are in one embodiment selected from the group consisting of acrylic, methacrylic, cinnamic, crotonic, maleic, fumaric and itaconic reactants. Alternatively, the carboxylic reactants are selected from the group consisting of maleic acid, fumaric acid, maleic anhydride, or a mixture of two or more of these. Maleic anhydride or a derivative thereof has advantages of commercial availability and ease of reaction. In the case of unsaturated ethylene copolymers or terpolymers, itaconic acid or its anhydride are useful due to its reduced tendency to form a cross-linked structure during the free-radical grafting process. [0037]
  • The ethylenically unsaturated carboxylic acid materials typically can provide one or two carboxylic groups per mole of reactant to the grafted polymer. That is, methyl methacrylate can provide one carboxylic group per molecule to the grafted polymer while maleic anhydride can provide two carboxylic groups per molecule to the grafted polymer. [0038]
  • In one embodiment, the carboxylic reactant is grafted onto the prescribed polymer backbone in an amount to provide 0.15 to 1.0 carboxylic groups per 1000 number average molecular weight units of the polymer backbone, preferably 0.3 to 0.5 carboxylic groups per 1000 number average molecular weight. For example, a copolymer substrate with Mn of 20,000 is grafted with 6 to 10 carboxylic groups per polymer chain or 3 to 5 moles of maleic anhydride per mole of polymer. A copolymer with Mn of 100,000 is grafted with 30 to 50 carboxylic groups per polymer chain or 15 to 25 moles of maleic anhydride per polymer chain. The minimum level of functionality is the level needed to achieve the minimum satisfactory dispersancy performance in the lubricated cooled EGR engines. [0039]
  • The grafting reaction to form the acylated olefin copolymers is generally carried out with the aid of a free-radical initiator either in solution or in bulk, as in an extruder or intensive mixing device. When the polymerization is carried out in hexane solution, it is economically convenient but not required herein to carry out the grafting reaction in hexane as described in U.S. Pat. Nos. 4,340,689, 4,670,515 and 4,948,842, incorporated herein by reference. The resulting polymer intermediate is characterized by having carboxylic acid acylating functionality randomly within its structure. [0040]
  • The highly grafted, multi-functional olefin copolymer dispersant VIIs used to lubricate the cooled EGR engines of the present invention can be incorporated into a lubricating oil in any convenient way. Thus, the highly grafted, multi-functional olefin copolymers can be added directly to the lubricating oil by dispersing or dissolving the same in the lubricating oil at the desired level of concentration. Such blending into the lubricating oil can occur at room temperature or elevated temperatures. Alternatively, the highly grafted, multi-functional olefin copolymers can be blended with a suitable oil-soluble solvent/diluent (such as benzene, xylene, toluene, lubricating base oils and petroleum distillates) to form a concentrate, and then blending the concentrate with a lubricating oil to obtain the final formulation. Such additive concentrates will typically contain (on an active ingredient (A.I.) basis) from about 3 to about 45 wt. %, and often from about 10 to about 35 wt. %, highly grafted, multi-functional olefin copolymer additive, and more often from about 40 to 60 wt %, base oil based on the concentrate weight. [0041]
  • The highly grafted, multi-functional olefin copolymer products useful in lubricating oils to lubricate cooled EGR engines of the present invention find their primary utility in lubricating oil compositions which employ a base oil in which the additives are dissolved or dispersed. Such base oils may be natural, synthetic or mixtures thereof. Base oils suitable for use in preparing the lubricating oil compositions of the present invention include those conventionally employed as crankcase lubricating oils for spark-ignited and compression-ignited internal combustion engines, such as automobile and truck engines, marine and railroad diesel engines, and the like. [0042]
