US20070149414A1 - Dispersant viscosity index improvers having high ethylene content and lubricating oil compositions containing the same - Google Patents

Dispersant viscosity index improvers having high ethylene content and lubricating oil compositions containing the same Download PDF

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US20070149414A1
US20070149414A1 US11/553,346 US55334606A US2007149414A1 US 20070149414 A1 US20070149414 A1 US 20070149414A1 US 55334606 A US55334606 A US 55334606A US 2007149414 A1 US2007149414 A1 US 2007149414A1
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alkenyl
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William Ruhe
Kirk A. Nass
Richard E. Cherpeck
Jean-Roch Schauder
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Chevron Oronite Co LLC
ExxonMobil Chemical Patents Inc
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M159/00Lubricating compositions characterised by the additive being of unknown or incompletely defined constitution
    • C10M159/005Macromolecular compounds, e.g. macromolecular compounds composed of alternatively specified monomers not covered by the same main group
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M149/00Lubricating compositions characterised by the additive being a macromolecular compound containing nitrogen
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2205/00Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions
    • C10M2205/02Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions containing acyclic monomers
    • C10M2205/022Ethene
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2205/00Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions
    • C10M2205/02Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions containing acyclic monomers
    • C10M2205/024Propene
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2205/00Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions
    • C10M2205/02Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions containing acyclic monomers
    • C10M2205/026Butene
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2205/00Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions
    • C10M2205/02Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions containing acyclic monomers
    • C10M2205/028Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions containing acyclic monomers containing aliphatic monomers having more than four carbon atoms
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2217/00Organic macromolecular compounds containing nitrogen as ingredients in lubricant compositions
    • C10M2217/06Macromolecular compounds obtained by functionalisation op polymers with a nitrogen containing compound
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2221/00Organic macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions
    • C10M2221/04Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2030/00Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/02Pour-point; Viscosity index
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2030/00Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/04Detergent property or dispersant property
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2030/00Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/04Detergent property or dispersant property
    • C10N2030/041Soot induced viscosity control
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2040/00Specified use or application for which the lubricating composition is intended
    • C10N2040/25Internal-combustion engines
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2060/00Chemical after-treatment of the constituents of the lubricating composition
    • C10N2060/09Treatment with nitrogen containing compounds

Definitions

  • the present invention relates to dispersant viscosity index improvers employable as additives in synthetic and petroleum oils, particularly lubricating oils. More particularly, the present invention relates to dispersant viscosity index improvers having high ethylene content which have been grafted: with an ethylenically unsaturated acylating agent and subsequently reacted with an amine compound.
  • V.I. viscosity index
  • Hydrocarbon polymers particularly ethylene-propylene copolymers
  • V.I. viscosity index
  • Various patents teach grafting ethylene copolymers with maleic anhydride, followed by reaction with an amine.
  • U.S. Pat. No. 4,160,739, issued Jul. 10, 1979, to Stambaugh et al. discloses graft copolymers wherein the backbone polymer is a polymeric hydrocarbon such as substantially linear ethylene/propylene copolymer and the grafted units are the residues of a monomer system comprising maleic acid or anhydride and one or more other monomers copolymerizable therewith, the monomer system being post-reacted with a polyamine compound comprising a primary or secondary amine.
  • the graft copolymers impart combined, detergent, viscosity index improvement and other useful properties to lubricating oils and hydrocarbon motor fuels.
  • U.S. Pat. No. 4,735,736, issued Apr. 5, 1988, to Chung discloses oil-soluble ethylene alpha-olefin hydrocarbon polymers, useful as V.I. improvers, such as ethylene copolymer, preferably ethylene-propylene copolymer, grafted with an unsaturated acid material, such as maleic anhydride, preferably by solid state grafting followed by reaction with a polyamine, preferably a tertiary-primary amine, and treatment and/or reaction with aliphatic monoamine.
  • the resulting material is used in oil compositions, such as lubricating oil, as a viscosity index improver having sludge dispersancy properties.
  • the monoamine treatment inhibits viscosity growth of the additive upon storage.
  • U.S. Pat. No. 4,863,623, issued Sep. 5, 1989, to Nalesnik discloses an additive composition comprising a graft and an amine-derivatized copolymer prepared from ethylene and at least one C 3 to C 10 alpha-monoolefin and, optionally, a polyene selected from non-conjugated dienes and trienes comprising from about 15 to 80 mole % of ethylene, from about 20 to 85 mole % of the C 3 to C 10 alpha-monoolefin and from about 0 to 15 mole % of the polyene having a average molecular weight ranging from about 5,000 to 500,000 which has been reacted with at least one olefinic carboxylic acid acylating agent to form one or more acylating reaction intermediates characterized by having a carboxylic acid acylating group within their structure and reacting the reaction intermediate with an amino-aromatic polyamine compound from the group consisting of an N-arylphenylenedi
  • U.S. Pat. No. 5,055,213, issued Oct. 8, 1991, to Germanaud et al. discloses additives resulting from the condensation of a primary or secondary amine and/or of an alkylene polyamine with a copolymer containing vicinal carboxylic groups.
  • Derivatives of phenothiazine, or naphthylamine and of diphenylamine are employed in most cases as alkylene polyamine. These compounds can be employed as multifunctional additives to lubricants.
  • U.S. Pat. No. 5,182,041, issued Jan. 26, 1993, to Benfarmeo et al. discloses an additive composition comprising a graft and an amine-derivatized polymer having an average molecular weight ranging from about 300 to 3,500 which has been reacted with at least one olefinic carboxylic acid acylating agent to form one or more acylating reaction intermediates characterized by having a carboxylic acid acylating group within their structure and reacting the reaction intermediate with an amino-aromatic polyamine compound from the group consisting of an N-arylphenylenediamine, an aminothiazole, an aminocarbazole, an amino-indazolinone, an aminomercaptotriazole and an aminopyrimidine to form the graft and amine-derivatized copolymer.
  • an amino-aromatic polyamine compound from the group consisting of an N-arylphenylenediamine, an aminothiazole, an aminocarbazole, an
  • U.S. Pat. No 5,366,647 issued Nov. 22, 1994, to Gutierrez et al. discloses a lubricating oil concentrate containing an oil soluble composition useful as a multifunctional viscosity index improver additive comprising an ethylene alpha-olefin polymer substituted with a mono- or dicarboxylic acid and at least one nucleophilic reagent selected from amines, alcohols, amino-alcohols, and reactive metal compounds.
  • the unsaturated mono- or dicarboxylic moiety is introduced by reaction with the end chain unsaturation of the ethylene alpha-olefin copolymer in a peroxide free reaction.
  • U.S. Pat. No. 5,427,702 issued Jun. 27, 1995 to Chung et al. discloses novel multifunctional viscosity modifiers comprising a mixture of derivatized ethylene-alpha olefin copolymers, A and B.
  • the A copolymer comprising from about 30 wt % to about 60 wt % monomer units derived from ethylene and the B copolymer comprising from about 60 wt % to about 80 wt % units derived from ethylene.
  • U.S. Pat. No. 5,429,757, issued Jul. 4, 1995, and U.S. Pat. No. 5,563,118, issued Oct. 8, 1996, to Mishra et al. disclose an additive composition comprising a graft and derivatized copolymer prepared from ethylene and at least one C 3 to C 10 alpha-monoolefin and, optionally, a polyene selected from non-conjugated dienes and trienes comprising from about 15 to 80 mole % of ethylene, from about 20 to 85 mole % of the C 3 to C 10 alpha-moonoolefin and from about 0 to 15 mole % of the polyone having an average molecular weight ranging from about 5,000 to 500,000, which has been reacted with at least one olefinic (carboxylic acid acylating agent to form one or more acylating reaction intermediates characterized by having a carboxylic acid acylating group within their structure and reacting the reaction intermediate
  • U.S. Pat. No. 6,107,257, issued Aug. 22, 2000, to Valcho et al. discloses a novel additive comprising a highly grafted, multifunctional olefin copolymer comprising a graft and amine-derivatized copolymer prepared from ethylene and at least one C 3 to C 23 alpha-monoolefin and, optionally, a polyene, wherein the copolymer of ethylene and at least one C 3 to C 23 alpha-monoolefin has grafted thereon from 0.3 to 0.75 carboxylic groups per 1,000 number average molecular weight units of olefin copolymer and wherein the olefin copolymer has a number average molecular weight of between 20,000 and 150,000.
  • U.S. Pat. No.6,107,258, issued Aug. 22, 2000, to Esche, Jr. et al. discloses novel functionalized olefin copolymers and their use as additives in fuel and lubricating oil compositions.
  • the functionalized olefin copolymers comprise an olefin copolymer on which has been grafted an ethylenically unsaturated carboxylic acid, or derivative thereof, to form an acylated olefin copolymer containing reactive carboxylic group.
  • the acylated olefin copolymer is reacted with a coupling compound, which contains more than one amine, thiol and/or hydroxy group capable of reacting with the carboxylic group of preferably more than one acylated olefin copolymer to form the novel additives. Additionally, the acylated olefin copolymers, either before or after reaction with the coupling compound, are reacted with a performance enhancing compound or compounds, i.e., compounds containing only one functional group capable of reacting with the carboxylic group of the acylated olefin copolymer, in order to obtain further benefits such as improved antioxidancy, antiwear and additional dispersancy properties.
  • WO97/32946 issued Sep. 12, 1997, to Hughes et al. discloses linear ethylene polymers with defined melt flow and critical shear rate for onset of melt fracture used for the production of oleaginous compositions. It also discloses the grafting of these linear backbones with maleic anhydride as well as their reaction with a carboxylic acid, an amine or an alcohol.
  • Canadian Patent No. 2,021,959, issued Nov. 28, 2000, to Migdal et al. discloses an additive composition comprising a graft and an amine-derivatized copolymer prepared from ethylene and at least one C 3 to C 10 alpha-monoolefin and, optionally, a polyene selected from non-conjugated dienes and trienes comprising from about 15 to 80 mole % of ethylene, from about 20 to 85 mole % of the C 3 to C 10 alpha-monoolefin and from about 0 to 15 mole % of the polyene having an average molecular weight ranging from about 1,000 to 40,000 which has been reacted with at least one olefinic carboxylic acid acylating agent to form one or more acylating reaction intermediates characterized by having at least about 1.5 wt % of a carboxylic acid acylating group within their structure and reacting the reaction intermediate with an amino-aromatic polyamine compound from the group consisting
  • U.S. Patent Application Publication Number 2006/0025316 published Feb. 2, 2006 discloses a method for lubricating a diesel engine equipped with exhaust gas recirculation, comprising supplying thereto a composition comprising the reaction product of: (a) a polymer comprising carboxylic acid group or a reactive equivalent thereof, said polymer having a number average molecular weight of greater than 5,000; and (b) an amine component comprising at least one aromatic amine containing at least one amino group capable of condensing with said carboxylic acid group to provide a pendant group and at least one additional group comprising at least one nitrogen, oxygen, or sulfur atom, wherein said aromatic; amine is selected from the group consisting of (i) a nitro-substituted aniline, (ii) amines comprising two aromatic moieties linked by a —C(O)NR— group, a —C(O)O— groups an —O— group, an —N ⁇ N— group or an —SO 2 — group where
  • the present invention relates to dispersant viscosity index improvers.
  • the present invention relates to a polymeric composition having an ethylene-alpha olefin copolymer backbone comprising at least 82 mole % ethylene and at most 18 mole % of an about C 3 to about C 28 alpha-monoolefin, wherein the alpha-monoolefin has a monomer distribution resulting from a R a R b product measured by 13 C-NMR below 0.8 and a level of regio-inversions less than 2 per 1000 carbon atoms, and an amide group having the formula (i) and/or an imide group having the formula (II):
  • the present invention relates to dispersant viscosity index improvers having high ethylene alpha-monoolefin copolymer content prepared by the process of grafting an ethylene-alpha-monoolefin copolymer backbone comprising at least 82 mole % ethylene and at most 18 mole % an about C 3 to about C 28 alpha-monoolefin.
  • the alpha-monoolefin has a monomer distribution resulting from a R a R b product measured by 13 C-NMR below 0.8 and a level of regio-inversions less than 2 per 1000 carbon atoms, with an ethylenically unsaturated acylating agent and subsequently reacting the resulting grafted copolymer with one, or more of the following amines:
  • the amine is an aromatic amine selected from the group consisting of
  • the present invention also relates to a lubricating oil composition
  • a lubricating oil composition comprising a major amount of base oil of lubricating viscosity and a minor amount of the polymeric composition of the present invention.
  • the present invention also relates to a lubricating oil composition
  • a lubricating oil composition comprising a major amount of base oil of lubricating viscosity and a minor amount of an oil-soluble product produced by the above process.
  • Another aspect of the present invention relates to a method of improving the soot and/or sludge dispersancy in an internal combustion engine by operating the internal combustion engine with the lubricating oil composition of the present invention containing the polymeric composition.
  • Another aspect of the present invention relates to a method of improving the soot and/or sludge dispersancy in an internal combustion engine by operating the internal combustion engine with the lubricating oil composition of the present invention containing the oil-soluble product produced by the process of the present invention.
  • the dispersant viscosity index improvers having high ethylene-alpha olefin copolymer content which have been grafted with an ethylenically unsaturated acylating agent and subsequently reacted with an amine compound provide multi-functional properties in lubricating oil compositions.
  • the dispersant viscosity index improvers of the present invention provide superior soot and/or sludge dispersancy as well as viscosity index improvement when used in lubricating oil compositions for internal combustion engines.
  • Such a lubricating oil composition is useful as a method of improving the soot and/or sludge dispersancy in an internal combustion engine, when the internal combustion engine is operated using the lubricating oil composition of the present invention.
  • grafts or “grafted” relate to covalent bonding of the grafting monomer to a polymer chain of the polymeric composition.
  • oil soluble refers to the ability of a material to dissolve in aliphatic and aromatic hydrocarbons such as lubricating oils or fuels in essentially all proportions.
  • R a R b product refers to the product of R a and R b where R a is being defined as the ratio of the kinetic constant for the reaction of ethylene with a second ethylene unit and the kinetic constant for the reaction of ethylene with propylene and R b as the ratio of the kinetic constant for the reaction of propylene with a second propylene unit and the kinetic constant for the reaction of propylene with ethylene.
  • R a R b product above 1 usually refers to polymers which are considered as blocky copolymers.
  • the polymers of the present invention have a low “R a R b product” and are more alternating copolymers.
  • level of regio-inversions refers to the presence of monomer sequences where propylene (or the higher alpha-olefin) is polymerized head to head or tail to tail which translates into sequences of even-numbered methylene units instead of head to tail which translates into sequences of odd-numbered methylene units.
  • the polymers of the present invention have almost no regio-inversions.
  • the “R a R b product” is measured by 13 C-NMR spectroscopy according to J. C. Randall in Macromolecules 15, 1584 (1982) or J. C. Randall, Encyclopedia of Polymer Sciences and Engineering , Vol. 9, p. 795, 2 nd Edition, John Wiley and Sons (1987) and the level of regio-inversions is measured according to S. Dimartino, M. Kelchtermans, Journal of Applied Polymer Sciences, 56, 1781 (1995).
  • the “R a R b product” is measured by 13 C-NMR spectroscopy according: to F. Cavagna, Macromolecules, 14, 215 (1981) and the level of regio-inversions is measured according to P. J. Adriaensens, Polymer 44 (12), 3483 (2003).
  • the polymer or copolymer substrate or backbone of the present invention may be prepared from ethylene and propylene or it may be prepared from ethylene and a higher olefin within the range of an about C 3 to about C 28 alpha-monoolefin, wherein the alpha-monoolefin has a monomer distribution resulting from a R a R b product measured by 13 C-NMR below 0.8 and a level of regio-inversions less than 2 per 1000 carbon atoms.
  • More complex polymer substrates may be prepared using a third component.
  • 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 about 5 to about 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 bi-cyclo 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 preferred 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 present invention are 1-isopropylidene-3a,4,7,7a-tetrahydroindene, 1-isopropylidenedicyclopentadiene, dehydro-isodicyclopentadiene, and 2-(2-methylene-4-methyl-3-pentenyl)[2.2.1]bicyclo-5-heptene.
  • the polymerization reaction to form the polymer or copolymer backbone is generally carried out in the presence of a catalyst in a solvent medium.
  • the polymerization solvent may be any suitable inert organic solvent that is liquid under reaction conditions for solution polymerization of monoolefins which is generally conducted in the presence of a Ziegler-type catalyst.
  • suitable hydrocarbon solvents include straight chain paraffins having from about 5 to about 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. It is desirable that the solvent be free of substances that will interfere with a Ziegler polymerization reaction.
  • hexane is first introduced into a reactor and the temperature in the reactor is raised moderately to about 30° C. Dry propylene is fed to the reactor until the pressure reaches about 40 to about 45 inches of mercury. The pressure is then increased to about 60 inches of mercury and dry ethylene and 5-ethylindene-2-norbornene are fed to the reactor. The monomer feeds are stopped and a mixture of aluminum sesquichloride and vanadium oxytrichloride is added to initiate the polymerization reaction. Completion of the polymerization reaction is evidenced by a drop in the pressure in the reactor.
