EP2083063A1 - Composition d'huile lubrifiante - Google Patents

Composition d'huile lubrifiante Download PDF

Info

Publication number
EP2083063A1
EP2083063A1 EP09150505A EP09150505A EP2083063A1 EP 2083063 A1 EP2083063 A1 EP 2083063A1 EP 09150505 A EP09150505 A EP 09150505A EP 09150505 A EP09150505 A EP 09150505A EP 2083063 A1 EP2083063 A1 EP 2083063A1
Authority
EP
European Patent Office
Prior art keywords
mass
lubricating oil
oil composition
group
viscosity
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP09150505A
Other languages
German (de)
English (en)
Other versions
EP2083063B1 (fr
Inventor
Nancy Infineum USA L.P. Diggs
Thomas Joseph Infineum USA L.P. Mulrane
Robert Raymond Infineum USA L.P. Salgueiro
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Infineum International Ltd
Original Assignee
Infineum International Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Infineum International Ltd filed Critical Infineum International Ltd
Publication of EP2083063A1 publication Critical patent/EP2083063A1/fr
Application granted granted Critical
Publication of EP2083063B1 publication Critical patent/EP2083063B1/fr
Not-in-force legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M167/00—Lubricating compositions characterised by the additive being a mixture of a macromolecular compound, a non-macromolecular compound and a compound of unknown or incompletely defined constitution, each of these compounds being essential
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2203/00—Organic non-macromolecular hydrocarbon compounds and hydrocarbon fractions as ingredients in lubricant compositions
    • C10M2203/10—Petroleum or coal fractions, e.g. tars, solvents, bitumen
    • C10M2203/102—Aliphatic fractions
    • C10M2203/1025—Aliphatic fractions used as base material
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2205/00—Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions
    • C10M2205/02—Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions containing acyclic monomers
    • C10M2205/026—Butene
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00—Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/02—Hydroxy compounds
    • C10M2207/023—Hydroxy compounds having hydroxy groups bound to carbon atoms of six-membered aromatic rings
    • C10M2207/028—Overbased salts thereof
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2219/00—Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions
    • C10M2219/04—Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions containing sulfur-to-oxygen bonds, i.e. sulfones, sulfoxides
    • C10M2219/046—Overbased sulfonic acid salts
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2219/00—Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions
    • C10M2219/06—Thio-acids; Thiocyanates; Derivatives thereof
    • C10M2219/062—Thio-acids; Thiocyanates; Derivatives thereof having carbon-to-sulfur double bonds
    • C10M2219/066—Thiocarbamic type compounds
    • C10M2219/068—Thiocarbamate metal salts
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2223/00—Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions
    • C10M2223/02—Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions having no phosphorus-to-carbon bonds
    • C10M2223/04—Phosphate esters
    • C10M2223/045—Metal containing thio derivatives
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2010/00—Metal present as such or in compounds
    • C10N2010/04—Groups 2 or 12
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2020/00—Specified physical or chemical properties or characteristics, i.e. function, of component of lubricating compositions
    • C10N2020/01—Physico-chemical properties
    • C10N2020/04—Molecular weight; Molecular weight distribution
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/06—Oiliness; Film-strength; Anti-wear; Resistance to extreme pressure
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/40—Low content or no content compositions
    • C10N2030/42—Phosphor free or low phosphor content compositions
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/40—Low content or no content compositions
    • C10N2030/43—Sulfur free or low sulfur content compositions
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/40—Low content or no content compositions
    • C10N2030/44—Boron free or low content boron compositions
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/40—Low content or no content compositions
    • C10N2030/45—Ash-less or low ash content
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/52—Base number [TBN]
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2040/00—Specified use or application for which the lubricating composition is intended
    • C10N2040/25—Internal-combustion engines
    • C10N2040/252—Diesel engines
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2060/00—Chemical after-treatment of the constituents of the lubricating composition
    • C10N2060/14—Chemical after-treatment of the constituents of the lubricating composition by boron or a compound containing boron

Definitions

  • the present invention relates to SAE 0W and SAE 5W multigrade crankcase lubricants for heavy duty diesel (HDD) engines that have less than 50 mass % of Group IV and Group V base stock, containing phosphorus-based antiwear agents in an amount introducing no greater than 1200 ppm of phosphorus into the lubricant, which lubricants meet the wear performance requirements of API CJ-4, API CI-4 and/or ACEA E7 specifications.