  • In the preparation of lubricating oil formulations it is common practice to introduce the additives in the form of 10 to 80 wt. % active ingredient concentrates in hydrocarbon oil, e.g. mineral lubricating oil, or other suitable solvent. Usually these concentrates may be diluted with 3 to 100, e.g., 5 to 40, parts by weight of lubricating oil per part by weight of the additive package in forming finished lubricants, e.g. crankcase motor oils. The purpose of concentrates, of course, is to make the handling of the various materials less difficult and awkward as well as to facilitate solution or dispersion in the final blend. Thus, the highly grafted, multi-functional olefin copolymer dispersant VII would usually be employed in the form of a 10 to 50 wt. % concentrate, for example, in a lubricating oil fraction. [0043]
  • The amount of dispersant viscosity index improver in the lubricating oil in the cooled EGR engine can be from about 20 wt. % to about 18 wt. %. [0044]
  • The highly grafted, multi-functional olefin copolymer dispersant VIIs used in an oil to lubricate the cooled EGR engines of the present invention will generally be used in admixture with a lube oil basestock, comprising an oil of lubricating viscosity, including natural lubricating oils, synthetic lubricating oils and mixtures thereof. Natural oils include animal oils and vegetable oils (e.g., castor, lard oil), liquid petroleum oils and hydrorefined, solvent-treated or acid-treated mineral lubricating oils of the paraffinic, naphthenic and mixed paraffinic-naphthenic types. Oils of lubricating viscosity derived from coal or shale are also useful base oils. The synthetic lubricating oils used in this invention include one of any number of commonly used synthetic hydrocarbon oils, which include, but are not limited to, poly-alpha-olefins, alkylated aromatics, alkylene oxide polymers, interpolymers, copolymers and derivatives thereof where the terminal hydroxyl groups have been modified by esterification, etherification etc, esters of dicarboxylic acids and silicon-based oils. [0045]
  • The present invention is further directed to a method of improving fuel economy and fuel economy durability of a vehicle having a cooled EGR engine, wherein said method comprises adding to and operating in the crankcase of the vehicle the lubricating oil composition containing the olefin copolymer dispersant VII described herein. [0046]
  • Also provided is a method of simultaneously passing the M-11 EGR and T-10 tests (ASTM D4485 classification for C1-4 oils D02.B0 C1-4 Ballot) and the Mack T-11 test which are cooled EGR engines. Said method comprises adding to and operating in the crankcase of the vehicle the lubricating oil composition containing the olefin copolymer dispersant VII described above. [0047]
  • The highly grafted, multi-functional olefin copolymers used in the oils to lubricate the cooled EGR engines of the present invention may be post-treated so as to impart additional properties necessary or desired for a specific lubricant application. Post-treatment techniques are well known in the art and include boronation, phosphorylation, and maleination. [0048]
  • In another embodiment herein, the EGR engine is lubricated with a lubricating oil further comprising an additive selected from the group consisting of zinc dialkyl dithiophosphates, friction modifiers, antioxidants, defoamants, surfactants, corrosion inhibitors, extreme pressure agents, detergents, and pour point depressants. [0049]
  • Thus, in another embodiment an EGR engine is lubricated with an oil comprising a highly grafted, multi-functional olefin copolymer viscosity modifier, also called a viscosity index improver, comprising the reaction product of an acylated olefin copolymer and a polyamine, wherein the acylated olefin copolymer comprises an olefin copolymer having grafted thereon from 0.15 to 1.0 carboxylic groups per 1000 number average molecular weight units of olefin copolymer and wherein the olefin copolymer has a number average molecular weight of between 10,000 and 150,000. [0050]
  • In another important embodiment, the lubricated cooled EGR engine of the present invention can surprisingly pass the M-11 EGR crosshead wear and dispersancy test, the T-10 test, and the Mack T-11 test (EGR equipped diesel engines). Conventional lubricating oils containing certain known dispersants including Ethyl's HiTEC® 5772 dispersant and non-dispersant VIIs have not been able to pass all of these tests in cooled EGR engines. The dispersant VIIs disclosed herein as useful in lubricating oils in a cooled EGR engine can be used in conjunction with other dispersants. Table I shows HiTEC® 5777 alone, HiTEC® 5777 plus HiTEC® 5772, and HiTEC® 5772 alone, when used to lubricate a Cummins cooled EGR engine after 250 hours. [0051]
    TABLE I
    0.1 wt. % H5777 % Active wt. % H5772 % Active Oil Viscosity
    1 5.0 1.41 0 0 25.04
    2 4.5 1.27 4.0 0.76 27.03