  • Ethylene-propylene or higher alpha-monoolefin copolymers of the present invention may consist of at least 82 mole % ethylene and at most 18 mole % propylene or higher alpha-monoolefin with the preferred mole ratios being at least 84 mole % ethylene and at most 16 mole % of a about C 3 to about C 28 alpha-monoolefin.
  • the alpha monoolefin is from about C 3 to about C 20 and more preferably from about C 6 to about C 12 alpha-monoolefin. Most preferred alpha-monoolefin is octene.
  • Terpolymer variations of the foregoing polymers may contain from 0 to about 10 mole %, preferably about 0 to about 6 mole %, more preferably about 0 to about 3 mole %, of a non-conjugated diene or triene. In the most preferred embodiment, the foregoing polymers will not contain any non-conjugated diene or triene.
  • the polymer substrate that is the ethylene copolymer or terpolymer is an oil-soluble, substantially linear, rubbery material having a weight average molecular weight from about 5,000 to about 500,000 with a preferred weight average molecular weight range of about 25,000 to about 250,000 and a most preferred range from about 50,000 to about 150,000.
  • 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 their basic characteristics are not materially changed.
  • the ethylenically unsaturated acylating agent is next grafted onto the prescribed copolymer backbone.
  • the ethylenically unsaturated acylating agent can be represented by formula (A) and/or formula (B):
  • R 1 is hydrogen or —CO—W′
  • R 2 and R 3 are independently hydrogen or —CH 3
  • W and W′ are independently —OH, or alkoxyl having 1 to about 24 carbon atoms.
  • Maleic anhydride or a derivative thereof is the preferred ethylenically unsaturated acylating agent. It grafts onto the ethylene copolymer or terpolymer to give two carboxylic acid functionalities.
  • the ethylenically unsaturated acylating agent may be grafted onto the copolymer backbone in a number of ways. It may be grafted onto tile backbone by a thermal process known as the “ene” process or by grafting in solution or in melt form using a free-radical initiator.
  • the free-radical induced grafting of ethylenically unsaturated acylating agents is carried out in solvents, such as hexane, heptane, mineral oil or aromatic solvents, which do not react with the peroxide, it is carried out at an elevated temperature in the range of about 100° C. to about 250° C., preferably about 120° C. to about 190° C. and more preferably at about 150° C.
  • a solvent preferably a mineral oil solution containing, e.g. about 1 wt % to about 50 wt %, preferably about 5 wt % to about 30 wt %, based on the initial total oil solution, of the ethylene copolymer and preferably under an inert environment.
  • the free-radical initiators which may be used are peroxides (diacyl peroxides such as benzoyl peroxide, dialkyl peroxides such as 1,1-bis(tert-butylperoxy)cyclohexane.
  • peroxides diacyl peroxides such as benzoyl peroxide, dialkyl peroxides such as 1,1-bis(tert-butylperoxy)cyclohexane.
  • the initiator is used in an amount of between about 0.005% and about 1% by weight based on the weight of the reaction mixture solution.
  • the grafting is preferably carried out in an inert atmosphere, such as under nitrogen blanketing.
  • the resulting polymer intermediate is characterized by having acylating group, typified by a carboxylic acid or acid chloride, within its structure.
  • the ethylenically unsaturated acylating agent with the optional use of a radical initiator is grafted on molten rubber using rubber masticating or shearing equipment.
  • Single screw but preferably twin screw extruder reactors such as co-rotating intermeshing extruders or counter-rotating non-intermeshing extruders but also co-kneaders such as those sold by Buss are especially preferred.
  • the temperature of the molten material in this process may range from about 120° C. to about 400° C.
  • the preferred sequence of events used for the grafting reaction consists of melting the copolymeric composition, adding and dispersing the grafting monomer, introducing the peroxide and venting the unreacted monomer and by-products resulting from the peroxide decomposition.
  • Other sequences may include feeding the monomers and the peroxide pre-dissolved in a solvent.
  • copolymer intermediate is then reacted with an amine compound from the group consisting of:
  • the reaction between the copolymer intermediate having grafted thereon carboxylic acid or acid chloride acylating group and the prescribed amine compound is conducted by heating a solution of the copolymer backbone under inert conditions and then adding the amine compound to the heated solution generally with mixing to effect the reaction. It is convenient to employ an oil solution of the copolymer backbone heated to about 140° C. to about 175° C. while maintaining the solution under a nitrogen blanket. The amine compound is added to this solution and the reaction is effected under the noted conditions. The reaction can also be carried out without solvent in a reactive extruder.
  • the amine compound may, in general, contain one or more reactive (condensable) amino groups.
  • a single reactive amino group is sometimes preferred.
  • Multiple amino groups, as in the case of the above described N,N-dialkylphenylenediamine, can be useful as well, especially if they are reacted under relatively mild conditions so as to avoid excessive crosslinking or gellation of the polymer.
  • amine compounds can be used alone or in combination with each other. They can also be used in combination with additional, aromatic or non-aromatic, e.g., aliphatic, amines, which, in one embodiment, comprise about 1 to about 8 carbon atoms. Other aromatic amines can include such amines as aminodiphenylamine. These additional amines can be included for a variety of reasons. Sometimes it may be desirable to incorporate an aliphatic amine in order to assure complete reaction of the acid group of the polymer, in the event that some residual acid group may tend to react incompletely with the relatively more bulky aromatic amine.
  • the aliphatic amine may replace a portion of a more costly aromatic amine, while maintaining the majority of the performance of the aromatic amine.
  • Aliphatic monoamines include methylamine, ethylamine, propylamine and various higher amines. Diamines or polyamines can be used for this function, provided that, in general, they have only a single reactive amino group, that is, a primary or secondary, and preferably primary, group.
  • diamines include dimethylaminopropylamine, diethylaminopropylamine, dibutyl aminopropyl amine, dimethylaminoethylamine, diethylaminoethylamine, dibutylaminoethylamine, 1-(2-aminoethyl)piperidine, 1-(2-aminoethyl)pyrrolidone, aminoethylmorpholine, and aminopropylmorpholine.
  • the aliphatic amine having a single reactive amino group is N,N-dimethylaminopropylamine or aminopropylmorpholine.
  • the amine is an aromatic amine selected from the group consisting of:
  • N-arylphenylenediamines are the N-phenylphenylenediamines, such as for example, N-phenyl-1,4-phenylenediamine, N-phenyl-1,3-phenylenediamine, and N-phenyl-1,2-phenylenediamine.
  • the N-arylphenylenediamine is N-phenyl-1,4phenylenediamine.
  • the phenoxyaniline is 4-phenoxyaniline.
  • the polymeric composition or the oil-soluble product produced by the process of the present invention are typically added to base oil in sufficient amounts to provide soot and/or sludge dispersancy as well as viscosity index improvement when used in lubricating oil compositions for internal combustion engines.
  • the lubricating oil compositions of the present invention will contain a major amount of base oil of lubricating viscosity and a minor amount of the polymeric composition or the oil-soluble product produced by the process of the present invention,
  • Base oil as used herein is defined as a base stock or blend of base stocks which is a lubricant component that is produced by each manufacturer to the same specifications (independent of feed source or manufacturer's location); that meets the same manufacturer's specification; and that is identified by a unique formula, product identification number, or both.
  • Base stocks may be manufactured using a variety of different processes including but not limited to distillation, solvent refining, hydrogen processing, oligomerization, esterification, and rerefining. Rerefined stock shall be substantially free from materials introduced through manufacturing, contamination, or previous use.
  • the base oil of this invention may be any natural or synthetic lubricating base oil fraction particularly those having a kinematic viscosity at 1000 centigrade (0° C.) and about 4 centistokes (cSt) to about 20 cSt.
  • Hydrocarbon synthetic oils may include, for example, oils prepared from the polymerization of ethylene, polyalphaolefin or PAO, or from hydrocarbon synthesis procedures using carbon monoxide and hydrogen gases such as in a Fisher-Tropsch process.
  • a preferred base oil is one that comprises little, if any, heavy fraction; e.g., little if any, lube oil fraction of viscosity about 20 cSt or higher at about 100° C.
  • Oils used as the base oil will be selected or blended depending on the desired end; use and the additives in the finished oil to give the desired grade of engine oil, e.g. a lubricating oil composition having an SAE Viscosity Grade of 0W, 0W-20, 0W-30, 0W-40, 0W-50 , 0W-60, 5W, 5W-20, 5W-30 , 5W-40, 5W-50, 5W-60, 10W, 10W-20, 10W-30, 10W-40 10W-50, 15W, 15W-20, 15W-30, or 15W-40.
  • SAE Viscosity Grade 0W, 0W-20, 0W-30, 0W-40, 0W-50 , 0W-60, 5W, 5W-20, 5W-30 , 5W-40, 5W-50, 5W-60, 10W, 10W-20, 10W-30, 10W-40 10W-50, 15W, 15W-20, 15W-30, or 15W-40.
  • the base oil may be derived from natural lubricating oils, synthetic lubricating oils or mixtures thereof.
  • Suitable base oil includes base stocks obtained by isomerization of synthetic wax and slack wax, as well as hydrocrackate base stocks produced by hydrocracking (rather than solvent extracting) the aromatic and polar components of the crude.
  • Suitable base oils include those in all API categories I, II, III, IV and V as defined in API Publication 1509, 14th Edition, Addendum 1, December 1998. Saturates levels and viscosity indices for Group I, II and III base oils are listed in Table 1.
  • Group IV base oils are polyalphaolefins (PAO).
  • Group V base oils include all other base oils not included in Groups I, II, III or IV.
  • Natural lubricating oils may include animal oils, vegetable oils (e.g., rapeseed oils, castor oils and lard oil), petroleum oils, mineral oils and oils derived from coal or shale.
  • vegetable oils e.g., rapeseed oils, castor oils and lard oil
  • petroleum oils e.g., mineral oils and oils derived from coal or shale.
  • Synthetic oils may include hydrocarbon oils and halo-substituted hydrocarbon oils such as polymerized and inter-polymerized olefins, alkylbenzenes, polyphenyls, alkylated diphenyl ethers, alkylated diphenyl sulfides, as well as their derivatives, analogues and homologues thereof, and the like.
  • Synthetic lubricating oils also include alkylene oxide polymers, interpolymers, copolymers and derivatives thereof wherein the terminal hydroxyl groups have been modified by esterification, etherification, etc.
  • esters useful as synthetic oils also include those made from about C 5 to about C 12 monocarboxylic acids and polyols and polyol ethers.
  • Tri-alkyl phosphate ester oils such as those exemplified by tri-n-butyl phosphate and tri-iso-butyl phosphate are also suitable for use as base oils.
  • Silicon-based oils (such as the polyalkyl-, polyaryl-, polyalkoxyl-, or polyaryoxy-siloxane oils and silicate oils) comprise another useful class of synthetic lubricating oils.
  • Other synthetic lubricating oils include liquid esters of phosphorus-containing acids, polymeric tetrahydrofurans, polyalphaolefins, and the like.
  • the base oil may be derived from unrefined, refined, rerefined oils, or mixtures thereof.
  • Unrefined oils are obtained directly from a natural source or synthetic source (e.g., coal, shale, or tar sand bitumen) without further purification or treatment.
  • Examples of unrefined oils include a shale oil obtained directly from a retorting operation, a petroleum oil obtained directly from distillations or an ester oil obtained directly from an esterification process, each of which may then be used without further treatment.
  • Refined oils are similar to the unrefined oils except that refined oils have been treated in one or more purification steps to improve one or more properties.
  • Suitable purification techniques include distillation, hydrocracking, hydrotreating dewaxing, solvent extraction, acid or base extraction, filtration, and percolation, all of which are known to those skilled in the art.
  • Rerefined oils are obtained by treating used oils in processes similar to those used to obtain the refined oils. These rerefined oils are also known as reclaimed or reprocessed oils and often are additionally processed by techniques for removal of spent additives and oil breakdown products.
  • Base oil derived from the hydroisomerization of wax may also be used, either alone or in combination with the aforesaid natural and/or synthetic base oil.
  • Such wax isomerate oil is produced by the hydroisomerization of natural or synthetic waxes or mixtures thereof over a hydroisotmerization catalyst.
  • a major amount of base oil as defined herein comprises 40 wt % or more.
  • Preferred amounts of base oil comprise about 40 wt % to about 97 wt %, preferably greater than about 50 wt % to about 97 wt %, more preferably about 60 wt % to about 97 wt % and most preferably about 80 wt % to about 95 wt % of the lubricating oil composition. (When weight percent is used herein, it is referrng to weight percent of the lubricating oil unless otherwise specified.)
  • the amount of the polymeric composition and the oil-soluble product produced by the process of the present invention in the lubricating oil composition will be in a minor amount compared to the base oil of lubricating viscosity. Generally it will be in an amount from about 2 wt % to about 30 wt % preferably froim about 4 wt % to about 20 wt % and more preferably from about 6 wt % to about 12 wt %, based on the total weight of the lubricating oil composition.
  • additive components are examples of components that can be favorably employed in combination with the lubricating additive of the present invention. These examples of additives are provided to illustrate the present invention, but they are not intended to limit it.
  • MA maleic anhydride
  • the screw speed was set at 350 rpm and following temperature profile was used: 180° C., 185° C., 205° C., 180° C. with the die at 135° C. Excess reagents as well as peroxide decomposition products were removed with vacuum prior to polymer recovery.
  • the amount of MA grafted was 2.8 wt %.
  • the maleated copolymer was dissolved in neutral oil to a concentration of 7 wt %.
  • 100 parts of the maleated copolymer/oil mixture were charged to a stirred glass reactor and heated to about 160° C.
  • 0.38 parts of N-phenyl-1,4-phenylenediamine (NPPDA) (1.05 moles of N-phenyl-1,4-phenylenediamine per mote of grafted MA) were charged to the reactor.
  • the reactor was held at about 160° C. for two hours.
  • the amount of soot present in the finished lubricating oil composition when the lubricating oil composition viscosity increased 12 cSt above the initial viscosity was determined by interpolating soot and viscosity data obtained throughout the test.
  • the amount of soot in the finished lubricating oil composition at an increase of 12 cSt was found to be 7.18 wt.
  • Example 2 The dispersant viscosity index improver of Example 2 was prepared and tested according to Example 1 except that the amine compound used was 4-phenoxyaniline (4-PA) instead of NPPDA.
  • the amount of soot in the lubricating oil composition at an increase of 12 cSt was determined to be 6.02 wt % in the Mack T-11 engine test,
  • An ethylene-octene copolymer having 86.7 mole % ethylene, a R a R b product of 0.32 and less than 0.1 regio-inversions per 1000 carbon atoms was grafted with MA under the following conditions: 95.8 wt % of polymer, 4 wt % of Crystalman® Maleic Anhydride (available from ExxonMobil Chemical Company) were fed at 7 kgf/h feed rate to the hopper of the extruder and 2.23 wt % of a 10% solution of Luperox® 130 (di-tertiary buty peroxide available from Atofina Chemical Incorporated) dissolved in Marcolo 52 oil (mineral oil available from ESSO Petroleum Company Limited) were added to the second barrel. The screw speed was set at 400 rpm and following temperature profile was used: 180° C., 190° C., 210° C., 1800° C. with the die at 180° C. The amount of MA grafted was 3.2 wt %.
  • the maleated copolymer was dissolved in neutral oil to a concentration of 7 wt %. 100 parts of the maleated copolymer/oil mixture were charged to a stirred glass reactor and heated to about 160° C. 1.63 parts of an alcohol ethoxylate (Huntsman Surfonic® L24-7, a seven-mote ethoxylate of a linear, primary about C 12 to about C 14 alcohol) and 0.46 parts of NPPDA (1.05 moles of NPPDA per mole of grafted MA) were charged to the reactor. The reactor was held at about 160° C. for two hours and then cooled. Three subsequent batches were synthesized using the same raw materials and procedures. A total of four batches were made and blended together.
  • the amount of soot in the finished lubricating oil composition at an increase of 12 cSt was found to be 7.59 wt
  • the screw speed was set at 250 rpm and following temperature profile was used: 160° C., 185° C., 205° C., 210° C. with the die at 160° C.
  • the amount of MA grafted was 2.0 wt %.
  • the maleated copolymer was dissolved in neutral oil to a concentration of 6%. 100 parts of the maleated copolyymer/oil mixture were charged to a stirred glass reactor and heated to about 160° C.
  • the finished lubricating oil composition was then run in the Mack T-1 I engine test.
  • the amount of soot present in the finished lubricating oil composition when the lubricating oil composition viscosity increased 12 cSt above the initial viscosity 20 was 6.32 wt.