  • HDD heavy duty diesel
  • Crankcase lubricants comprise base stock and additives that delay degradation of the base stock and improve its performance.
  • additives typically include dispersant, overbased and neutral salts of organic acids, corrosion inhibitors, antiwear agents, antioxidants, friction modifiers, antifoamants, and demulsifiers.
  • These additives may be combined in a package, sometimes referred to as a detergent inhibitor (or DI) package.
  • the additives in such a package may include functionalized polymers, but these have relatively short chains, typically having a number average molecular weight M n of not more than 7000.
  • Multigrade lubricants perform over wide temperature ranges. Typically, they are identified by two numbers such as 10W-30 or 5W-30. The first number in the multigrade designation is associated with a safe cranking temperature (e.g., -20° C) viscosity requirement for that multigrade oil as measured by a cold cranking simulator (CCS) under high shear rates (ASTM D5293).
  • a safe cranking temperature e.g., -20° C
  • CCS cold cranking simulator
  • ASTM D5293 high shear rates
  • lubricants that have low CCS viscosities allow the engine to crank more easily at lower temperatures and thus improve engine startability at those ambient temperatures.
  • the second number in the multigrade designation is associated with a lubricant's viscosity under normal operating temperatures and is measured in terms of the kinematic viscosity (kV) at 100°C (ASTM D445).
  • the high temperature viscosity requirement brackets minimum and maximum kinematic viscosity at 100°C. Viscosity at high temperatures is desirable to prevent engine wear that would result if the lubricant thinned out too much during engine operation. However the lubricant should not be too viscous because excessive viscosity may cause unnecessary viscous drag and work to pump the lubricant which in turn can increase fuel consumption. In general, the lower a lubricants' kV 100°C, the better the scores that lubricant achieves in fuel economy tests.
  • SAE J300 The current viscosity limits set in SAE J300 are as follows: SAE VISCOSITY GRADES SAE viscosity grade Maximum CCS Viscosity (10 -3 Pa.s @ (°C)) kV 100°C (mm 2 /s) minimum kV 100°C (mm 2 /s) maximum 0W 3250 (-30) 3.8 5W 3500 (-25) 3.8 - 10W 3500 (-20) 4.1 - 15W 3500 (-15) 5.6 - 20W 4500 (-10) 5.6 - 25W 6000 (-5) 9.3 - 20 - 5.6 ⁇ 9.3 30 - 9.3 ⁇ 12.5 40 - 12.5 ⁇ 16.3 50 - 16.3 ⁇ 21.9 60 - 21.9 ⁇ 26.1
  • an SAE 5W-30 multigrade oil has viscosity characteristics that satisfy both the 5W and the 30 viscosity grade requirements -- i.e., a maximum CCS viscosity of 3500 ⁇ 10 -3 Pa.s at - 25°C, a minimum kV 100°C of 9.3 mm 2 /s and a maximum kV 100°C of ⁇ 12.5 mm 2 /s.
  • the viscosity characteristics of a lubricant depend primarily on the viscosity characteristics of the base stock and on the viscosity characteristics of the viscosity modifier. Of the other additives often found in lubricants only high molecular weight dispersants have been thought to influence viscometrics, and their influence has been deemed small in comparison to base stock and viscosity modifier.
  • the viscosity characteristic of a base stock on which a lubricating oil is based is typically expressed by the neutral number of the oil (e.g., S150N) with a higher neutral number being associated with a higher viscosity at a given temperature. This number is defined as the viscosity of the base stock at 40°C measured in Saybolt Universal Seconds. Blending base stocks is one way of modifying the viscosity properties of the resulting lubricating oil. For example a lubricant formulated entirely with S100N will have both a lower kV 100 and a lower CCS than a lubricant formulated entirely with a S 150N base stock.
  • a base stock comprised of a blend of S100N and S150N will have a CCS in between those of the straight cuts.