    3 3.1 0.87 3.7 0.70 33.28
    4 0 0 5.35 1.01 66.73
  • The viscosities of the used 15W-40 oils were measured at 100° C. Table I clearly shows that HiTEC® 5777 dispersant controls the viscosity increase while the use of the dispersant viscosity modifier HiTEC® 5772 does not (higher viscosity of 66.73). [0052]
  • In yet another embodiment, the lubricated engine achieves a viscosity increase of less than 10 cSt at 100° C. at a soot level of up to 6.0% m in the Mack T-11 test. [0053]
  • Another embodiment herein provides a lubricated EGR engine wherein the lubricating oil passes the Mack T-11 test at a viscosity increase of less than 8 cSt at 100° C. at a soot level of up to 6.09% m in the Mack T-11 test. [0054]
  • Further provided herein is a lubricated EGR engine wherein the lubricating oil has a viscosity increase of less than 10 cSt at 100° C. and up to 6.0% m soot in the Mack T-11 test. [0055]
  • It is known that hard soot particles cause abrasive wear on valve trains, rings, and liners. Thick lubricating oil films containing the olefin copolymer dispersant VIIs defined herein can significantly and surprisingly reduce this abrasive wear. Oils with good M-11 test performances formed thick boundary films providing percent film resistance values of 80 to about 95 after 2000 seconds in the High Frequency Reciprocating Rig (HFRR) test. [0056]
  • EGR tests results have shown soot thickening from the present embodiments superior to that seen in the T-8E test. Lubricating oils containing the olefin copolymer dispersant VII described herein have been successfully tested in cooled EGR engines from Cat, Mack, Cummins, Volvo, and Detroit Diesel. Thus another embodiment herein provides a use in an Internal Combustion engine, comprising a cooled exhaust gas recirculation system, of a lubricating oil comprising a base oil, and at least one olefin copolymer dispersant viscosity index improver in an amount sufficient to reduce the amount of soot-induced oil thickening of the lubricating oil. [0057]
  • Lubricating oil films containing the olefin copolymer dispersant VIIs defined herein provide excellent performance in the Mack T-11 test, reduce both high and low temperature thickening, give superior sludge performance, and give superior wear protection from soot. [0058]
  • In another embodiment, the present invention provides a method to extend the service time between oil drains in a vehicle equipped with an exhaust gas recirculation engine up to about 60,000 miles by the addition to a lubricating oil in the engine of an olefin copolymer dispersant VII as described herein. [0059]
  • The oils containing the olefin copolymer dispersant VII as taught herein also have the following advantages when used in cooled EGR engines: excellent for building film strength and reducing wear; low treat rate of, for example, 8.5% wt. (˜9.5% vol.) for 15W-40; strong sludge suppression performance; provides superior performance in EGR engines; good shear stability, permanent and HTHS; excellent dispersancy for soot handling and improved wear protection; allows for lower additive treat rate; and excellent used-oil low temperature viscosity properties, relative to the low temperature viscosity properties of oils not containing the olefin copolymer dispersant VII as taught herein. [0060]
  • FIG. 1 illustrates that by the use in the cooled EGR engine of a lubricating oil containing the olefin dispersant copolymer VII described herein, the oil exhibited a kinematic viscosity at 100° C. that does not increase rapidly in high soot loading, whereas the kinematic viscosity of the industry standard reference oil increases rapidly beyond the 4% soot loading level. FIG. 1 shows viscosities for lubricating oils using Group I and Group II base oils. [0061]
  • A particularly useful olefin copolymer dispersant VII for addition to a lubricating oil in a cooled EGR engine is HiTEC® 5777 Dispersant available from Ethyl Corporation, Richmond, Va. [0062]
  • The following examples further illustrate aspects of the present invention but do not limit the present invention. [0063]
  • FIG. 2 illustrates the effect on viscosity measured at 25° C. of increasing weight percent of soot loading in a lubricating oil containing an olefin copolymer dispersant viscosity index improver, Ethyl's HiTEC® 5777 dispersant additive. The Figure shows a curve for Group I and for Group II base oils in this low temperature Mack T-8E test. In this illustration, the additive HiTEC® 5777 allowed the maintenance of low temperature viscosity below the 15W limit to a loading of over 6% soot in Group I base oil and to over 9% soot in Group II base oil. [0064]