  • the dispersant viscosity index improver of Comparative Example B was prepared and tested according; to Comparative Example A except that: the amine compound used was 4-phenoxyaniline (4-PA) instead of NPPDA.
  • the amount of soot in the finished lubricating oil composition at an increase of 12 cSt was determined to be 5.42 wt % in the Mack T-12 engine test.
  • the maleated ethylene-propylene copolymer having 73.2 mole % ethylene of Comparative Example A was further grafted with MA in a second pass extrusion process under the following conditions: 98 wt % of polymer, 2 wt % of Crystalman® Maleic Anhydride (available from ExxoniMobil Chemical Company) were fed at 7 kg/h feed rate to the hopper of the extruder and 0.91 wt % of a 10% solution of Luperox® 130 (di-tertiary butyl peroxide available from Atofina Chemical Incorporated) dissolved in Marcol® 52 oil (mineral oil available from ESSO Petroleum Company Limited) were added to the second barrel.
  • Luperox® 130 di-tertiary butyl peroxide available from Atofina Chemical Incorporated
  • Marcol® 52 oil mineral oil available from ESSO Petroleum Company Limited
  • the screw speed was set at 250 rpm and following temperature profile was used: 160° C., 185° C., 205° C., 210° C. with the die at 145° C. A final grafting level of 2.6 wt % MA was achieved.
  • the maleated: copolymer was dissolved in neutral oil to a concentration of 6 wt %. 100 parts of the maleated copolymer/oil mixture were charged to a stirred glass reactor and heated to about 160° C.
  • a viscosity index improver having an ethylene-propylene copolymer with 68.4 mole % ethylene was prepared as specified in Example 1 except no amine was used and blended into a formulated lubricating oil composition to achieve a kinematic viscosity at about 100° C. equal to 14.5 cSt.
  • This material is available commercially from Chevron Oronite Company, LLC.
  • the finished lubricating oil composition was then run in the Mack T-11 engine test. The amount of soot present in the finished lubricating oil composition when the oil viscosity increased 12 cSt above the initial viscosity was 4.91 wt %.
  • the lubricating oil composition for each test is provided in Table 2 below.
  • Lubricating Oil Compositions a Examples Comparative Examples 1 2 3 A B C D Dispersant 7.5 8.0 8.5 8.5 8.5 8.5 7.5 Viscosity Index Improver, wt % Kinematic 14.3 14.3 14.5 14.4 13.5 14.8 15.6 viscosity at 100° C. (ASTM D445), cSt a
  • the wt % balance of the lubricating oil composition comprised Group I and Group II base oil, detergents, dispersants, wear inhibitors, antioxidants, friction modifiers, metal deactivators, foam inhibitors, and pour point depressants.
  • results of this data indicate that the dispersant viscosity index improvers of the present invention having high ethylene content, wherein the alpha-monoolefin has a monomer distribution resulting from a R a R b product measured by 13 C-NMR below 0.8 and a level of regio-inversions less than 2 per 1000 carbon atoms, provide superior soot dispersancy compared to lubricating oil compositions with viscosity index improvers having lower ethylene content.

Abstract

A polymeric composition is disclosed which contains an ethylene-alpha olefin copolymer backbone having at least 82 mole % ethylene and at most 18 mole % of an about C3 to about C28 alpla-monoolefin, wherein the alpha-monoolefin has a monomer distribution resulting from a RaRb product measured by 13C-NMR below 0.8 and a level of regio-inversions less than 2 per 1000 carbon atoms, and an amide group having the formula (I) and/or an imide group having the formula (II):
Figure US20070149414A1-20070628-C00001
wherein P is the ethylene-alpha olefin copolymer backbone, R1 is hydrogen or —CO—X′, R2 and R3 are independently hydrogen or —CH3, X and X′ are independently —OH, alkoxyl of 1 to about 24 carbon atoms, or a secondary or tertiary amine, provided that at least one of X and X′ is a secondary or tertiary amine, and Z is a tertiary amine, wherein Z and X and X′, when X and X′ are secondary or tertiary amines, are each independently derived from one or more amine compounds described herein.

Description

  • The present invention relates to dispersant viscosity index improvers employable as additives in synthetic and petroleum oils, particularly lubricating oils. More particularly, the present invention relates to dispersant viscosity index improvers having high ethylene content which have been grafted: with an ethylenically unsaturated acylating agent and subsequently reacted with an amine compound.
  • BACKGROUND OF THE INVENTION
  • Hydrocarbon polymers, particularly ethylene-propylene copolymers, are in widespread use as viscosity index (V.I.) improving additives for oil compositions, particularly lubricating oil compositions. A substantial body of prior art exists directed towards further reacting these ethylene copolymer V.I. improvers to form a multi-functional V.I. improver. This is a material useful as a V.I.-dispersant oil additive so as to improve not only the V.I. properties of the oil but to also impart dispersancy so as to suspend soot or sludge that may form during the operation or use of the lubricant in engines. Various patents teach grafting ethylene copolymers with maleic anhydride, followed by reaction with an amine. A number of these prior disclosures teach reducing or avoiding the use of polyamine having two primary amine groups to thereby reduce cross-linking problems which become more of a problem as the number of amine moieties added to the polymer molecule is increased in order to increase dispersancy. Generally, these patents used a primary-tertiary amine.
  • U.S. Pat. No. 4,160,739, issued Jul. 10, 1979, to Stambaugh et al. discloses graft copolymers wherein the backbone polymer is a polymeric hydrocarbon such as substantially linear ethylene/propylene copolymer and the grafted units are the residues of a monomer system comprising maleic acid or anhydride and one or more other monomers copolymerizable therewith, the monomer system being post-reacted with a polyamine compound comprising a primary or secondary amine. The graft copolymers impart combined, detergent, viscosity index improvement and other useful properties to lubricating oils and hydrocarbon motor fuels.
  • U.S. Pat. No. 4,320,019, issued Mar. 16, 1982, to Hayashi discloses reaction products prepared by reacting (a) interpolymers of ethylene, one or more C3 to C8 alpha-monoolefins, and one or more polyenes selected from non-conjugated dienes and trienes, in the absence of free radical initiator with (b) one or more olefinic carboxylic acid acylating agents to form an acylating reaction intermediate which is further reacted with (c) an amine. These reaction products have been found useful as multi-functional additives to a variety of lubricating oils for enhancing their dispersancy as well as improving their viscosity-temperature relationship.
  • U.S. Pat. No. 4,735,736, issued Apr. 5, 1988, to Chung discloses oil-soluble ethylene alpha-olefin hydrocarbon polymers, useful as V.I. improvers, such as ethylene copolymer, preferably ethylene-propylene copolymer, grafted with an unsaturated acid material, such as maleic anhydride, preferably by solid state grafting followed by reaction with a polyamine, preferably a tertiary-primary amine, and treatment and/or reaction with aliphatic monoamine. The resulting material is used in oil compositions, such as lubricating oil, as a viscosity index improver having sludge dispersancy properties. The monoamine treatment inhibits viscosity growth of the additive upon storage.
  • U.S. Pat. No. 4,863,623, issued Sep. 5, 1989, to Nalesnik discloses an additive composition comprising a graft and an amine-derivatized copolymer prepared from ethylene and at least one C3 to C10 alpha-monoolefin and, optionally, a polyene selected from non-conjugated dienes and trienes comprising from about 15 to 80 mole % of ethylene, from about 20 to 85 mole % of the C3 to C10 alpha-monoolefin and from about 0 to 15 mole % of the polyene having a average molecular weight ranging from about 5,000 to 500,000 which has been reacted with at least one olefinic carboxylic acid acylating agent to form one or more acylating reaction intermediates characterized by having a carboxylic acid acylating group within their structure and reacting the reaction intermediate with an amino-aromatic polyamine compound from the group consisting of an N-arylphenylenediamine, an aminothiazole, an aminocarbazole, an aminoindole, an aminopyrrole, an amino-indazolinone, an aminomercaptotriazole and an aminopyrimidine to form the graft and amine-derivatized copolymer. A lubricating oil composition containing the amine-derivatized copolymer is also disclosed.
  • U.S. Pat. No. 5,055,213, issued Oct. 8, 1991, to Germanaud et al. discloses additives resulting from the condensation of a primary or secondary amine and/or of an alkylene polyamine with a copolymer containing vicinal carboxylic groups. Derivatives of phenothiazine, or naphthylamine and of diphenylamine are employed in most cases as alkylene polyamine. These compounds can be employed as multifunctional additives to lubricants.
  • U.S. Pat. No. 5,182,041, issued Jan. 26, 1993, to Benfarmeo et al. discloses an additive composition comprising a graft and an amine-derivatized polymer having an average molecular weight ranging from about 300 to 3,500 which has been reacted with at least one olefinic carboxylic acid acylating agent to form one or more acylating reaction intermediates characterized by having a carboxylic acid acylating group within their structure and reacting the reaction intermediate with an amino-aromatic polyamine compound from the group consisting of an N-arylphenylenediamine, an aminothiazole, an aminocarbazole, an amino-indazolinone, an aminomercaptotriazole and an aminopyrimidine to form the graft and amine-derivatized copolymer.
  • U.S. Pat. No 5,366,647, issued Nov. 22, 1994, to Gutierrez et al. discloses a lubricating oil concentrate containing an oil soluble composition useful as a multifunctional viscosity index improver additive comprising an ethylene alpha-olefin polymer substituted with a mono- or dicarboxylic acid and at least one nucleophilic reagent selected from amines, alcohols, amino-alcohols, and reactive metal compounds. In this case, the unsaturated mono- or dicarboxylic moiety is introduced by reaction with the end chain unsaturation of the ethylene alpha-olefin copolymer in a peroxide free reaction.
  • U.S. Pat. No. 5,427,702, issued Jun. 27, 1995) to Chung et al. discloses novel multifunctional viscosity modifiers comprising a mixture of derivatized ethylene-alpha olefin copolymers, A and B. The A copolymer comprising from about 30 wt % to about 60 wt % monomer units derived from ethylene and the B copolymer comprising from about 60 wt % to about 80 wt % units derived from ethylene.
  • U.S. Pat. No. 5,429,757, issued Jul. 4, 1995, and U.S. Pat. No. 5,563,118, issued Oct. 8, 1996, to Mishra et al. disclose an additive composition comprising a graft and derivatized copolymer prepared from ethylene and at least one C3 to C10 alpha-monoolefin and, optionally, a polyene selected from non-conjugated dienes and trienes comprising from about 15 to 80 mole % of ethylene, from about 20 to 85 mole % of the C3 to C10 alpha-moonoolefin and from about 0 to 15 mole % of the polyone having an average molecular weight ranging from about 5,000 to 500,000, which has been reacted with at least one olefinic (carboxylic acid acylating agent to form one or more acylating reaction intermediates characterized by having a carboxylic acid acylating group within their structure and reacting the reaction intermediate with an amino-aromatic compound to form the graft derivatized copolymer.
  • U.S. Pat. No. 6,107,257, issued Aug. 22, 2000, to Valcho et al. discloses a novel additive comprising a highly grafted, multifunctional olefin copolymer comprising a graft and amine-derivatized copolymer prepared from ethylene and at least one C3 to C23 alpha-monoolefin and, optionally, a polyene, wherein the copolymer of ethylene and at least one C3 to C23 alpha-monoolefin has grafted thereon from 0.3 to 0.75 carboxylic groups per 1,000 number average molecular weight units of olefin copolymer and wherein the olefin copolymer has a number average molecular weight of between 20,000 and 150,000.
  • U.S. Pat. No.6,107,258, issued Aug. 22, 2000, to Esche, Jr. et al. discloses novel functionalized olefin copolymers and their use as additives in fuel and lubricating oil compositions. The functionalized olefin copolymers comprise an olefin copolymer on which has been grafted an ethylenically unsaturated carboxylic acid, or derivative thereof, to form an acylated olefin copolymer containing reactive carboxylic group. The acylated olefin copolymer is reacted with a coupling compound, which contains more than one amine, thiol and/or hydroxy group capable of reacting with the carboxylic group of preferably more than one acylated olefin copolymer to form the novel additives. Additionally, the acylated olefin copolymers, either before or after reaction with the coupling compound, are reacted with a performance enhancing compound or compounds, i.e., compounds containing only one functional group capable of reacting with the carboxylic group of the acylated olefin copolymer, in order to obtain further benefits such as improved antioxidancy, antiwear and additional dispersancy properties.
  • WO97/32946, issued Sep. 12, 1997, to Hughes et al. discloses linear ethylene polymers with defined melt flow and critical shear rate for onset of melt fracture used for the production of oleaginous compositions. It also discloses the grafting of these linear backbones with maleic anhydride as well as their reaction with a carboxylic acid, an amine or an alcohol.
  • Canadian Patent No. 2,021,959, issued Nov. 28, 2000, to Migdal et al. discloses an additive composition comprising a graft and an amine-derivatized copolymer prepared from ethylene and at least one C3 to C10 alpha-monoolefin and, optionally, a polyene selected from non-conjugated dienes and trienes comprising from about 15 to 80 mole % of ethylene, from about 20 to 85 mole % of the C3 to C10 alpha-monoolefin and from about 0 to 15 mole % of the polyene having an average molecular weight ranging from about 1,000 to 40,000 which has been reacted with at least one olefinic carboxylic acid acylating agent to form one or more acylating reaction intermediates characterized by having at least about 1.5 wt % of a carboxylic acid acylating group within their structure and reacting the reaction intermediate with an amino-aromatic polyamine compound from the group consisting of an N-arylphenylenediamine, an aminothiazole, an aminocarbazole, an aminoindole, an aminopyrrole, an amino-indazolinone, an aminomercaptotriazole and an aminopyrimidine to form the graft and amine-derivatized copolymer.
  • U.S. Patent Application Publication Number 2006/0025316 published Feb. 2, 2006, discloses a method for lubricating a diesel engine equipped with exhaust gas recirculation, comprising supplying thereto a composition comprising the reaction product of: (a) a polymer comprising carboxylic acid group or a reactive equivalent thereof, said polymer having a number average molecular weight of greater than 5,000; and (b) an amine component comprising at least one aromatic amine containing at least one amino group capable of condensing with said carboxylic acid group to provide a pendant group and at least one additional group comprising at least one nitrogen, oxygen, or sulfur atom, wherein said aromatic; amine is selected from the group consisting of (i) a nitro-substituted aniline, (ii) amines comprising two aromatic moieties linked by a —C(O)NR— group, a —C(O)O— groups an —O— group, an —N═N— group or an —SO2— group where R is hydrogen or hydrocarbyl, one of said aromatic moieties bearing said condensable amino group, (iii) an aminoquinoline, (iv) an aminobenzimidazole, (v) an N,N-dialkylphenylenediamine and (vi) a ring-substituted benzylamine.
  • SUMMARY OF THE INVENTION
  • The present invention relates to dispersant viscosity index improvers. In particular, the present invention relates to a polymeric composition having an ethylene-alpha olefin copolymer backbone comprising at least 82 mole % ethylene and at most 18 mole % of an about C3to about C28 alpha-monoolefin, wherein the alpha-monoolefin has a monomer distribution resulting from a RaRb product measured by 13C-NMR below 0.8 and a level of regio-inversions less than 2 per 1000 carbon atoms, and an amide group having the formula (i) and/or an imide group having the formula (II):
  • Figure US20070149414A1-20070628-C00002
      • wherein P is the ethylene-alpha olefin copolymer backbone, R1 is hydrogen or —CO—X′, R2 and R3 are independently hydrogen or —CH3, X and X′ are independently —OH, alkoxyl of 1 to about 24 carbon atoms, or a secondary or tertiary amine, provided that at least one of X and X′ is a secondary or tertiary amine, and Z is a tertiary amine, wherein Z and X and X′, when X and X′ are secondary or tertiary amines, are each independently derived from one or more of the following amines:
      • (a) an aromatic amine comprising two aromatic groups linked by a group, L, represented by the following formula.