  • a particularly effective class of antioxidant-antiwear additives available to lubricant formulators is metal salts of dialkyldithiophosphates, particularly zinc salts thereof, commonly referred to as ZDDP. While such additives provide excellent performance, ZDDP contributes each of sulfated ash, phosphorus and sulfur to lubricants.
  • lubricant manufacturers have formulated fully synthetic, lubricants and lubricants containing significant proportions of synthetic base stocks defined as Group IV base stocks (polyalphaolefin or PAO base stocks) and/ or Group V base stocks, such as ester base stocks.
  • Group IV base stocks polyalphaolefin or PAO base stocks
  • Group V base stocks such as ester base stocks.
  • Group IV and Group V base stocks have a high viscosity index (VI), which means that the kinematic viscosity of the base stock varies less with temperature.
  • a lubricant can be provided having a low CCS viscosity and high kV100.
  • Group IV and Group V base stocks are expensive relative to Group I, Group II and Group III mineral oil base stocks.
  • SAE 0W and SAE 5W multigrade crankcase lubricants for heavy duty diesel (HDD) engines having less than 30 mass %, of Group IV and/or Group V base stock, and phosphorus-based antiwear agents in amounts introducing no greater than 1200 ppm of phosphorus into the lubricant can meet the performance requirements, including the wear performance requirements of the API CJ-4; API CI-4; and/or ACEA E7 specifications when formulated with a minor amount of a non-hydrogenated olefin polymer and at least 40 ppm of boron.
  • a SAE 0W and SAE 5W multigrade crankcase lubricating oil composition for heavy duty diesel (HDD) engines meeting the performance requirements of at least one of the API CJ-4; API CI-4; and/or ACEA E7 specifications, having a sulfated ash content of no greater than 1.0 mass %, such as from about 0.7 to 1.0 mass %, a sulfur content of no greater than 0.4 mass %, and a phosphorus content of no greater than 0.12 mass % (1200 ppm), such as from about 0.08 to 0.12 mass %; which lubricating oil composition comprises a major amount of oil of lubricating viscosity including less than about 30 mass %, preferably less than 10 mass %, based on the total mass of oil of lubricating viscosity, of Group IV and/or Group V base stock, at least 0.3 mass %, such as 0.3 to 5 mass %, of a non-hydrogenated
  • a lubricating oil composition as described in the first aspect, having a TBN of from about 7 to about 15,
  • a lubricating oil composition as described in the first or second aspect, comprising a magnesium detergent in an amount providing said composition with at least 0.09 mass % (900 ppm), preferably at least 0.10 mass % (1000 ppm), more preferably at least 0.115 mass % (1150 ppm) of magnesium.
  • a lubricating oil composition as described in the first, second or third aspect, further comprising a nitrogen-containing dispersant in an amount providing the lubricating oil composition with at least 0.08 mass% of nitrogen.
  • a lubricating oil composition comprising at least 0.5 mass %, such as at least 0.6 mass %, preferably at least 0.8 mass%, more preferably at least 1.0 mass % of at least one ashless antioxidant selected from sulfur-free hindered phenol antioxidants, aminic antioxidants, and combinations thereof.
  • a heavy duty diesel (HDD) engine lubricated with a lubricating oil composition as described in any of the first through fifth aspects.
  • a method for improving the fuel economy and wear performance of a heavy duty diesel (HDD) engine comprises the steps of lubricating the engine with a lubricating oil composition as described in any of the first through fifth aspects, and operating the lubricated engine.
  • HDD heavy duty diesel
  • a lubricating oil composition as described in any of the first through fifth aspects to improve the fuel economy and wear performance of a heavy duty diesel (HDD) engine.
  • HDD heavy duty diesel
  • the oil of lubricating viscosity useful in the practice of the invention may range in viscosity from about 2 mm 2 /sec (centistokes) to about 40 mm 2 /sec, especially from about 3 mm 2 /sec to about 20 mm 2 /sec, most preferably from about 9 mm 2 /sec to about 17 mm 2 /sec, measured at 100°C.