  • FIG. 3 illustrates the performance in a cooled EGR engine of a lubricating oil labeled C1-4 D1 containing HiTEC® 5777 versus a standard reference oil CH-4 in the common extended T-8E test for viscosity change caused by soot loading. It is clear that the use in a cooled EGR engine of the olefin copolymer dispersant VII described herein significantly restricted the viscosity increase at higher soot levels. [0065]
  • EXAMPLES Example I
  • In an example of an embodiment herein, a cooled EGR engine was lubricated with an oil containing an olefin copolymer dispersant VII prepared as follows: An acylated ethylene-propylene copolymer was prepared by free radically grafting maleic anhydride, in the presence of a solvent, onto an ethylene-propylene copolymer backbone. The acylated ethylene-propylene copolymer had a number average molecular weight of approximately 40,000 as determined by gel permeation chromatography. The reaction conditions and molar proportions of maleic anhydride and ethylene-propylene copolymer were such that 7.2 molecules of maleic anhydride were grafted onto the olefin copolymer backbone. This is equivalent to 0.36 carboxylic groups per 1000 Mn of polymer backbone (i.e., 2×7.2=14.4 carboxylic groups/40,000 Mn=0.36 carboxylic groups/1000 Mn) to form the acylated ethylene-propylene copolymer. The acylated ethylene-propylene copolymer was reacted with N-phenyl-1,4-phenylenediamine (NPPDA), in the presence of a surfactant, at 160° C. for approximately six hours. The NPPDA was added in an amount sufficient to theoretically react with all of the grafted carboxylic groups. [0066]
  • Example II
  • In another example, a cooled EGR engine was lubricated with an oil containing an olefin copolymer dispersant VII prepared as follows: The highly grafted, multi-functional viscosity modifier of Example II was prepared in the same manner as that of Example I. However, a sufficient amount of maleic anhydride was added such that 14.2 molecules of maleic anhydride were grafted onto the olefin copolymer backbone. This is equivalent to 0.71 carboxylic groups per 1000 Mn of polymer backbone (i.e., 2×14.2=28.4 carboxylic groups/40,000 Mn=0.71 carboxylic groups/1000 Mn) to form the acylated ethylene-propylene copolymer. The acylated ethylene-propylene copolymer was reacted with N-phenyl-1,4-phenylenediamine (NPPDA), in the presence of a surfactant, at 160° C. for approximately six hours. The NPPDA was added in an amount sufficient to theoretically react with all of the grafted carboxylic groups. [0067]
  • It has been noted that the use of some dispersant polymers and copolymers in lubricating oils used in cooled EGR engines did not prevent severe oil thickening, unlike the olefin copolymer dispersant VII described herein when used in an oil to lubricate a cooled EGR engine. [0068]
  • In certain embodiments herein, the olefin copolymer dispersant VII can be present in the lubricating oil in the cooled EGR engine in an amount of from 2 weight percent to about 18 weight percent. Active material range from 0.55 to 10.0% m. [0069]
  • Other embodiments of the present invention will be apparent to those skilled in the art from consideration of the specification and practice of the invention disclosed herein. It is intended that the specification and examples be considered as exemplary only, with a true scope and spirit of the invention being indicated by the following claims. This invention is susceptible to considerable variation in its practice. Accordingly, this invention is not limited to the specific exemplifications set forth hereinabove. Rather, this invention is within the spirit and scope of the appended claims, including the equivalents thereof available as a matter of law. [0070]
  • The patentee does not intend to dedicate any disclosed embodiments to the public, and to the extent any disclosed modifications or alterations may not literally fall within the scope of the claims, they are considered to be part of the invention under the doctrine of equivalents. [0071]

Claims (22)

What is claimed is:
1. A lubricated engine comprising an exhaust gas recirculation system, whereby exhaust gases comprising soot generated in the combustion in the engine of fuel contact a lubricating oil used to lubricate said engine, wherein said lubricating oil comprises: a base oil, and at least one dispersant viscosity index improver in an amount sufficient to reduce the amount of oil thickening of the lubricating oil.