  • Figure US20070149414A1-20070628-C00003
        • wherein L is selected from —O—, —N═N—, —NH—, —CH2NH—, —C(O)NR4—, —C(O)O—, —SO2—, —SO2NR5— or —SO2NH—, wherein R4 and R5 independently represent a hydrogen, an alkyl, an alkenyl or an alkoxyl group having from about 1 to about 8 carbon atoms;
        • wherein each Y1, Y2, Y3 and Y4 are independently N or CH provided that Y1 and Y2 may not both be N;
        • R6 and R7 independently represent a hydrogen, —OH, —NO2, —SO3H, —SO3Na, —CO2H or salt thereof, —NH-aryl, —NH-alkyl, —NH-alkaryl, —NH-aralkyl having up to about 24 carbon atoms or a branched or straight chain group having from about 4 to about 24 carbon atoms that can be alkyl, alkenyl, alkoxyl, aralkyl, alkaryl, hydroxyalkyl or aminoalkyl;
        • R8 and R9 independently represent a hydrogen, an alkyl, an alkenyl or an alkoxyl group having from about 1 to about 8 carbon atoms, —OH, —SO3H or —SO3Na; and
        • R10 represents —NH2, —NHR11, wherein R11 is an alkyl or an alkenyl group having from about 1 to about 8 carbon atoms, —CH2—(CH2)n—NH2or —CH2-aryl-NH2 and n is from 0 to about 10;
      • (b) an aminothiazole selected from the group consisting of aminothiazole, aminobenzothiazole, aminobenzothiadiazole and aminoalkylthiazole;
      • (c) an aminocarbazole represented by the formula:
  • Figure US20070149414A1-20070628-C00004
        • wherein R12 and R13 independently represent a hydrogen, an alkyl or alkenyl group having from about 1 to about 14 carbon atoms;
      • (d) an aminoindole represented by the formula:
  • Figure US20070149414A1-20070628-C00005
        • wherein R14 represents a hydrogen, an alkyl or alkenyl group having from about 1 to about 14 carbon atoms;
      • (e) an aminopyrrole represented by the formula:
  • Figure US20070149414A1-20070628-C00006
        • wherein R15 represents a divalent alkylene group having about 2 to about 6 carbon atoms and R16 represents: a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
      • (f) an amino-indazolinone represented by the formula:
  • Figure US20070149414A1-20070628-C00007
        • wherein R17 represents a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
      • (g) an aminomercaptotriazole represented by the formula:
  • Figure US20070149414A1-20070628-C00008
      • (h) an aminopyrimidine represented by the formula:
  • Figure US20070149414A1-20070628-C00009
        • wherein R18 represents a hydrogen, an alkyl, an alkenyl or an alkoxyl group having from about 1 to about 8 carbon atoms;
      • (i) a ring substituted or unsubstituted aniline, such as nitroaniline or 4-aminoacetanilide;
      • (j) an aminoquinoline;
      • (k) an aminobenzimidazole;
      • (l) a N,N-dialkylphenylenediamine; and
      • (m) a benzylamine
  • In a further embodiment, the present invention relates to dispersant viscosity index improvers having high ethylene alpha-monoolefin copolymer content prepared by the process of grafting an ethylene-alpha-monoolefin copolymer backbone comprising at least 82 mole % ethylene and at most 18 mole % an about C3 to about C28 alpha-monoolefin. wherein the alpha-monoolefin has a monomer distribution resulting from a RaRb product measured by 13C-NMR below 0.8 and a level of regio-inversions less than 2 per 1000 carbon atoms, with an ethylenically unsaturated acylating agent and subsequently reacting the resulting grafted copolymer with one, or more of the following amines:
      • (a) an aromatic amine comprising aromatic groups linked by a group, L, represented by the following formula:
  • Figure US20070149414A1-20070628-C00010
        • wherein L is selected from —O—, —N═N—, —NH—, —CH2NH—, —C(O)NR4, —C(O)O—, —SO2—, —SO2NR5— or —SO2NH—; wherein R4 and R5 independently represent a hydrogen, an alkyl, an alkenyl or an alkoxyl group having from about 1 to about 8 carbon atoms;
        • wherein each Y1, Y2, Y3 and Y4 are independently N or CH provided that Y1 and Y2 may not both be N;
        • R6 and R7 independently represent a hydrogen, —OH, —NO2, SO3H, —SO3Na, —CO2H or salt thereof, —NH-aryl, —NH-alkyl, —NH-alkaryl, —NH-aralkyl having up to about 24 carbon atoms or a branched or straight chain group having from about 4 to about 24 carbon atoms that can be alkyl, alkenyl, alkoxyl, aralkyl, alkaryl, hydroxyalkyl or aminoalkyl;
        • R8 and R9 independently represent a hydrogen, an alkyl, an alkenyl or an alkoxyl group having from about 1 to about 8 carbon atoms, —OH, —SO3H or —SO3Na, and
        • R10 represents —NH2, —NHR11, wherein R11 is an alkyl or an alkenyl group having from about 1 to about 8 carbon atoms, —CH2—(CH2)n—NH2 or —CH2-aryl-NH2 and n is from 0 to about 10;
      • (b) an aminothiazole selected from the group consisting of aminothiazole, aminobenzothiazole, aminobenzothiadiazole and aminoalkylthiazole,
      • (c) an aminocarbazole represented by the formula;
  • Figure US20070149414A1-20070628-C00011
        • wherein R12 and R13 independently represent a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
      • (d) an aminoindole represented by the formula
  • Figure US20070149414A1-20070628-C00012
        • wherein R14 represents a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
      • (e) an aminopyrrole represented by the formula:
  • Figure US20070149414A1-20070628-C00013
        • wherein R15 represents a divalent alkylene group having about 2 to about 6 carbon atoms and R16 represents a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
      • (f) an amino-indazolinone represented by the formula:
  • Figure US20070149414A1-20070628-C00014
        • wherein R17 represents a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms.
      • (g) an aminomercaptotriazole represented by the formula:
  • Figure US20070149414A1-20070628-C00015
      • (h) an aminopyrimidine represented by the formula:
  • Figure US20070149414A1-20070628-C00016
        • wherein R18 represents a hydrogen; an alkyl, an alkenyl, or an alkoxyl group having from about 1 to about 8 carbon atoms;
      • (i) a ring substituted or unsubstituted aniline, such as nitroaniline or 4-aminoacetanilide;
      • (j) an aminoquinoline;
      • (k) an aminobenzimidazole;
      • (l) a N,N-dialkylphenylenediamine; and
      • (m) a benzylamine
      • to yield an oil-soluble product having an amide group with the formula (I) and/or an imide group having the formula (II):
  • Figure US20070149414A1-20070628-C00017
      • wherein P is the ethylene-alpha olefin copolymer backbone, R1 is hydrogen or —CO—X′, R2 and R3 are independently hydrogen or —CH3, X and X′ are independently —OH, alkoxyl of 1 to about 24 carbon atoms, or a secondary or tertiary amine, provided that at least one of X and X′ is a secondary or tertiary amine, and Z is a tertiary amine, wherein Z and X and X′, when X and X′ are secondary or tertiary amines, are each independently derived from one or more of the amines in (a)-(m) above.
  • Preferably, the amine is an aromatic amine selected from the group consisting of
      • (a) an N-arylphenylenediamine represented by the formula:
  • Figure US20070149414A1-20070628-C00018
        • wherein R19 represents a hydrogen, —NH-aryl, —NH-alkyl, —NH-alkaryl, —NH-aralkyl having up to about 24 carbon atoms or a branched or straight chain having from about 4 to about 24 carbon atoms that can be alkyl, alkenyl, alkoxyl, aralkyl, alkaryl, hydroxyalkyl or aminoalkyl;
        • R20 represents —NH2, —CH2—(CH2)n—NH2, —CH2-aryl-NH2 and n is from about 1 to about 10; and
        • R21 represents a hydrogen, an alkyl an alkenyl, an alkoxyl, an aralkyl or an alkaryl group having about 4 to about 24 carbon atoms; and
      • (b) a phenoxyaniline represented by the formula:
  • Figure US20070149414A1-20070628-C00019
        • wherein R22 represents a hydrogen, —NH-aryl, —NH-alkyl, —NH-alkaryl, —NH-aralkyl having up to about 24 carbon atoms or a branched or straight chain having from about 4 to about 24 carbon atoms that can be alkyl, alkenyl, alkoxyl, aralkyl, alkaryl, hydroxyalkyl or aminoalkyl;
        • R23 represents —NH2, —CH2—(CH2)n—NH2, —CH2-aryl-NH2 and n is from about 1 to about 10; and
        • R24 represents a hydrogen, an alkyl an alkenyl, alkoxyl, an aralkyl or an alkaryl group having about 4 to about 24 carbon atoms.
  • The present invention also relates to a lubricating oil composition comprising a major amount of base oil of lubricating viscosity and a minor amount of the polymeric composition of the present invention.
  • The present invention also relates to a lubricating oil composition comprising a major amount of base oil of lubricating viscosity and a minor amount of an oil-soluble product produced by the above process.
  • Another aspect of the present invention relates to a method of improving the soot and/or sludge dispersancy in an internal combustion engine by operating the internal combustion engine with the lubricating oil composition of the present invention containing the polymeric composition.
  • Another aspect of the present invention relates to a method of improving the soot and/or sludge dispersancy in an internal combustion engine by operating the internal combustion engine with the lubricating oil composition of the present invention containing the oil-soluble product produced by the process of the present invention.
  • Among other things, the dispersant viscosity index improvers having high ethylene-alpha olefin copolymer content which have been grafted with an ethylenically unsaturated acylating agent and subsequently reacted with an amine compound provide multi-functional properties in lubricating oil compositions. In particular, the dispersant viscosity index improvers of the present invention provide superior soot and/or sludge dispersancy as well as viscosity index improvement when used in lubricating oil compositions for internal combustion engines. Such a lubricating oil composition is useful as a method of improving the soot and/or sludge dispersancy in an internal combustion engine, when the internal combustion engine is operated using the lubricating oil composition of the present invention.
  • DETAILED DESCRIPTION OF THE INVENTION
  • Prior to discussing the present invention in detail, the following terms will have the following meanings unless expressly stated to the contrary.
  • The terms “grafts” or “grafted” relate to covalent bonding of the grafting monomer to a polymer chain of the polymeric composition.
  • The term “oil soluble” refers to the ability of a material to dissolve in aliphatic and aromatic hydrocarbons such as lubricating oils or fuels in essentially all proportions.
  • The term “RaRb product” refers to the product of Ra and Rb where Ra is being defined as the ratio of the kinetic constant for the reaction of ethylene with a second ethylene unit and the kinetic constant for the reaction of ethylene with propylene and Rb as the ratio of the kinetic constant for the reaction of propylene with a second propylene unit and the kinetic constant for the reaction of propylene with ethylene. An “RaRb product” above 1 usually refers to polymers which are considered as blocky copolymers. The polymers of the present invention have a low “RaRb product” and are more alternating copolymers.
  • The term “level of regio-inversions” refers to the presence of monomer sequences where propylene (or the higher alpha-olefin) is polymerized head to head or tail to tail which translates into sequences of even-numbered methylene units instead of head to tail which translates into sequences of odd-numbered methylene units. The polymers of the present invention have almost no regio-inversions.
  • In the ethylene propylene copolymers, the “RaRb product” is measured by 13C-NMR spectroscopy according to J. C. Randall in Macromolecules 15, 1584 (1982) or J. C. Randall, Encyclopedia of Polymer Sciences and Engineering, Vol. 9, p. 795, 2nd Edition, John Wiley and Sons (1987) and the level of regio-inversions is measured according to S. Dimartino, M. Kelchtermans, Journal of Applied Polymer Sciences, 56, 1781 (1995). In the ethylene octene copolymers, the “RaRb product” is measured by 13C-NMR spectroscopy according: to F. Cavagna, Macromolecules, 14, 215 (1981) and the level of regio-inversions is measured according to P. J. Adriaensens, Polymer 44 (12), 3483 (2003).
  • The polymer or copolymer substrate or backbone of the present invention may be prepared from ethylene and propylene or it may be prepared from ethylene and a higher olefin within the range of an about C3 to about C28 alpha-monoolefin, wherein the alpha-monoolefin has a monomer distribution resulting from a RaRb product measured by 13C-NMR below 0.8 and a level of regio-inversions less than 2 per 1000 carbon atoms.
  • More complex polymer substrates, often designated as interpolymers, may be prepared using a third component. 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 about 5 to about 14 carbon atoms in the chain. Preferably, the diene monomer is characterized by the presence of a vinyl group in its structure and can include cyclic and bi-cyclo 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. A preferred 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 present invention are 1-isopropylidene-3a,4,7,7a-tetrahydroindene, 1-isopropylidenedicyclopentadiene, dehydro-isodicyclopentadiene, and 2-(2-methylene-4-methyl-3-pentenyl)[2.2.1]bicyclo-5-heptene.
  • The polymerization reaction to form the polymer or copolymer backbone is generally carried out in the presence of a catalyst in a solvent medium. The polymerization solvent may be any suitable inert organic solvent that is liquid under reaction conditions for solution polymerization of monoolefins which is generally conducted in the presence of a Ziegler-type catalyst. Examples of satisfactory hydrocarbon solvents include straight chain paraffins having from about 5 to about 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. It is desirable that the solvent be free of substances that will interfere with a Ziegler polymerization reaction.
  • In a typical preparation of a polymer or copolymer backbone, hexane is first introduced into a reactor and the temperature in the reactor is raised moderately to about 30° C. Dry propylene is fed to the reactor until the pressure reaches about 40 to about 45 inches of mercury. The pressure is then increased to about 60 inches of mercury and dry ethylene and 5-ethylindene-2-norbornene are fed to the reactor. The monomer feeds are stopped and a mixture of aluminum sesquichloride and vanadium oxytrichloride is added to initiate the polymerization reaction. Completion of the polymerization reaction is evidenced by a drop in the pressure in the reactor.
  • Ethylene-propylene or higher alpha-monoolefin copolymers of the present invention may consist of at least 82 mole % ethylene and at most 18 mole % propylene or higher alpha-monoolefin with the preferred mole ratios being at least 84 mole % ethylene and at most 16 mole % of a about C3 to about C28 alpha-monoolefin.
  • Preferably, the alpha monoolefin is from about C3 to about C20 and more preferably from about C6 to about C12 alpha-monoolefin. Most preferred alpha-monoolefin is octene.
  • Terpolymer variations of the foregoing polymers may contain from 0 to about 10 mole %, preferably about 0 to about 6 mole %, more preferably about 0 to about 3 mole %, of a non-conjugated diene or triene. In the most preferred embodiment, the foregoing polymers will not contain any non-conjugated diene or triene.
  • The polymer substrate, that is the ethylene copolymer or terpolymer is an oil-soluble, substantially linear, rubbery material having a weight average molecular weight from about 5,000 to about 500,000 with a preferred weight average molecular weight range of about 25,000 to about 250,000 and a most preferred range from about 50,000 to about 150,000.
  • 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 their basic characteristics are not materially changed.
  • An ethylenically unsaturated acylating agent is next grafted onto the prescribed copolymer backbone. The ethylenically unsaturated acylating agent can be represented by formula (A) and/or formula (B):
  • Figure US20070149414A1-20070628-C00020
  • wherein R1 is hydrogen or —CO—W′, R2 and R3 are independently hydrogen or —CH3; and W and W′ are independently —OH, or alkoxyl having 1 to about 24 carbon atoms.
  • Maleic anhydride or a derivative thereof is the preferred ethylenically unsaturated acylating agent. It grafts onto the ethylene copolymer or terpolymer to give two carboxylic acid functionalities.
  • The ethylenically unsaturated acylating agent may be grafted onto the copolymer backbone in a number of ways. It may be grafted onto tile backbone by a thermal process known as the “ene” process or by grafting in solution or in melt form using a free-radical initiator. The free-radical induced grafting of ethylenically unsaturated acylating agents is carried out in solvents, such as hexane, heptane, mineral oil or aromatic solvents, which do not react with the peroxide, it is carried out at an elevated temperature in the range of about 100° C. to about 250° C., preferably about 120° C. to about 190° C. and more preferably at about 150° C. to about 180° C., e.g. above 160° C., in a solvent preferably a mineral oil solution containing, e.g. about 1 wt % to about 50 wt %, preferably about 5 wt % to about 30 wt %, based on the initial total oil solution, of the ethylene copolymer and preferably under an inert environment.
  • The free-radical initiators which may be used are peroxides (diacyl peroxides such as benzoyl peroxide, dialkyl peroxides such as 1,1-bis(tert-butylperoxy)cyclohexane. 1,1-bis(tert-butylperoxy)-3,3,5-trimethylcyclohexane, 2,2-bis(tert-butylperoxy)butane, dicumylperoxide, tert-butylcumylperoxide, a,a′-bis(tert-butylperoxyisopropyl)benzene, di-tert-butylperoxide (DTBP), 2,5-dimethyl-2,5-di(tert-butylperoxy)+hexane, 2,5-dimethyl-2,5-di(tert-butylperoxy)-hexyne), hydroperoxides, peroxyesters such as tert-butyl peroxy benzoate, tert-butylperoxy acetate, O,O-tert-butyl-O-(2-ethylhexyl)monoperoxy carbonate, peroxketals such as n-butyl 4,4-di-(tert-butylperoxy)valerate and the like and azo compounds and preferably those which have a boiling point greater than about 100° C. and decompose thermally within the grafting temperature range to provide free radicals. The initiator is used in an amount of between about 0.005% and about 1% by weight based on the weight of the reaction mixture solution. The grafting is preferably carried out in an inert atmosphere, such as under nitrogen blanketing. The resulting polymer intermediate is characterized by having acylating group, typified by a carboxylic acid or acid chloride, within its structure.