  • Natural oils include animal oils and vegetable oils (e.g., castor oil, lard oil); liquid petroleum oils and hydrorefined, solvent-treated or acid-treated mineral oils of the paraffinic, naphthenic and mixed paraffinic-naphthenic types. Oils of lubricating viscosity derived from coal or shale also serve as useful base oils.
  • Synthetic lubricating oils include hydrocarbon oils and halo-substituted hydrocarbon oils such as polymerized and interpolymerized olefins (e.g., polybutylenes, polypropylenes, propylene-isobutylene copolymers, chlorinated polybutylenes, poly(1-hexenes), poly(1-octenes), poly(1-decenes)); alkylbenzenes (e.g., dodecylbenzenes, tetradecylbenzenes, dinonylbenzenes, di(2-ethylhexyl)benzenes); polyphenyls (e.g., biphenyls, terphenyls, alkylated polyphenols); and alkylated diphenyl ethers and alkylated diphenyl sulfides and derivative, analogs and homologs thereof.
  • Alkylene oxide polymers and interpolymers and derivatives thereof where the terminal hydroxyl groups have been modified by esterification, etherification, etc. constitute another class of known synthetic lubricating oils. These are exemplified by polyoxyalkylene polymers prepared by polymerization of ethylene oxide or propylene oxide, and the alkyl and aryl ethers of polyoxyalkylene polymers (e.g., methyl-polyiso-propylene glycol ether having a molecular weight of 1000 or diphenyl ether of poly-ethylene glycol having a molecular weight of 1000 to 1500); and mono- and polycarboxylic esters thereof, for example, the acetic acid esters, mixed C 3 -C 8 fatty acid esters and C 13 Oxo acid diester of tetraethylene glycol.
  • polyoxyalkylene polymers prepared by polymerization of ethylene oxide or propylene oxide
  • alkyl and aryl ethers of polyoxyalkylene polymers e.g.
  • Another suitable class of synthetic lubricating oils comprises the esters of dicarboxylic acids (e.g., phthalic acid, succinic acid, alkyl succinic acids and alkenyl succinic acids, maleic acid, azelaic acid, suberic acid, sebasic acid, fumaric acid, adipic acid, linoleic acid dimer, malonic acid, alkylmalonic acids, alkenyl malonic acids) with a variety of alcohols (e.g., butyl alcohol, hexyl alcohol, dodecyl alcohol, 2-ethylhexyl alcohol, ethylene glycol, diethylene glycol monoether, propylene glycol).
  • dicarboxylic acids e.g., phthalic acid, succinic acid, alkyl succinic acids and alkenyl succinic acids, maleic acid, azelaic acid, suberic acid, sebasic acid, fumaric acid, adipic acid, linole
  • esters includes dibutyl adipate, di(2-ethylhexyl) sebacate, di-n-hexyl fumarate, dioctyl sebacate, diisooctyl azelate, diisodecyl azelate, dioctyl phthalate, didecyl phthalate, dieicosyl sebacate, the 2-ethylhexyl diester of linoleic acid dimer, and the complex ester formed by reacting one mole of sebacic acid with two moles of tetraethylene glycol and two moles of 2-ethylhexanoic acid.
  • Esters useful as synthetic oils also include those made from C 5 to C 12 monocarboxylic acids and polyols and polyol esters such as neopentyl glycol, trimethylolpropane, pentaerythritol, dipentaerythritol and tripentaerythritol.
  • Silicon-based oils such as the polyalkyl-, polyaryl-, polyalkoxy- or polyaryloxysilicone oils and silicate oils comprise another useful class of synthetic lubricants; such oils include tetraethyl silicate, tetraisopropyl silicate, tetra-(2-ethylhexyl)silicate, tetra-(4-methyl-2-ethylhexyl)silicate, tetra-(p-tert-butyl-phenyl) silicate, hexa-(4-methyl-2-ethylhexyl)disiloxane, poly(methyl)siloxanes and poly(methylphenyl)siloxanes.
  • oils include tetraethyl silicate, tetraisopropyl silicate, tetra-(2-ethylhexyl)silicate, tetra-(4-methyl-2-ethylhexy
  • Other synthetic lubricating oils include liquid esters of phosphorous-containing acids (e.g., tricresyl phosphate, trioctyl phosphate, diethyl ester of decylphosphonic acid) and polymeric tetrahydrofurans.