2. The engine of claim 1, wherein the lubricating oil further comprises an additive selected from the group consisting of zinc dialkyl dithiophosphates, friction modifiers, corrosion inhibitors, extreme pressure agents, antioxidants, defoamants, surfactants, detergents, and pour point depressants.
3. The engine of claim 1, wherein the base oil of the lubricating oil is selected from the group consisting of natural lubricating oils, synthetic lubricating oils, and mixtures thereof.
4. The engine of claim 1, wherein the base oil of the lubricating oil is selected from the group consisting of animal oils, vegetable oils, castor oil, lard oil, liquid petroleum oils, hydrorefined, solvent-treated or acid-treated mineral lubricating oils of the paraffinic, naphthenic and mixed paraffinic-naphthenic types, oils of lubricating viscosity derived from coal or shale, poly-alpha-olefins, alkylated aromatics, alkylene oxide polymers, interpolymers, copolymers and derivatives thereof where the terminal hydroxyl groups have been modified by esterification or etherification, esters of dicarboxylic acids, and silicon oils.
5. The engine of claim 1, wherein the at least one dispersant viscosity index improver in the lubricating oil comprises an olefin copolymer dispersant viscosity index improver.
6. The engine of claim 1, wherein the at least one dispersant viscosity index improver in the lubricating oil comprises is selected from the group consisting of polymethacrylates, ethylene/propylene copolymers, polyisoprene or saturated polyisoprene, and polyisoprene/saturated polyisoprene copolymers.
7. The engine of claim 1, wherein the engine is selected from the group consisting of automotive engines, heavy and light duty truck engines, gasoline combustion engines, diesel engines, hybrid Internal Combustion/electric engines.
8. The engine of claim 1, wherein the at least one dispersant viscosity index improver in the lubricating oil is a highly grafted, multi-functional olefin copolymer that comprises the reaction product of (1) an acylated olefin copolymer, wherein the acylated copolymer comprises copolymers or terpolymers of ethylene and C3 to C23 alpha-olefin and optionally a non-conjugated diene or triene on which has been grafted ethylenically unsaturated carboxylic reactants to a level of 0.3 to 0.75 carboxylic groups per 1000 number average molecular weight units (Mn), and (2) a polyamine compound.
9. The engine of claim 8, wherein the polyamine compound is selected from the group consisting of
(a) an N-arylphenylenediamine represented by the formula:
Figure US20040259742A1-20041223-C00008
 in which R1 is hydrogen, —NH-aryl, —NH-arylalkyl, —NH-alkyl, or a branched or straight chain radical having from 4 to 24 carbon atoms that can be alkyl, alkenyl, alkoxyl, aralkyl, alkaryl, hydroxyalkyl or aminoalkyl; R2 is —NH2, CH2—(CH2)n—NH2, CH2-aryl-NH2, in which n has a value from 1 to 10; and R3 is hydrogen, alkyl, alkenyl, alkoxyl, aralkyl, alkaryl having from 4 to 24 carbon atoms;
(b) an aminothiazole from the group consisting of aminothiazole, aminobenzothiazole, aminobenzo-thiadiazole and aminoalkylthiazole;
(c) an aminocarbazole represented by the formula:
Figure US20040259742A1-20041223-C00009
 in which R and R1 represent hydrogen or an alkyl, alkenyl or alkoxyl radical having from 1 to 14 carbon atoms; (d) an aminoindole represented by the formula:
Figure US20040259742A1-20041223-C00010
 in which R represents hydrogen or an alkyl radical having from 1 to 14 carbon atoms;
(e) an aminopyrrole represented by the formula:
Figure US20040259742A1-20041223-C00011
 in which R is a divalent alkylene radical having 2-6 carbon atoms and R1 is hydrogen or an alkyl radical having from 1 to 14 carbon atoms;
(f) an amino-indazolinone represented by the formula:
Figure US20040259742A1-20041223-C00012
 in which R is hydrogen or an alkyl radical having from 1 to 14 carbon atoms;
(g) an aminomercaptotriazole represented by the formula:
Figure US20040259742A1-20041223-C00013
 in which R can be absent or is a C1-C10 linear or branched hydrocarbon selected from the group consisting of alkyl, alkenyl, arylalkyl, or aryl;
(h) and an aminoperimidine represented by the formula,
Figure US20040259742A1-20041223-C00014
 in which R represents hydrogen or an alkyl or alkoxy radical having from 1 to 14 carbon atoms;
(i) aminoalkyl imidazoles, such as 1-(2-aminoethyl) imidazole, 1-(3-aminopropyl) imidazole; and
(j) aminoalkyl morpholines, such as 4-(3-aminopropyl) morpholine.