  • In the solid or melt process for forming a graft copolymer, the ethylenically unsaturated acylating agent with the optional use of a radical initiator is grafted on molten rubber using rubber masticating or shearing equipment. Single screw but preferably twin screw extruder reactors such as co-rotating intermeshing extruders or counter-rotating non-intermeshing extruders but also co-kneaders such as those sold by Buss are especially preferred. The temperature of the molten material in this process may range from about 120° C. to about 400° C.
  • The preferred sequence of events used for the grafting reaction consists of melting the copolymeric composition, adding and dispersing the grafting monomer, introducing the peroxide and venting the unreacted monomer and by-products resulting from the peroxide decomposition. Other sequences may include feeding the monomers and the peroxide pre-dissolved in a solvent.
  • The copolymer intermediate is then reacted with an amine compound from the group consisting of:
      • (a) an aromatic amine comprising two aromatic groups, linked by a group L, represented by the following formula:
  • Figure US20070149414A1-20070628-C00021
        • wherein L is selected from —O—, —N═N—, —NH—,—CH2NH—, —C(O)N4—, —C(O)O—, —SO2—, —SO2NR5— or —SO2NH—; wherein R4 and R5 independently represent a hydrogen, an alkyl, an alkenyl or an alkoxyl group having from about 1 to about 8 carbon atoms;
        • wherein each Y1, Y2, Y3 and Y4 are independently N or CH provided that Y1 and Y2 may not both be N;
        • R6 and R7 independently represent a hydrogen, —OH: —NO2, —SO3H, —SO3Na, —CO2H or salt thereof, —NH-aryl, —NH-alkyl, —NH-alkaryl, —NH-aralkyl having up to about 24 carbon atoms or a branched or straight chain group having from about 4 to about 24 carbon atoms that can be alkyl, alkenyl, alkoxyl, aralkyl alkaryl, hydroxyalkyl or aminoalkyl;
        • R8 and R9 independently represent a hydrogen, an alkyl, an alkenyl or an alkoxyl group having from about 1 to about 8 carbon atoms, —OH, —SO3H or —SO3Na; and
        • R10 represents —NH2, —NHR11, wherein R11 is an alkyl or an alkenyl group having from about 1 to about 8 carbon atoms, —CH2—(CH2)n—NH2or —CH2-aryl-NH2 and n is from 0 to about 10;
      • (b) an aminothiazole selected from the group consisting of aminothiazole, aminobenzothiazole, aminobenzothiadiazole and aminoalkylthiazole;
      • (c) an aminocarbazole represented by the formula:
  • Figure US20070149414A1-20070628-C00022
        • wherein R12 and R13 independently represent a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
      • (d) an aminoindole represented by the formula:
  • Figure US20070149414A1-20070628-C00023
        • wherein R14 represents a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
      • (e) an aminopyrrole represented by the formula:
  • Figure US20070149414A1-20070628-C00024
        • wherein R15 represents a divalent alkylene group having about 2 to about 6 carbon atoms and R16 represents a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
      • (f) an amino-indazolinone represented by the formula:
  • Figure US20070149414A1-20070628-C00025
        • wherein R17 represents a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
      • (9) an aminomercaptotriazole represented by the formula:
  • Figure US20070149414A1-20070628-C00026
      • (h) an aminopyrimidine represented by the formula:
  • Figure US20070149414A1-20070628-C00027
        • wherein R18 represents a hydrogen, an alkyl, an alkenyl or an alkoxyl group having from about 1 to about 8 carbon atoms,
      • (i) a ring substituted or unsubstituted aniline, such as nitroaniline or 4-aminoacetanilide;
      • (j) an aminoquinoline;
      • (k) an aminobenzimidazole;
      • (l) a N,N-dialkylphenylenediamine; and
      • (m) a benzylamine.
  • The aromatic amine compounds above are substantially described, for example, in U.S. Pat. No. 4,863,623 and U.S. Patent Application Publication No. 200610025316A1, the disclosures of which are, herein incorporated by reference for all purposes.
  • The reaction between the copolymer intermediate having grafted thereon carboxylic acid or acid chloride acylating group and the prescribed amine compound is conducted by heating a solution of the copolymer backbone under inert conditions and then adding the amine compound to the heated solution generally with mixing to effect the reaction. It is convenient to employ an oil solution of the copolymer backbone heated to about 140° C. to about 175° C. while maintaining the solution under a nitrogen blanket. The amine compound is added to this solution and the reaction is effected under the noted conditions. The reaction can also be carried out without solvent in a reactive extruder.
  • The amine compound may, in general, contain one or more reactive (condensable) amino groups. A single reactive amino group is sometimes preferred. Multiple amino groups, as in the case of the above described N,N-dialkylphenylenediamine, can be useful as well, especially if they are reacted under relatively mild conditions so as to avoid excessive crosslinking or gellation of the polymer.
  • The above-described amine compounds can be used alone or in combination with each other. They can also be used in combination with additional, aromatic or non-aromatic, e.g., aliphatic, amines, which, in one embodiment, comprise about 1 to about 8 carbon atoms. Other aromatic amines can include such amines as aminodiphenylamine. These additional amines can be included for a variety of reasons. Sometimes it may be desirable to incorporate an aliphatic amine in order to assure complete reaction of the acid group of the polymer, in the event that some residual acid group may tend to react incompletely with the relatively more bulky aromatic amine. Alternatively, the aliphatic amine may replace a portion of a more costly aromatic amine, while maintaining the majority of the performance of the aromatic amine. Aliphatic monoamines include methylamine, ethylamine, propylamine and various higher amines. Diamines or polyamines can be used for this function, provided that, in general, they have only a single reactive amino group, that is, a primary or secondary, and preferably primary, group. Suitable examples of diamines include dimethylaminopropylamine, diethylaminopropylamine, dibutyl aminopropyl amine, dimethylaminoethylamine, diethylaminoethylamine, dibutylaminoethylamine, 1-(2-aminoethyl)piperidine, 1-(2-aminoethyl)pyrrolidone, aminoethylmorpholine, and aminopropylmorpholine. Preferably the aliphatic amine having a single reactive amino group is N,N-dimethylaminopropylamine or aminopropylmorpholine.
  • Preferably, the amine is an aromatic amine selected from the group consisting of:
      • (a) an N-arylphenylenediamine represented by the formula:
  • Figure US20070149414A1-20070628-C00028
        • wherein R19 represents a hydrogen, —NH-aryl, —NH-alkyl —NH-alkaryl, —NH-aralkyl having up to about 24 carbon atoms or a branched or straight chain having from about 4 to about 24 carbon atoms that can be alkyl, alkenyl, alkoxyl, aralkyl, alkaryl, hydroxyalkyl or aminoalkyl;
        • R20 represents —NH2, —CH2—(CH2)n—NH2, —CH2-aryl-NH2 and n is from about 1 to about 10, and
        • R21 represents a hydrogen, an alkyl an alkenyl, an alkoxyl, an aralkyl or an alkaryl group having about 4 to about 24 carbon atoms; and
      • (b) a phenoxyaniline represented by the formula:
  • Figure US20070149414A1-20070628-C00029
        • wherein R22 represents a hydrogen, —NH-aryl, —NH-alkyl, —NH-alkaryl, —NH-aralkyl having up to about 24 carbon atoms or a branched or straight chain having from about 4 to about 24 carbon atoms that can be alkyl, alkenyl, alkoxyl, aralkyl, alkaryl, hydroxyalkyl or aminoalkyl;
        • R23 represents —NH2, —CH2—(CH2)n—NH2, —CH2-aryl-NH2 and n is from about 1 to about 10; and
        • R24 represents a hydrogen, an alkyl, an alkenyl, an alkoxyl, an aralkyl or an alkaryl group having about 4 to about 24 carbon atoms.
  • Particularly preferred N-arylphenylenediamines are the N-phenylphenylenediamines, such as for example, N-phenyl-1,4-phenylenediamine, N-phenyl-1,3-phenylenediamine, and N-phenyl-1,2-phenylenediamine. Most preferably, the N-arylphenylenediamine is N-phenyl-1,4phenylenediamine. Preferably, the phenoxyaniline is 4-phenoxyaniline.
  • The Lubricating Oil Composition
  • The polymeric composition or the oil-soluble product produced by the process of the present invention are typically added to base oil in sufficient amounts to provide soot and/or sludge dispersancy as well as viscosity index improvement when used in lubricating oil compositions for internal combustion engines. Generally, the lubricating oil compositions of the present invention will contain a major amount of base oil of lubricating viscosity and a minor amount of the polymeric composition or the oil-soluble product produced by the process of the present invention,
  • Base Oil of Lubricating Viscosity
  • Base oil as used herein is defined as a base stock or blend of base stocks which is a lubricant component that is produced by each manufacturer to the same specifications (independent of feed source or manufacturer's location); that meets the same manufacturer's specification; and that is identified by a unique formula, product identification number, or both. Base stocks may be manufactured using a variety of different processes including but not limited to distillation, solvent refining, hydrogen processing, oligomerization, esterification, and rerefining. Rerefined stock shall be substantially free from materials introduced through manufacturing, contamination, or previous use.
  • The base oil of this invention may be any natural or synthetic lubricating base oil fraction particularly those having a kinematic viscosity at 1000 centigrade (0° C.) and about 4 centistokes (cSt) to about 20 cSt. Hydrocarbon synthetic oils may include, for example, oils prepared from the polymerization of ethylene, polyalphaolefin or PAO, or from hydrocarbon synthesis procedures using carbon monoxide and hydrogen gases such as in a Fisher-Tropsch process. A preferred base oil is one that comprises little, if any, heavy fraction; e.g., little if any, lube oil fraction of viscosity about 20 cSt or higher at about 100° C. Oils used as the base oil will be selected or blended depending on the desired end; use and the additives in the finished oil to give the desired grade of engine oil, e.g. a lubricating oil composition having an SAE Viscosity Grade of 0W, 0W-20, 0W-30, 0W-40, 0W-50 , 0W-60, 5W, 5W-20, 5W-30 , 5W-40, 5W-50, 5W-60, 10W, 10W-20, 10W-30, 10W-40 10W-50, 15W, 15W-20, 15W-30, or 15W-40.
  • The base oil may be derived from natural lubricating oils, synthetic lubricating oils or mixtures thereof. Suitable base oil includes base stocks obtained by isomerization of synthetic wax and slack wax, as well as hydrocrackate base stocks produced by hydrocracking (rather than solvent extracting) the aromatic and polar components of the crude. Suitable base oils include those in all API categories I, II, III, IV and V as defined in API Publication 1509, 14th Edition, Addendum 1, December 1998. Saturates levels and viscosity indices for Group I, II and III base oils are listed in Table 1. Group IV base oils are polyalphaolefins (PAO). Group V base oils include all other base oils not included in Groups I, II, III or IV.
  • TABLE 1
    Saturates, Sulfur and Viscosity Index of Group I, II, III, IV and V Base
    Stocks
    Saturates (As determined by Viscosity Index
    ASTM D2007) (As determined by ASTM
    Sulfur (As determined by D4294, ASTM D4297
    Group ASTM D2270) or ASTM D3120)
    I Less than 90% saturates and/ Greater than or equal to 80 and
    or Greater than to 0.03% less than 120
    sulfur
    II Greater than or equal to 90% Greater than or equal to 80 and
    saturates and less than or less than 120
    equal to 0.03% sulfur
    III Greater than or equal to 90% Greater than or equal to 120
    saturates and less than or
    equal to 0.03% sulfur
    IV All Polyalphaolefins (PAOs)
    V All others not included in Groups I, II, III, or IV
  • Natural lubricating oils may include animal oils, vegetable oils (e.g., rapeseed oils, castor oils and lard oil), petroleum oils, mineral oils and oils derived from coal or shale.
  • Synthetic oils may include hydrocarbon oils and halo-substituted hydrocarbon oils such as polymerized and inter-polymerized olefins, alkylbenzenes, polyphenyls, alkylated diphenyl ethers, alkylated diphenyl sulfides, as well as their derivatives, analogues and homologues thereof, and the like. Synthetic lubricating oils also include alkylene oxide polymers, interpolymers, copolymers and derivatives thereof wherein the terminal hydroxyl groups have been modified by esterification, etherification, etc. Another suitable class of synthetic lubricating oils comprises the esters of dicarboxylic acids with a variety of alcohols: Esters useful as synthetic oils also include those made from about C5 to about C12 monocarboxylic acids and polyols and polyol ethers. Tri-alkyl phosphate ester oils such as those exemplified by tri-n-butyl phosphate and tri-iso-butyl phosphate are also suitable for use as base oils.
  • Silicon-based oils (such as the polyalkyl-, polyaryl-, polyalkoxyl-, or polyaryoxy-siloxane oils and silicate oils) comprise another useful class of synthetic lubricating oils. Other synthetic lubricating oils include liquid esters of phosphorus-containing acids, polymeric tetrahydrofurans, polyalphaolefins, and the like.
  • The base oil may be derived from unrefined, refined, rerefined oils, or mixtures thereof. Unrefined oils are obtained directly from a natural source or synthetic source (e.g., coal, shale, or tar sand bitumen) without further purification or treatment. Examples of unrefined oils include a shale oil obtained directly from a retorting operation, a petroleum oil obtained directly from distillations or an ester oil obtained directly from an esterification process, each of which may then be used without further treatment. Refined oils are similar to the unrefined oils except that refined oils have been treated in one or more purification steps to improve one or more properties. Suitable purification techniques include distillation, hydrocracking, hydrotreating dewaxing, solvent extraction, acid or base extraction, filtration, and percolation, all of which are known to those skilled in the art. Rerefined oils are obtained by treating used oils in processes similar to those used to obtain the refined oils. These rerefined oils are also known as reclaimed or reprocessed oils and often are additionally processed by techniques for removal of spent additives and oil breakdown products.
  • Base oil derived from the hydroisomerization of wax may also be used, either alone or in combination with the aforesaid natural and/or synthetic base oil.
  • Such wax isomerate oil is produced by the hydroisomerization of natural or synthetic waxes or mixtures thereof over a hydroisotmerization catalyst.
  • It is preferred to use a major amount of base oil in the lubricating oil composition of the present invention. A major amount of base oil as defined herein comprises 40 wt % or more. Preferred amounts of base oil comprise about 40 wt % to about 97 wt %, preferably greater than about 50 wt % to about 97 wt %, more preferably about 60 wt % to about 97 wt % and most preferably about 80 wt % to about 95 wt % of the lubricating oil composition. (When weight percent is used herein, it is referrng to weight percent of the lubricating oil unless otherwise specified.)
  • The amount of the polymeric composition and the oil-soluble product produced by the process of the present invention in the lubricating oil composition will be in a minor amount compared to the base oil of lubricating viscosity. Generally it will be in an amount from about 2 wt % to about 30 wt % preferably froim about 4 wt % to about 20 wt % and more preferably from about 6 wt % to about 12 wt %, based on the total weight of the lubricating oil composition.
  • Other Additive Components
  • The following additive components are examples of components that can be favorably employed in combination with the lubricating additive of the present invention. These examples of additives are provided to illustrate the present invention, but they are not intended to limit it.
      • (A) Detergents are additives designed to hold the acid-neutralizing compounds in solution in the oil. They are usually alkaline and react with the strong acids (sulfuric and nitric) which form during the combustion of the fuel and which would cause corrosion to the engine parts if left unchecked. Examples are carboxylates, sulfurized or unsulfurized alkyl or alkenyl phenates, alkyl or alkenyl aromatic sulfonates, sulfurized or unsulfurized metal salts of multi-hydroxy alkyl or alkenyl aromatic compounds, alkyl or alkenyl hydroxy aromatic sulfonates, sulfurized or unsulfurized alkyl or alkenyl naphthenates, metal salts of alkanoic acids, metal salts of an alkyl or alkenyl multiacids and chemical and physical mixtures thereof.
      • (B) Dispersants are additives that keep soot and combustion products in suspension in the body of the oil charge and therefore prevent deposition as sludge or lacquer. Typically, the ashless dispersants are nitrogen-containing dispersants formed by reacting alkenyl succinic acid anhydride with an amine. Examples are alkenyl succinimides, alkenyl succinimides modified with other organic compounds. e.g., ethylene carbonating post-treatment, alkenyl succinimides modified with boric acid, polysuccinimides, and alkenyl succinic ester.
      • (C) Oxidation Inhibitors:
        • 1) Phenol type phenolic) oxidation inhibitors: 4,4′-methylenebis (2,6-di-tert-butylphenol),4,4′-bis(2,6-di-tert-butylphenol), 4,4′-bis(2-methyl-6-tert-butylphenol), 2,2′-(methylenebis(4-methyl-6-tert-butyl-phenol), 4,4′-butyli dene-bis(3-methyl-6-tert-butylphenol), 4,4′-isopropylidenebis(2,6-di-tert-butylphenol), 2,2′-methylenebis(4-methyl-6-nonylphenol), 2,2′-isobutyli dene-bis(4,6-dimethylphenol), 2,2′-methylenebis(4-methyl-6-cyclohexylphenol), 2,6-di-tert-butyl-4-methylphenol, 2,6-di-tert-butyl-4-ethylphenol, 2,4-dimethyl-6-tert-butyl-phenol, 2,6-di-tert-α-dimethylamino-p-cresol, 2,6-di-tert-4(N,N′ dimethylaminomethylphenol),4,4′-thiobis(2-methyl-6-tert-butylphenol), 2,2′-thiobis(4-methyl-6-tert-butylphenol), bis(3-methyl-4-hydroxy-5tert-butylbenzyl)-sulfide and bis(3,5-di-tert-butyl-4-hydroxybenzyl).