  • base oil examples include gas-to-liquid (“GTL”) base oils, i.e. the base oil may be oil derived from Fischer-Tropsch-synthesized hydrocarbons made from synthesis gas containing hydrogen and carbon monoxide using a Fischer-Tropsch catalyst. These hydrocarbons typically require further processing in order to be useful as base oil. For example, they may, by methods known in the art, be hydroisomerized; hydrocracked and hydroisomerized; dewaxed; or hydroisomerized and dewaxed.
  • GTL gas-to-liquid
  • base stocks and base oils in this invention are the same as those found in the American Petroleum Institute (API) publication "Engine Oil Licensing and Certification System", Industry Services Department, Fourteenth Edition, December 1996, Addendum 1, December 1998. Said publication categorizes base stocks as follows:
  • Oil of lubricating viscosity useful in the practice of the present invention may comprise a Group I, Group II, Group III, base stocks or base oil blends of the aforementioned base stocks.
  • the oil of lubricating viscosity may also comprise a base oil blend of one or more Group I, Group II, and/or Group III, base stocks and less than 30 mass %, based on the total mass of oil of lubricating viscosity, of one or more Group IV and/or Group V base stocks.
  • the oil of lubricating viscosity is mixture of one or more Group II and/or Group III base stock and an amount of less than 30 mass %, preferably less than 10 mass %, based on the total mass % of oil of lubricating viscosity, of one or more Group IV or Group V base stocks.
  • Particularly preferred are Group III base stocks and base stock blends, and blends of one or more Group III base stocks and 0 to 10 mass %, based on the total mass of oil of lubricating viscosity, of one or more Group IV base stocks.
  • the base stock, or base stock blend preferably has a saturate content of at least 65%, more preferably at least 75%, such as at least 85%.
  • the base stock, or base stock blend has a saturate content of greater than 90%.
  • the oil or oil blend will have a sulfur content of less than 1 mass %, preferably less than 0.6 mass %, most preferably less than 0.4 mass %, such as less than 0.3 mass %.
  • the volatility of the base stock or base stock blend is less than or equal to 30 mass %, such as less than about 25 mass%, preferably less than or equal to 20 mass %, more preferably less than or equal to 15 mass %, most preferably less than or equal 13 mass %.
  • the viscosity index (VI) of the base stock or base stock blend is at least 85, preferably at least 100, most preferably from about 105 to 140.
  • a certain amount of oil of lubricating viscosity may be introduced into the lubricating oil composition as a diluent for the various additives and are commonly Group I base stocks.
  • the preferred mass percentages, saturates contents, Noack and VI described above are for the base stock or base stock blends used to formulate the lubricating oil composition, excluding any oil that may be introduced as an additive diluent.
  • the non-hydrogenated olefin (co)polymer useful in the practice of the present invention is preferably a polymer or copolymer of one or more acyclic olefin monomers.
  • the non-hydrogenated olefin (co)polymers useful in the invention have, or have on average, about one double bond per polymer chain.
  • the (co)polymer may be prepared by polymerizing alpha-olefin monomer, or mixtures of alpha-olefin monomers, or mixtures comprising ethylene and at least one C 3 to C 28 alpha-olefin monomer, in the presence of a catalyst system comprising at least one metallocene (e.g., a cyclopentadienyl-transition metal compound) and an alumoxane compound.
  • a catalyst system comprising at least one metallocene (e.g., a cyclopentadienyl-transition metal compound) and an alumoxane compound.
  • the percentage of polymer chains exhibiting terminal ethenylidene unsaturation may be determined by FTIR spectroscopic analysis, titration, or C 13 NMR.
  • the chain length of the R 1 alkyl group will vary depending on the comonomer(s) selected for use in the polymerization.
  • These terminally unsaturated interpolymers may be prepared by known metallocene chemistry and may also be prepared as described in U.S. Patent Nos. 5,498,809 ; 5,663,130 ; 5,705,577 ; 5,814,715 ; 6,022,929 and 6,030,930 .