10. The lubricated engine of claim 1, wherein the amount of the dispersant viscosity improver in the lubricating oil is from 2 weight percent to about 18 weight percent.
11. The engine of claim 1, wherein the engine is cooled by the circulation of a material selected from the group consisting of water, a water/hydrocarbon mix, water/glycol mix, air, and gas.
12. The engine of claim 1, wherein said lubricated engine achieves a viscosity increase of less than 10 cSt at 100° C. at a soot level of up to 6.0% m in the Mack T-11 test.
13. The lubricated engine of claim 1, wherein the lubricating oil passes the Mack T-11 test at a viscosity increase of less than 8 cSt at 100° C. at a soot level of up to 6.09% m in the Mack T-11 test.
14. The lubricated engine of claim 1, wherein the lubricating oil has a viscosity increase of less than 10 cSt at 100° C. and up to 6.0% m soot in the Mack T-11 test.
15. The use in an Internal Combustion engine comprising a cooled exhaust gas recirculation system of a lubricating oil comprising a base oil, and at least one olefin copolymer dispersant viscosity index improver in an amount sufficient to reduce the amount of soot-induced oil thickening of the lubricating oil.
16. A method of reducing the soot-induced thickening of a lubricating oil used to lubricate a cooled exhaust gas recirculating engine in which soot accumulates in the oil, said method comprising lubricating the engine with a lubricating oil comprising a base oil and a sufficient amount of an olefin copolymer dispersant viscosity index improver.
17. A method of improving fuel economy of a vehicle having a cooled exhaust gas recirculation engine, wherein said method comprises adding to and operating in the crankcase of said vehicle a lubricating oil composition containing a sufficient amount of the olefin copolymer dispersant viscosity index improver described herein.
18. A method of improving fuel economy durability of a vehicle having a cooled exhaust gas recirculation engine, wherein said method comprises adding to and operating in the crankcase of said vehicle a lubricating oil composition containing a sufficient amount of the olefin copolymer dispersant viscosity index improver described herein.
19. A method of simultaneously passing the M-11 EGR test, T-10 test (ASTM D4485 classification for API C1-4 oils), and the Mack T-11 in cooled EGR engine, said method comprising adding to and operating in the crankcase of the engine a lubricating oil composition containing a sufficient amount of the olefin copolymer dispersant viscosity index improver described herein.
20. A method to give superior oil sludge performance in a vehicle with a cooled EGR engine, said method comprising adding to and operating in the crankcase of the vehicle a lubricating oil composition containing a sufficient amount of the olefin copolymer dispersant viscosity index improver described herein, whereby the oil sludge performance is superior to the oil sludge performance in a cooled EGR engine of an oil without the olefin copolymer dispersant viscosity index improver described herein.
21. A method to give superior wear protection from soot in a vehicle equipped with a cooled EGR engine, said method comprising adding to and operating in the crankcase of the engine a lubricating oil composition containing a sufficient amount of the olefin copolymer dispersant viscosity index improver described herein, whereby the wear protection from soot is superior to the wear protection from soot in a cooled EGR engine lubricated with an oil without the olefin copolymer dispersant viscosity index improver described herein.
22. A method to extend the service time between oil drains in a vehicle equipped with an exhaust gas recirculation engine up to about 60,000 miles by the addition to a lubricating oil in the engine of a sufficient amount of an olefin copolymer dispersant viscosity index improver as described herein.
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