        • 2) Diphenylamine type oxidation inhibitor: alkylated diphenylamine, phenyl-α-naphthylamine and alkylated α-naphthylamine.
        • 3) Other types: metal dithiocarbamate (e.g., zinc dithiocarbamate), and methylenebis(dibutyldithiocarbamate).
      • (D) Rust Inhibitors (Anti-rust agents):
        • 1) Nonionic polyoxyethylene surface active agents: polyoxyethylene lauryl ether, polyoxyethylene higher alcohol ether, polyoxyethylene nonylphenyl ether, polyoxyethylene octylphenyl ether, polyoxyethylene octyl stearyl ether, polyoxyethylene oleyl ether, polyoxyethylene sorbitol monostearate, polyoxyethylene sorbitol mono-oleate and polyethylene glycol monooleate.
        • 2) Other compounds: stearic acid and other fatty acids, dicarboxilic acids, metal soaps, fatty acid amine salts, metal salts of heavy sulfonic acid, partial carboxylic acid ester of polyhydric alcohol and phosphoric ester.
      • (E) Demulsifiers: addition product of alkylphenol and ethyleneoxide, polyoxyethylene alkyl ether and polyoxyethylene sorbitane ester.
      • (F) Extreme pressure agents (EP agents): sulfurized oils, diphenyl sulfide, methyl trichlorostearate, chlorinated naphthalene, benzyl iodide fluoroalkylpolysiloxane and lead naphthenate.
      • (G) Friction modifiers: fatty alcohol, fatty acid, amine, borated ester and other esters.
      • (H) Multifunctional additives: sulfurized oxymolybdenum dithiocarbamate, sulfurized oxymolybdenum organo phosphorodithioate, oxymolybdenum monoglyceride, oxymolybdenum diethylate amide, amine-molybdenum complex compound and sulfur-containing molybdenum complex compounds.
      • (I) Viscosity Index improvers (VII); polymethacrylate type polymers, ethylene-propylene copolymers, styrene-isoprene copolymers, hydrogenated styrene-isoprene copolymers, hydrogenated star-branched polyisoprene, polyisobutylene, hydrogenated star-branched styrene-isoprene copolymer and dispersant type viscosity index improvers.
      • (J) Pour point depressants: polymethyl methacrylates, alkylmethacrylates and dialkyl fumarate-vinyl acetate copolymers.
      • (K) Foam inhibitors: alkyl methacrylate polymers and dimethyl silicone polymers.
      • (L) Wear Inhibitors: zinc dialkyldithiophosphate (Zn-DTP, primary alkyl type, secondary alkyl type, aryl type or mixtures thereof).
    EXAMPLES
  • The invention will be further illustrated by the following examples, which set forth particularly advantageous method embodiments. While the Examples are provided to illustrate the present invention, they are not intended to limit it.
  • Example 1
  • An ethylene-octene copolymer having 86.7 mole % ethylene, a RaRb product of 0.32 and less than 0.1 regio-inversions per 1000 carbon atoms was grafted with maleic anhydride (MA) using peroxide on a non-intermeshing counter-rotating twin screw extruder (30 mm, Length/Diameter=48) under the following conditions: 96.3 wt % of polymer, 3.1 wt % of Crystalman® Maleic Anhydride (available from ExxonMobil Chemical Company) were fed at 7 kgyh feed rate to the hopper of the extruder and 1.9 wt % of a 10% solution of Luperox® 130 (di-tertiary butyl peroxide available from Atofina Chemical Incorporated) dissolved in Marcol®) 52 oil (mineral oil available from ESSO Petroleum Company Limited) were added to the second barrel. The screw speed Was set at 350 rpm and following temperature profile was used: 180° C., 185° C., 205° C., 180° C. with the die at 135° C. Excess reagents as well as peroxide decomposition products were removed with vacuum prior to polymer recovery.
  • The amount of MA grafted was 2.8 wt %. The maleated copolymer was dissolved in neutral oil to a concentration of 7 wt %. 100 parts of the maleated copolymer/oil mixture were charged to a stirred glass reactor and heated to about 160° C. 0.38 parts of N-phenyl-1,4-phenylenediamine (NPPDA) (1.05 moles of N-phenyl-1,4-phenylenediamine per mote of grafted MA) were charged to the reactor. The reactor was held at about 160° C. for two hours. 1.63 parts of an alcohol ethoxylate (Huntsman Surfonic® L24-7, a seven-mole ethoxylate of a linear, primary about C12 to about C14 alcohol) were added to reaction mixture just before the reaction mixture was cooled to stabilize viscosity. Three subsequent batches were synthesized using the same raw materials and procedures. A total of four batches were made and blended together. The resulting dispersant viscosity index improver was blended into a formulated lubricating oil composition as indicated in Table 2 below, using a base oil to achieve a kinematic viscosity at about 100° C. equal to 14.5 cSt. The finished lubricating oil composition was then run in the Mack T-11 engine test as specified in ASTM D7156. The amount of soot present in the finished lubricating oil composition when the lubricating oil composition viscosity increased 12 cSt above the initial viscosity was determined by interpolating soot and viscosity data obtained throughout the test. The amount of soot in the finished lubricating oil composition at an increase of 12 cSt was found to be 7.18 wt.
  • Example 2
  • The dispersant viscosity index improver of Example 2 was prepared and tested according to Example 1 except that the amine compound used was 4-phenoxyaniline (4-PA) instead of NPPDA. The amount of soot in the lubricating oil composition at an increase of 12 cSt was determined to be 6.02 wt % in the Mack T-11 engine test,
  • Example 3
  • An ethylene-octene copolymer having 86.7 mole % ethylene, a RaRb product of 0.32 and less than 0.1 regio-inversions per 1000 carbon atoms was grafted with MA under the following conditions: 95.8 wt % of polymer, 4 wt % of Crystalman® Maleic Anhydride (available from ExxonMobil Chemical Company) were fed at 7 kgf/h feed rate to the hopper of the extruder and 2.23 wt % of a 10% solution of Luperox® 130 (di-tertiary buty peroxide available from Atofina Chemical Incorporated) dissolved in Marcolo 52 oil (mineral oil available from ESSO Petroleum Company Limited) were added to the second barrel. The screw speed was set at 400 rpm and following temperature profile was used: 180° C., 190° C., 210° C., 1800° C. with the die at 180° C. The amount of MA grafted was 3.2 wt %.
  • The maleated copolymer was dissolved in neutral oil to a concentration of 7 wt %. 100 parts of the maleated copolymer/oil mixture were charged to a stirred glass reactor and heated to about 160° C. 1.63 parts of an alcohol ethoxylate (Huntsman Surfonic® L24-7, a seven-mote ethoxylate of a linear, primary about C12 to about C14 alcohol) and 0.46 parts of NPPDA (1.05 moles of NPPDA per mole of grafted MA) were charged to the reactor. The reactor was held at about 160° C. for two hours and then cooled. Three subsequent batches were synthesized using the same raw materials and procedures. A total of four batches were made and blended together. When the resulting dispersant viscosity index improver was blended into a finished lubricating oil composition and tested in the Mack T-11 engine test, the amount of soot in the finished lubricating oil composition at an increase of 12 cSt was found to be 7.59 wt
  • Comparative Example A
  • An ethylene-propylene copolymer having 73.2 mole % ethylene, RaRb product of 1.06 and 23.6 regio-inversions per 1000 carbon atoms was grafted with MA under the following conditions: 96.8 wt % of polymer, 3.2 wt % of Crystalman® Maleic Anhydride (available from ExxonMobil Chemical Company) were fed at 7 kg/h feed rate to the hopper of the extruder and 2.44 wt % of a 10% solution of Luperox® 130 (di-tertiary butyl peroxide available from Atofina Chemical Incorporated:) dissolved in Marcol® 52 oil oil available from ESSO Petroleum Company Limited) were added to the second barrel. The screw speed was set at 250 rpm and following temperature profile was used: 160° C., 185° C., 205° C., 210° C. with the die at 160° C. The amount of MA grafted was 2.0 wt %. The maleated copolymer was dissolved in neutral oil to a concentration of 6%. 100 parts of the maleated copolyymer/oil mixture were charged to a stirred glass reactor and heated to about 160° C. 0.81 parts of an alcohol ethoxylate (Huntsman Surfonic® L24-7, a seven-mole ethoxylate of a linear, primary about 012 to about C14 alcohol) and 024 parts 1 0 of NPPDA (1 ::05 moles of NPPDA per mole of grafted MA) were first combined and then charged to the reactor. The reactor was held at about 160° C. for two hours and then cooled. Three subsequent batches were synthesized using the same raw materials and procedures. A total of four batches were made and blended together. The resulting dispersant viscosity It index improver was blended into a formulated lubricating oil composition to achieve a kinematic viscosity at about 100° C. equal to 114.5 cSt. The finished lubricating oil composition was then run in the Mack T-1 I engine test. The amount of soot present in the finished lubricating oil composition when the lubricating oil composition viscosity increased 12 cSt above the initial viscosity 20 was 6.32 wt.
  • Comparative Example B
  • The dispersant viscosity index improver of Comparative Example B was prepared and tested according; to Comparative Example A except that: the amine compound used was 4-phenoxyaniline (4-PA) instead of NPPDA. The amount of soot in the finished lubricating oil composition at an increase of 12 cSt was determined to be 5.42 wt % in the Mack T-12 engine test.
  • Comparative Example C
  • The maleated ethylene-propylene copolymer having 73.2 mole % ethylene of Comparative Example A was further grafted with MA in a second pass extrusion process under the following conditions: 98 wt % of polymer, 2 wt % of Crystalman® Maleic Anhydride (available from ExxoniMobil Chemical Company) were fed at 7 kg/h feed rate to the hopper of the extruder and 0.91 wt % of a 10% solution of Luperox® 130 (di-tertiary butyl peroxide available from Atofina Chemical Incorporated) dissolved in Marcol® 52 oil (mineral oil available from ESSO Petroleum Company Limited) were added to the second barrel. The screw speed was set at 250 rpm and following temperature profile was used: 160° C., 185° C., 205° C., 210° C. with the die at 145° C. A final grafting level of 2.6 wt % MA was achieved. The maleated: copolymer was dissolved in neutral oil to a concentration of 6 wt %. 100 parts of the maleated copolymer/oil mixture were charged to a stirred glass reactor and heated to about 160° C. 1.63 parts of an alcohol ethoxylate (Huntsman Surfonic® L24-7, a seven-mole ethoxylate of a linear, primary about C12 to about C14 alcohol) and 0.30 parts of NPPDA (1.05 moles of NPPDA per mole of grafted MA) were charged to the reactor. The reactor was held at about 160° C. for two hours and then cooled. The product was tested in the Mack T-11 engine test as described in the previous Examples. Upon completion of the test, the finished lubricating oil was found to contain 5.75 wt % soot when the finished lubricating oil composition viscosity increased 12 cSt above the initial viscosity.
  • Comparative Example D
  • A viscosity index improver having an ethylene-propylene copolymer with 68.4 mole % ethylene was prepared as specified in Example 1 except no amine was used and blended into a formulated lubricating oil composition to achieve a kinematic viscosity at about 100° C. equal to 14.5 cSt. This material is available commercially from Chevron Oronite Company, LLC. The finished lubricating oil composition was then run in the Mack T-11 engine test. The amount of soot present in the finished lubricating oil composition when the oil viscosity increased 12 cSt above the initial viscosity was 4.91 wt %.
  • The lubricating oil composition for each test is provided in Table 2 below.
  • TABLE 2
    Lubricating Oil Compositionsa
    Examples Comparative Examples
    1 2 3 A B C D
    Dispersant 7.5 8.0 8.5 8.5 8.5 8.5 7.5
    Viscosity
    Index
    Improver,
    wt %
    Kinematic 14.3 14.3 14.5 14.4 13.5 14.8 15.6
    viscosity
    at 100° C.
    (ASTM
    D445), cSt
    aThe wt % balance of the lubricating oil composition comprised Group I and Group II base oil, detergents, dispersants, wear inhibitors, antioxidants, friction modifiers, metal deactivators, foam inhibitors, and pour point depressants.
  • Results of the Mack T-11 engine tests are presented in Table 3 below.
  • TABLE 3
    Mack T-11 Engine Test Results
    Examples Comparative Examples
    1 2 3 A B C D
    Copolymer Ethylene Ethylene Ethylene Ethylene Ethylene Ethylene Ethylene
    Octene Octene Octene Propylene Propylene Propylene Propylene
    Mole % 86.7 86.7 86.7 73.2 73.2 73.2 68.4
    Ethylene
    Number- 56,000 56,000 56,000 43,000 43,000 43,000 80,000
    average
    Mol. Wt
    (Mn)
    Weight- 115,000 115,000 115,000 90,000 90,000 90,000 110,000
    average
    Mol. Wt
    (Mw)
    Grafting 2.8 2.8 3.2 2.0 2.0 2.6 0
    level, %
    MA
    Extruder 1 1 1 1 1 2 0
    passes to
    achieve
    grafting
    Amine NPPDA 4-PA NPPDA NPPDA 4-PA NPPDA 0
    Soot wt % 7.18 6.02 7.59 6.32 5.42 5.75 4.91
  • The results of this data indicate that the dispersant viscosity index improvers of the present invention having high ethylene content, wherein the alpha-monoolefin has a monomer distribution resulting from a RaRb product measured by 13C-NMR below 0.8 and a level of regio-inversions less than 2 per 1000 carbon atoms, provide superior soot dispersancy compared to lubricating oil compositions with viscosity index improvers having lower ethylene content.

Claims (63)

1. A polymeric composition comprising an ethylene-alpha olefin copolymer backbone comprising at least 82 mole % ethylene and at most 18 mole % of an about C3to about C28 alpha-monoolefin, wherein the alpha-monoolefin has a monomer distribution resulting from a RaRb product measured by 13C-NMR below 0.8 and a level of regio-inversions less than 2 per 1000 carbon atoms, and an amide group having the formula (I) and/or an imide group having the formula (II):
Figure US20070149414A1-20070628-C00030
wherein P is the ethylene-alpha olefin copolymer backbone, R1 is hydrogen or —CO—X′, R2 and R3 are independently hydrogen or —CH3, X and X′ are independently —OH, alkoxyl of 1 to about 24 carbon atoms, or a secondary or tertiary amine, provided that at least one of X and X′ is a secondary or tertiary amine, and Z is a tertiary amine, wherein Z and X and X′, when X and X′ are secondary or tertiary amines, are each independently derived from one or more of the following amines:
(a) an aromatic amine comprising two aromatic groups, linked by a group, L represented by the following formula:
Figure US20070149414A1-20070628-C00031
wherein L is selected from —O—, —N═N—, —NH—, —CH2NH—, —C(O)NR4—, —C(O)O—, —SO2—, —SO2NR5— or —SO2NH—; wherein R4 and R5 independently represent a hydrogen, an alkyl, an alkenyl or an alkoxyl group having from about 1 to about f8 carbon atoms;
wherein each Y1, Y2, Y3, and Y4 are independently N or CH provided that Y1 and Y2 may not both be N;
R6 and R7 independently represent a hydrogen, —OH, —NO2, —SO3H, —SO3Na, —CO2H or salt thereof —NH-aryl, —NH-alkyl, —NH-alkaryl, —NH-aralkyl having up to about 24 carbon atoms, or a branched or straight chain group having from about 4 to about 24 carbon atoms that can be alkyl, alkenyl, alkoxyl, aralkyl, alkaryl, hydroxyalkyl or aminoalkyl;
R8 and R9 independently represent a hydrogen, an alkyl an alkenyl or an alkoxyl group having about 1 to about 8 carbon atoms, —OH, —SO3H or —SO3Na; and
R10 represents —NH2, —NHR11, wherein R11 is an alkyl or an alkenyl group having from about 1 to about 8 carbon atoms, —CH2—(CH2)n—NH2 or —CH2-aryl-NH2 and n is from 0 to about 10;
(b) an aminothiazole selected from the group consisting of aminothiazole, aminobenzothiazole, aminobenzothiadiazole and aminoalkylthiazole;
(c) an aminocarbazole represented by the formula:
Figure US20070149414A1-20070628-C00032
wherein R12 and R13 independently represent a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
(d) an aminoindole represented by the formula:
Figure US20070149414A1-20070628-C00033
wherein R14 represents a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
(e) an aminopyrrole represented by the formula:
Figure US20070149414A1-20070628-C00034
wherein R15 represents a divalent alkylene group having about 2 to about 6 carbon atoms and R16 represents a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms,
(f) an amino-indazolinone represented by the formula:
Figure US20070149414A1-20070628-C00035
wherein R17 represents a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
(g) an aminomercaptotriazole represented by the formula:
Figure US20070149414A1-20070628-C00036
(h) an aminopyrimidine represented by the formula:
Figure US20070149414A1-20070628-C00037
wherein R18 represents a hydrogen, an alkyl, an alkenyl or an alkoxyl group having from about 1 to about 8 carbon atoms;
(i) a ring substituted or unsubstituted aniline;
(j) an aminoquinoline;
(k) an aminobenzimidazole;
(l) a N,N-dialkylphenylenediamine and
(m) a benzylamine.
2. The polymeric composition according to claim 1, further comprising a polyene selected from non-conjugated dienes and trienes.
3. The polymeric composition according to claim 1, wherein the ethylene-alpha copolymer comprises at least 84 mole % ethylene and at most 16 mole % of an about C3 to about C28 alpha-monoolefin.
4. The polymeric composition according to claim 3, wherein the alpha-monoolefin is an about C3 to about C20 alpha-monolefin.
5. The polymeric composition according to claim 4, wherein the alpha-monoolefin is an about C6 to about C12 alpha-monoolefin.
6. The polymeric composition according to claim 5, wherein the alpha-monoolefin is octene.
7. The polymeric composition according to claim 1, wherein the amine compound is an aromatic amine selected from the group consisting of
(a) an N-arylphenylenediamine represented by the formula:
Figure US20070149414A1-20070628-C00038
wherein R19 represents a hydrogen, —NH-aryl, —NH-alkyl, —NH-alkaryl, —NH-aralkyl having up to about 24 carbon atoms or a branched or straight chain having from about 4 to about 24 carbon atoms that can be alkyl, alkenyl, alkoxyl, aralkyl, alkaryl, hydroxyalkyl or aminoalkyl;
R20 represents —NH2 —CH2—(CH2)n—NH2, —CH2-aryl-NH2 and n is from about 1 to about 10; and
R21 represents a hydrogen, an alkyl, an alkenyl, an alkoxyl, an aralkyl or an alkaryl group having about 4 to about 24 carbon atoms; and
(b) a phenoxyaniline represented by the formula:
Figure US20070149414A1-20070628-C00039
wherein P22 represents a hydrogen, —NH-aryl, —NH-alkyl, —NH-alkaryl), —NH-aralkyl having up to about 24 carbon atoms or a branched or straight chain having from about 4 to about 24 carbon atoms that can be alkyl, alkenyl, alkoxyl, aralkyl, alkaryl, hydroxyalkyl or aminoalkyl;
R23 represents —NH2, —CH2—(CH2)n—NH2, —CH2-aryl-NH2 and n is from about 1 to about 10; and
R24 represents a hydrogen, an alkyl, an alkenyl, an alkoxyl, an aralkyl or an alkaryl group having about: 4 to about 24 carbon atoms.
8. The polymeric composition according to claim 7, wherein the N-arylphenylenediamine is N-phenylphenylenediamine.
9. The polymeric composition according to claim 8 wherein the N-phenylphenylenediamine is N-phenyl-1,4-phenylenediamine.
10. The polymeric composition according to claim 7, wherein the phenoxyanilines is 4-phenoxyaniline.
11. The polymeric compositions according to claim 1, further comprising an aliphatic amine having a single reactive amino group.
12. The polymeric composition according to claim 11, wherein the aliphatic amine having a single reactive amino group has from about 1 to about 8 carbon atoms.
13. The polymeric composition according to claim 12, wherein the aliphatic amine having a single reactive amino group is
N,N-dimethylaminopropylamine or aminopropylmorpholine.
14. An oil-soluble product prepared by the process comprising grafting an ethylene-alpha olefin copolymer backbone comprising at least 82 mole % ethylene and at most 18 mole % of an about C3 to about C28 alpha-monoolefin, wherein the alpha-monoolefin has a monomer distribution resulting from a RaRb product measured by 13C-NMR below 0.8 and a level of regio-inversions less than 2 per 1000 carbon atoms with an ethylenically unsaturated acylating agent and subsequently reacting the resulting grafted copolymer with one or more of the following amines;
(a) an aromatic amine comprising two aromatic groups, linked by a group, L represented by the following formula:
Figure US20070149414A1-20070628-C00040
wherein L is selected from —O—, —N═N—, —NH—, —CH2NH—, —C(O)NR4—,
—C(O)O—, —SO2—, —SO2NR5— or —SO2NH—; wherein R4 and R5 independently represent a hydrogen, an alkyl, an alkenyl or an alkoxyl group having from about 1 to about 8 carbon atoms;
wherein each Y1, Y2, Y3 and Y4 are independently N or CH, provided that Y1 and Y2 may not both be N;
R6 and R7 independently represent a hydrogen, —OH, —NO2, —SO3H, —SO3Na, —CO2H or salt thereof, —NH-aryl, —NH-alkyl, —NH-alkaryl, —NH-aralkyl having up to about 24 carbon atoms or a branched or straight chain group having from about 4 to about 24 carbon atoms that can be alkyl, alkenyl, alkoxyl, aralkyl, alkaryl, hydroxyalkyl or aminoalkyl;
R8 and R9 independently represent a hydrogen, an alkyl, an alkenyl or an alkoxyl group having from about 1 to about 8 carbon atoms, —OH, —SO3H or —SO3Na; and
R10 represents —NH2, —NHR11, wherein R11 is an alkyl or an alkenyl group having from about 1 to about 8 carbon atoms, —CH2—(CH2)n—NH2 or —CH2-aryl-NH2 and n is from 0 to about 10;
(b) an aminothiazole selected from the group consisting of aminothiazole, aminobenzothiazole, aminobenzothiadiazole and aminoalkylthiazole;
(c) an aminocarbazole represented by the formula:
Figure US20070149414A1-20070628-C00041
wherein R12 and R13 independently represent a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
(d) an aminoindole represented by the formula;
Figure US20070149414A1-20070628-C00042
wherein R14 represents a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
(e) an aminopyrrole represented by the formula:
Figure US20070149414A1-20070628-C00043
wherein R15 represents a divalent alkylene group having about 2 to about 6 carbon atoms and R16 represents a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
(f) an amino-indazolinone represented by the formula:
Figure US20070149414A1-20070628-C00044
wherein R17 represents a hydrogen an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
(g) an aminomercaptotriazole represented by the formula:
Figure US20070149414A1-20070628-C00045
(h) an aminopyrimidine represented by the formula:
Figure US20070149414A1-20070628-C00046
wherein R18 represents a hydrogen, an alkyl, an alkenyl or an alkoxyl group having from about 1 to about 8 carbon atoms;
(i) a ring substituted or unsubstituted aniline;
(j) an aminoquinoline;
(k) an aminobenzimidazole;
(l) a N,N-dialkylphenylenediamine and
(m) a benzylamine
to yield an oil-soluble product having an amide group with the formula (I) and/or an imide group having the formula (II)
Figure US20070149414A1-20070628-C00047
wherein P is the ethylene-alpha olefin copolymer backbone, R1 is hydrogen or —CO—X′, R2 and R3 are independently hydrogen or —CH3, X and X′ are independently —OH, alkoxyl of 1 to about 24 carbon atoms, or a secondary or tertiary amine, provided that at least one of X and X′ is a secondary or tertiary amine, and Z is a tertiary amine, wherein Z and X and X′, when X and X′ are secondary or tertiary amines, are each independently derived from one or more of the amines in (a)-(m) above.
15. The oil-soluble product prepared by the process according to claim 14, further comprising a polyene selected from non-conjugated dienes and trienes.
16. The oil-soluble product prepared by the process according to claim 14, wherein the ethylene-alpha copolymer comprises at least 84 mole % ethylene and at most 16 mole % of an about C3to about C28 alpha-monoolefin.
17. The oil-soluble product prepared by the process according to claim 16, wherein the alpha-monoolefin is an about C3 to about C20 alpha-monolefin.
18. The oil-soluble product prepared by the process according to claim 17, wherein the alpha-monoolefin is an about C6 to about C12 alpha-monoolefin.
19. The oil-soluble product prepared by the process according to claim 18, wherein the alpha-monoolefin is octene.
20. The oil-soluble product prepared by the process according to claim 14, wherein the ethylenically unsaturated acylating agent is maleic anhydride.
21. The oil-soluble product prepared by the process according to claim 14, wherein the amine is an aromatic amine selected from the group consisting of
(a) N-arylphenylenediamine represented by the formula:
Figure US20070149414A1-20070628-C00048
wherein R19 represents a hydrogen, —NH-aryl, —NH-alkyl, —NH-alkaryl, —NH-aralkyl having up to about 24 carbon atoms or a branched or straight chain having from about 4 to about 24 carbon atoms that can be alkyl, alkenyl, alkoxyl, aralkyl, alkaryl, hydroxyalkyl or aminoalkyl;
R20 represents —NH2, —CH2—(CH2)n—NH2, —CH2-aryl-NH2 and n is from about 1 to about 10;
and R21 represents a hydrogen, an alkyl an alkenyl, an alkoxyl, an aralkyl or an alkaryl group having about 4 to about 24 carbon atoms; and
(b) a phenoxyaniline represented by the formula:
Figure US20070149414A1-20070628-C00049
wherein R22 represents a hydrogen, —NH-aryl, —NH-alkyl, —NH-alkaryl, —NH-aralkyl having up to about 24 carbon atoms or a branched or straight chain having from about 4 to about 24 carbon atoms that can be alkyl, alkenyl, alkoxyl, aralkyl, alkaryl, hydroxyalkyl or aminoalkyl;
R23 represents —NH2, —CH2—(CH2)n—NH2, —CH2-aryl-NH2 and n is from about 1 to about 10; and
R24 represents a hydrogen, an alkyl an alkenyl, an alkoxyl, an aralkyl or an alkaryl group having about 4 to about 24 carbon atoms.
22. The oil-soluble product prepared by the process according to claim 21, wherein the N-arylphenylenediamine is N-phenylphenylenediamine.
23. The oil-soluble product prepared by the process according to claim 22, wherein the N-phenylphenylenediamine is N-phenyl-1,4-phenylenediamine.
24. The oil-soluble product prepared by the process according to claim 21 wherein the phenoxyaniline is 4-phenoxylaniline
25. The oil-soluble product prepared by the process according to claim 14, further comprising an aliphatic amine having a single reactive amino group.
26. The oil-soluble product prepared by the process according to claim 25, wherein the aliphatic amine having a single reactive amino group has from about 1 to about 8 carbon atoms.
27. The oil-soluble product prepared by the process according to claim 26, wherein the aliphatic amine having a single reactive amino group is N,N-dimethylaminopropylamine or aminopropylmorpholine.
28. A lubricating oil composition comprising a major amount of base oil of lubricating viscosity and a minor amount of a polymeric composition comprising an ethylene-alpha olefin copolymer backbone comprising at least 82 mole % ethylene and at most 18 mole % of an about C3 to about C28 alpha-monoolefin, wherein the alpha-monoolefin has a monomer distribution resulting from a RaRb product measured by 13C-NMR below 0.8 and a level of regio-inversions less than 2 per 1000 carbon atoms, and an amide group having the formula (I) and/or an imide group having the formula (II):
Figure US20070149414A1-20070628-C00050
wherein P is the ethylene-alpha olefin copolymer backbone, R1 is hydrogen or —CO—X′, R2 and R3 are independently hydrogen or —CH3, X and X′ are independently —OH, alkoxyl of 1 to about 24 carbon atoms, or a secondary or tertiary amine, provided that at least one of X and X′ is a secondary or tertiary amine, and Z is a tertiary amine, wherein Z and X and X′, when X and X′ are secondary or tertiary amines, are each independently derived from one or more of the following amines;
(a) an aromatic amine comprising two aromatic groups linked by a group, L represented by the following formula;
Figure US20070149414A1-20070628-C00051
wherein L is selected from —O—, —N═N—, —NH—, —OH2NH2—, —C(O)NR4—, —C(O)O—, —SO2—, —SO2NR5— or —SO2NH—; wherein R4 and R5 independently represent a hydrogen, an alkyl, an alkenyl or an alkoxyl group having from about 1 to about 8 carbon atoms;
wherein each Y1, Y2, Y3 and, Y4 are independently N or CH provided that Y1 and Y2 may not both be N;
R6 and R7 independently represent a hydrogen, —OH, —NO2, —SO3H, —SO3Na, —CO2H or salt thereof, —NH-aryl, —NH-alkyl, —NH-alkaryl, —NH-aralkyl having up to about 24 carbon atoms or a branched or straight chain group having from about 4 to about 24 carbon atoms that can be alkyl, alkenyl, alkoxyl, aralkyl, alkaryl, hydroxyalkyl or aminoalkyl;
R8 and R9 independently represent a hydrogen, an alkyl an alkenyl or an alkoxyl group having from about 1 to about 8 carbon atoms, —OH, —SO3 or, —SO3Na; and
R10 represents —NH2, —NHR , wherein R11 is an alkyl or an alkenyl group having from about 1 to about 8 carbon atoms, —CH2—(CH2)n—NH2or —CH2-aryl-NH2 and n is from 0 to about 10;
(b) an aminothiazole selected from the group consisting of aminothiazole, aminobenzothiazole, aminobenzothiadazole and aminoalkylthiazole,
(c) an aminocarbazole represented by the formula:
Figure US20070149414A1-20070628-C00052
wherein R12 and R13 independently represent a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
(d) an aminoindole represented by the formula:
Figure US20070149414A1-20070628-C00053
wherein R14 represents a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
(e) an aminopyrrole represented by the formula:
Figure US20070149414A1-20070628-C00054
wherein R15 represents a divalent alkylene group having about 2 to about 6 carbon atoms and R16 represents a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
(f) an amino-indazolinone represented by the formula:
Figure US20070149414A1-20070628-C00055
wherein R17 represents a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms:
(g) an aminomercaptotriazole: represented by the formula:
Figure US20070149414A1-20070628-C00056
(h) an aminopyrimidine represented by the formula:
Figure US20070149414A1-20070628-C00057
wherein R18 represents a hydrogen, an alkyl, an alkenyl or an alkoxyl group having from about 1 to about 8 carbon atoms;
(i) a ring substituted or unsubstituted aniline;
(j) an aminoquinoline;
(k) an aminobenzimidazole;
(l) a N,N.-dialkylphenylenediamine and
(m) a benzylamine.
29. The lubricating oil composition according to claim 28, further comprising a polyene selected from non-conjugated dienes and trienes.
30. The lubricating oil composition according to claim 28, wherein the ethylene-alpha copolymer comprises at least 84 mole % ethylene and at least 16 mole % of an about C3 to about C28alpha-monoolefin.
31. The lubricating oil composition according to claim 30, wherein the alpha-monoolefin is a about C6to about C20 alpha-monoolefin.
32. The lubricating oil composition according to claim 31, wherein the alpha-monoolefin is a about C6 to: about C12 alpha-monoolefin.
33. The lubricating oil composition according to claim 32, wherein the z:o alpha-monoolefin is octene.
34. The lubricating oil composition according to claim 28, wherein the amine is an aromatic amine selected from the group consisting of
(a) an N-arylphenylenediamine represented by the formula:
Figure US20070149414A1-20070628-C00058
wherein R19 represents a hydrogen, —NH-aryl, —NH-alkyl;, —NH-alkaryl, —NH-aralkyl having up to about 24 carbon atoms or a branched or straight chain having from about 4 to about 24 carbon atoms that can be alkyl, alkenyl, alkoxyl, aralkyl, alkaryl, hydroxyalkyl or aminoalkyl;
R20 represents —NH2, —CH2—(CH2)n—NH2, —CH2-aryl-NH2 and n is from about 1 to about 10; and
R21 represents a hydrogen, an alkyl an alkenyl, an alkoxy, an aralkyl or an alkaryl group having about 4 to about 24 carbon atoms; and
(b) a phenoxyaniline represented by the formula:
Figure US20070149414A1-20070628-C00059
wherein R22 represents a hydrogen, —NH-aryl, —NH-alkyl, —NH-alkaryl, —NH-aralkyl having up to about 24 carbon atoms or a branched or straight chain having from about 4 to about 24 carbon atoms that can be alkyl, alkenyl, alkoxyl, aralkyl, alkaryl, hydroxyalkyl or aminoalkyl;
R23 represents —NH2, —CH2—(CH2)n—NH2, —CH2-aryl-NH2 and n is from about 1 to about 10; and
R24 represents a hydrogen, an alkyl, an alkenyl, an alkoxyl, an aralkyl or an alkaryl group having about 4 to about 24 carbon atoms.
35. The lubricating oil composition according to claim 34, wherein the N-aryl phenylenediamine is N-phenylphenylenediamine
36. The lubricating oil composition according to claim 35, wherein the N-phenylphenylenediamine is N-phenyl-1,4-phenylenediamine.
37. The lubricating oil composition according to claim 34, wherein the phenoxyaniline is 4-phenoxylaniline.
38. The lubricating oil composition according to claim 28, further comprising an amine having a single reactive amine group.
39. The lubricating oil composition according to claim 38, wherein the aliphatic amine having a single reactive amino group has from about 1 to about 8 carbon atoms.
40. The lubricating oil compositions according to claim 39, wherein the aliphatic amine having a single reactive amino group is N,N-dimethylaminopropylamine or aminopropylmorpholine.
41. The lubricating oil composition according to claim 28, wherein the polymetric composition is from about 2 wt % to about 30 wt %, based on the total weight of the lubricating oil composition.
42. The lubricating oil composition according to claim 41, wherein the polymeric composition is from about 4 wt % to about 20 wt %, based on the total weight of the lubricating oil composition.
43. The lubricating oil composition according to claim 42, wherein the polymeric composition is from about 6 wt % to about 12 wt %, based on the total weight of the lubricating oil composition.
44. A lubricating oil composition comprising a major amount of base oil of lubricating viscosity and a minor amount of an oil-soluble product prepared by the process comprising grafting an ethylene-alpha olefin copolymer backbone comprising at least 82 mole % ethylene and at most 18 mole % of an about C3to about C28 alpha-monoolefin, wherein the alpha-monoolefin has a monomer distribution resulting from a RaRb product measured by 13C-NMR below 0.8 and a level of regio-inversions less than 2: per 1000 carbon atoms with an ethylenically unsaturated acylating agent and subsequently reacting the resulting grafted copolymer with one or more of the following amines:
(a) an aromatic amine comprising two aromatic groups linked by a group, L, represented by the following formula;
Figure US20070149414A1-20070628-C00060
wherein L is selected from —O—, —N═N—, —NH—, —CH2NH—, —C(O)NR4—, —C(O)O—, —SO2—, —SO2NR5— or —SO2NH—; wherein R4 and R5 independently represent a hydrogen, an alkyl, an alkenyl or an alkoxyl group having from about 1 to about 8 carbon atoms;
wherein each Y1, Y2 Y3 and Y4 are independently N or CH provided that Y1 and Y2 may not both be N;
R6 and R7 independently represent a hydrogen, —OH, —NO2, —SO3H, —SO3Na, —CO2H or salt thereof, —NH-aryl, —NH-alkyl, —NH-alkaryl, —NH-aralkyl having up to about 24 carbon atoms or a branched or straight chain group having from about 4 to about 24 carbon atoms that can be alkyl, alkenyl, alkoxyl, aralkyl, alkaryl, hydroxyalkyl or aminoalkyl;
R8 and R9 independently represent a hydrogen, an alkyl an alkenyl or an alkoxyl group having from about 1 to about 8 carbon atoms, —OH, —SO3H or —SO3Na; and
R10 represents —NH2, —NHR11, wherein R11 is an alkyl or an alkenyl group having from about 1 to about 8 carbon atoms, —CH2—(CH2)n—NH2 or —C2-aryl-NH2 and n is from 0 to about 10;
(b) an aminothiazole selected from the group consisting of aminothiazole, aminobenzothiazole, aminobenzothiadiazole and aminoalkylthiazole;
(c) an aminocarbazole represented by the formula:
Figure US20070149414A1-20070628-C00061
wherein R12 and R13 independently represent a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
(d) an aminoindole represented by the formula:
Figure US20070149414A1-20070628-C00062
wherein R14 represents a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
(e) an aminopyrrole represented by the formula:
Figure US20070149414A1-20070628-C00063
wherein R15 represents a divalent alkylene group having about 2 to about 6 carbon atoms and R16 represents a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
(f) an amino-indazolinone represented by the formula:
Figure US20070149414A1-20070628-C00064
wherein R17 represents a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
(g) an aminomercaptotriazole represented by the formula:
Figure US20070149414A1-20070628-C00065
(h) an aminopyrimidine represented by the formula:
Figure US20070149414A1-20070628-C00066
wherein R18 represents a hydrogen, an alkyl, an alkenyl or an alkoxyl group having from about 1 to about 8 carbon atoms;
(i) a ring substituted or unsubstituted aniline;
(j) an aminoquinoline;
(k) an aminobenzimidazole;
(l) a N,N-dialkylphenylenediamine and
(m) a benzylamine
to yield an oil-soluble product having an amide group with the formula (l) and/or an imide group having the formula (II):
Figure US20070149414A1-20070628-C00067
wherein P is the ethylene-alpha olefin copolymer backbone, R1 is hydrogen or —CO—X′, R2 and R3 are independently hydrogen or —CH3, X and X′ are independently —OH, alkoxyl of 1 to about 24 carbon atoms, or a secondary or tertiary amine, provided that at least one of X and X′ is a secondary or tertiary amine, and Z is a tertiary amine, wherein Z and X and X′, when X and X′ are secondary or tertiary amines, are each independently derived from one or more of the amines in (a)-(m) above.
45. The lubricating oil composition according to claim 44, further comprising a polyene selected from non-conjugated dienes and trienes.
46. The lubricating oil composition according to claim 44, wherein the ethylene-alpha copolymer comprises at least 83 mole % ethylene and at least 17 mole % of an about C3to about C28 alpha-monoolefin.
47. The lubricating oil composition according to claim 46, wherein the ethylene-alpha copolymer comprises at least 84 mole % ethylene and at least 16 mole % of an about C3 to about C28 alpha-monoolefin.
48. The lubricating oil composition according to claim 47, wherein the alpha-monoolefin is an about C3to about C20 alpha-monoolefin.
49. The lubricating oil composition according to claim 48, wherein the alpha-monoolefin is an about C6 to about C12 alpha-monoolefin.
50. The lubricating oil composition according to claim 49, wherein the alpha-monoolefin is octene.
51. The lubricating oil composition according to claim 44, wherein the ethylenically unsaturated acylating agent is maleic anhydride.
52. The lubricating oil composition according to claim 44, wherein the amine is an aromatic amine selected from the group consisting of:
(a) N-arylphenylenediamine represented by the formula:
Figure US20070149414A1-20070628-C00068
wherein R19 represents a hydrogen, —NH-aryl, —NH-alkyl, —NH-alkaryl, —NH-aralkyl having up to about 24 carbon atoms or a branched or straight chain having from about 4 to about 24 carbon atoms that can be alkyl, alkenyl, alkoxyl, aralkyl, alkaryl, hydroxyalkyl or aminoalkyl;
R20 represents —NH2, —CH2—(CH2)n—NH2, —CH2-aryl-NH2 and n is from about 1 to about 10; and
R21 represents a hydrogen, an alkyl, an alkenyl, an alkoxyl, an aralky or an alkaryl group having about 4 to about 24 carbon atoms; and
(b) a phenoxyaniline represented by the formula:
Figure US20070149414A1-20070628-C00069
wherein R22 represents a hydrogen, —NH-aryl, —NH-alkyl, —NH-alkaryl, —NH-aralkyl having up to about 24 carbon atoms or a branched or straight chain having from about 4 to about 24 carbon atoms that can be alkyl, alkenyl, alkoxyl, aralkyl, alkaryl, hydroxyalkyl or aminoalkyl;
R23 represents —NH2, —CH2—(CH2)n—NH2, —CH2-aryl-NH2 and n is from about 1 to about 10; and
R24 represents a hydrogen, an alkyl, an alkenyl an alkoxyl, an aralkyl or an alkaryl group having about 4 to about 24 carbon atoms.
53. The lubricating oil composition according to claim 52, wherein the N-arylphenylenediamine is N-phenylphenylenediamine.
54. The lubricating oil composition according to claim 53, wherein the N-phenylphenylenediamine is N-phenyl-1,4-phenylenediamine.
55. The lubricating oil composition according to claim 52, wherein the phenoxyaniline is 4-phenoxylaniline,
56. The lubricating oil composition according to claim 44, further comprising an aliphatic amine having a single reactive amino group.
57. The lubricating oil composition according to claim 56, wherein the aliphatic amine having a single reactive amino group has from about 1 to about 8 carbon atoms.
58. The lubricating oil composition according to claim 57, wherein the aliphatic amine having a single reactive amino group is N,N-dimethylaminiopropylamine or aminopropylmorpholine.
59. The lubricating oil composition according to claim 44, wherein the oil-soluble product prepared by the process is from about 2 wt % to about 30 wt %, based on the total weight of the lubricating oil composition.
60. The lubricating oil composition according to claim 59 wherein the oil-soluble product prepared by the process is from about 4 wt % to about 20 wt %, based on the total weight of the lubricating oil composition.
61. The lubricating oil composition according to claim 60, wherein the oil-soluble product prepared by the process is from about 6 wt % to about 12 wt %, based on the total weight of the lubricating oil composition.
62. A method of improving the soot and/or sludge dispersancy in an internal combustion engine, said method comprising operating said internal combustion engine with a lubricating oil composition comprising a major amount of base oil of lubricating viscosity and a minor amount of a polymeric composition comprising an ethylene-alpha olefin copolymer backbone comprising at least 82 mole % ethylene and at most 18 mole % of an about C3 to about C28 alpha-monoolefin, wherein the alpha-monoolefin has a monomer distribution resulting from a RaRb product measured by 13C-NMR below 0.8 and a level of regio-inversions less than 2 per 1000 carbon atoms, and an amide group having the formula (I) and/or an imide group having the formula (II):
Figure US20070149414A1-20070628-C00070
wherein P is the ethylene-alpha olefin copolymer backbone, R1 is hydrogen or —CO—X′, R2 and R3 are independently hydrogen or —CH3, X and X′ are independently —OH, alkoxyl of 1 to about 24 carbon atoms, or a secondary or tertiary amine, provided that at least one of X and X′ is a secondary or tertiary amine, and Z is a tertiary amine, wherein Z and X and X′, when X and X′ are secondary or tertiary amines, are each independently derived from one or more of the following amines:
(a) an aromatic amine comprising two aromatic groups, linked by a group L represented by the following formula,
Figure US20070149414A1-20070628-C00071
wherein L is selected from the group consisting of —O—, —N═N—, —NH—, —CH2NH—, —C(O)NR4—, —C(O)O—, —SO2—, —SO2NR3— or —SO2NH—; wherein R4 and R5 independently re-present a hydrogen, an alkyl, an alkenyl or an alkoxyl group having from about 1 to about 8 carbon atoms;
wherein each Y1 Y2 Y3 and Y4 are independently N or CH provided that Y1 and Y2 may not both be N;
R6 and R7 independently represent a hydrogen, —OH, —NO2, —SO3H, —SO3Na, —CO2H or salt thereof —NH-aryl, —NH-alkyl, —NH-alkaryl, —NH-aralkyl having up to about 24 carbon atoms or a branched or straight chain group having from about 4 to about 24 carbon atoms that can be alkyl, alkenyl, alkoxyl, aralkyl, alkaryl, hydroxyalkyl or aminoalkyl;
R8 and R9 independently represent a hydrogen, an alkyl, an alkenyl or an alkoxyl group having from about 1 to about 8 carbon atoms, —OH, —SO3H or —SO3Na; and
R10 represents —NH2, —NHR11 wherein R11 is an alkyl or an alkenyl group having from about 1 to about 8 carbon atoms, —CH2—(CH2)n—NH2 or —CH2-aryl-NH2 and n is from 0 to about 10;
(b) an aminothiazole selected from the group consisting of aminothiazole, aminobenzothiazole, aminobenzothiadiazole and aminoalkylthiazole;
(c) an aminocarbazole represented by the formula:
Figure US20070149414A1-20070628-C00072
wherein R12 and R13 represent a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
(d) an aminoindole represented by the formula:
Figure US20070149414A1-20070628-C00073
wherein R14 represents a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
(e) an aminopyrrole represented by the formula:
Figure US20070149414A1-20070628-C00074
wherein R15 represents a divalent alkylene group having about 2 to about 6 carbon atoms and R16 represents a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
(f) an amino-indazolinone represented by the formula:
Figure US20070149414A1-20070628-C00075
wherein R17 represents a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
(g) an aminomercaptotriazole represented by the formula:
Figure US20070149414A1-20070628-C00076
(h) an aminopyridine represented by the formula:
Figure US20070149414A1-20070628-C00077
wherein R18 represents a hydrogen, an alkyl, an alkenyl or an alkoxyl group having from about 1 to about 8 carbon atoms;
(i) a ring substituted or unsubstituted aniline;
(j) an aminoquinoline;
(k) an aminobenzimidazole;
(l) a N,N-dialkylphenylenediamine and
(m) a benzylamine
63. A method of improving the soot and/or sludge dispersancy in an internal combustion engine, said method comprising operating said internal combustion engine with a lubricating oil composition comprising a major amount of base oil of lubricating viscosity and a minor amount of an oil-soluble product produced by the process comprising grafting an ethylene-alpha olefin copolymer backbone comprising at least 82 mole % ethylene annd at most 138 mole % of an about: C3 to about C28 alpha-monoolefin, wherein the alpha-monoolefin has a monomer distribution resulting from a RaRb product measured by 13C-NMR below 0.8 and a level of regio-inversions less than 2 per 1000 carbon atoms with an ethylenically unsaturated acylating agent and subsequently reacting the resulting grafted copolymer with one or more of the following amines:
(a) an aromatic amine comprising two aromatic groups, linked by a group L represented by the following formulas:
Figure US20070149414A1-20070628-C00078
wherein L is selected from the group consisting of —O—, —N═N—, —NH—, —CH2NH—, —C(O)NR4, —C(O)O—, —SO2—, —SO2NR5— or —SO2NH—; wherein R4 and R5 independently represent a hydrogen, an alkyl an alkenyl or an alkoxyl group having from about 1 to about 8 carbon atoms;
wherein each Y1 Y2 Y3 and Y4 are independently N or CH provided that Y1 and Y2 may not both be N;
R6 and R7 independently represent a hydrogen, —OH, —NO2, —SO3H, —SO3Na, —CO2H or salt thereof —NH-aryl, —NH-alkyl, —NH-alkaryl, —NH-aralkyl having up to about 24 carbon atoms or a branched or straight chain group having from about 4 to about 24 carbon atoms that can be alkyl, alkenyl, alkoxyl, aralkyl, alkaryl, hydroxyalkyl or aminoalkyl;
R8 and R9 independently represent a hydrogen, an alkyl, an alkenyl or an alkoxyl group having from about 1 to about 8 carbon atoms, —OH, —SO3H or —SO3Na; and
R10 represents —NH2, —NHR11, wherein R11 is an alkyl or an alkenyl group having from about 1 to about 8 carbon atoms, —CH2—(CH2)n—NH2or —CH2-aryl-NH2and n is from 0 to about 10;
(b) an aminothiazole selected from the group consisting of aminothiazole, aminobenzothiazole, aminobenzothiadiazole and aminoalkylthiazole;
(c) an aminocarbazole represented by the formula,
Figure US20070149414A1-20070628-C00079
wherein R12 and R13 represent a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
(d) an aminoindole represented by the formula:
Figure US20070149414A1-20070628-C00080
wherein R14 represents a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
(e) an aminopyrrole represented by the formula:
Figure US20070149414A1-20070628-C00081
wherein R15 represents a divalent alkylene group having about 2 to about 6 carbon atoms and R16 represents a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
(f) an amino-indazolinone represented by the formula:
Figure US20070149414A1-20070628-C00082
wherein R17 represents a hydrogen, an alkyl or an alkenyl group having from about 1 to about 14 carbon atoms;
(g) an aminomercaptotriazole represented by the formula:
Figure US20070149414A1-20070628-C00083
(h) an aminopyrimidine represented by the formula:
Figure US20070149414A1-20070628-C00084
wherein R18 represents a hydrogen, an alkyl, an alkenyl, or an alkoxyl group having from about 1 to about 8 carbon atoms;
(i) a ring substituted or unsubstituted aniline;
(j) an aminoquinoline;
(k) an aminobenzimidazole;
(l) a N,N-dialkylphenylenediamine and
(m) a benzylamine
to yield an oil-soluble product having an amide group with the formula (I) and/or an imide group having the formula (II);
Figure US20070149414A1-20070628-C00085
wherein P is the ethylene-alpha olefin copolymer backbone, R1 is hydrogen or —CO—X′, R2 and R3 are independently hydrogen or —CH3, X and X′ are independently —OH, alkoxyl of 1 to about 24 carbon atoms, or a secondary or tertiary amine provided that at least one of X and X′ is a secondary or tertiary amine, and Z is a tertiary amine, wherein Z and X and X′, when X and X′ are secondary or tertiary amines, are each independently derived from one or more of the amines in (a)-(m) above.
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US20060205611A1 (en) * 2005-03-11 2006-09-14 Sauer Richard P Multiple function graft polymer
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US9624451B2 (en) 2013-03-15 2017-04-18 Castrol Limited Multiple function dispersant viscosity index improver
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