  • (co)polymers prepared by cationic polymerization of isobutene, styrene, and the like.
  • Common (co)polymers from this class include polyisobutenes obtained by polymerization of a C 4 refinery stream having a butene content of about 35 to about 75 mass %., and an isobutene content of about 30 to about 60% by wt., in the presence of a Lewis acid catalyst, such as aluminum trichloride or boron trifluoride, with aluminium trichloride preferred.
  • a preferred source of monomer for making poly-n-butenes is petroleum feedstreams such as Raffinate II.
  • Polyisobutylene is a most preferred polymer of the present invention because it is readily available by cationic polymerization from butene streams ( e . g ., using AlCl 3 or BF 3 catalysts). Such polyisobutylenes generally contain residual unsaturation in amounts of about one ethylenic double bond per polymer chain, positioned along the chain.
  • a preferred embodiment utilizes polyisobutylene prepared from a pure isobutylene stream or a Raffinate I stream to prepare reactive isobutylene polymers with terminal vinylidene olefins.
  • these polymers referred to as highly reactive polyisobutylene (HR-PIB)
  • HR-PIB highly reactive polyisobutylene
  • these polymers have a terminal vinylidene content of at least 65%, e . g ., 70%, more preferably at least 80%, most preferably, at least 85%.
  • the preparation of such polymers is described, for example, in U.S. Patent No. 4,152,499 .
  • HR-PIB is known and is commercially available, for example, under the tradenames Glissopal TM (from BASF) and Ultravis TM (from BP-Amoco).
  • the non-hydrogenated olefin (co)polymer for example, polyisobutylene
  • polyisobutylene has at most 10, such as 5 to 10, %, of the polymer chains possessing a terminal double bond (or terminal ethenylidene-type or terminal vinylidene unsaturation).
  • Such a polymer is considered not highly reactive; an example of a commercially available polymer is under tradename Napvis TM (from BP-Amoco), and usually obtained by polymerization with aluminium trichloride as catalyst.
  • the (co)polymer is derived from polymerisation of one or more olefins having 2 to 10, such as 3 to 8, carbon atoms.
  • olefins having 2 to 10, such as 3 to 8, carbon atoms.
  • An especially preferred olefin is butene, advantageously isobutene.
  • the number average molecular weight of the non-hydrogenated olefin (co)polymer useful in the present invention is preferably in the range of from about 450 to about 2300, such as from about 450 to about 1300, preferably from about 450 to about 950.
  • the molecular weight can be determined by several known techniques. A convenient method for such determination is by gel permeation chromatography (GPC), which additionally provides molecular weight distribution information (see W.W. Yau, J.J Kirkland and D.D Bly, "Modern Size Exclusion Liquid Chromatography", John Wiley and Sons, New York, 1979 ).
  • the kinematic viscosity of the non-hydrogenated olefin polymer at 100°C, as measured according to ASTM D445, is at least 9 or 15, such as 100 or 150 to 3000, advantageously 200 to 2500 or 2700 mm 2 s -1 .
  • a polyisobutylene polymer having a number average molecular weight of 450 to 2300, and a kinematic viscosity at 100°C of from about 200 to 2400 mm 2 s -1 was found to provide particularly beneficial properties.
  • Lubricating oil compositions of the present invention can contain the non-hydrogenated olefin polymer in an amount of at least 0.3 mass %, such as from about 0.3 to about 5.0 mass %, particularly from about 0.5 to about 3.0 mass %, preferably from about 1.0 to about 2.5 mass %.
  • lubricating oil compositions of the present invention contain less than about 35 mass %, preferably less than about 15 mass %, based on the combined total mass of oil of lubricating viscosity and non-hydrogenated olefin polymer, of a combination of Group IV and/or Group V base stock and non-hydrogenated olefin polymer.
  • Lubricating oil compositions of the present invention contain greater than about 40 ppm, such as 40 to 600 ppm, preferably from about 50 to 200 ppm, more preferably from about 50 to 100 ppm of boron.
  • the boron can be introduced into the lubricating oil composition by a borated dispersant, a borated detergent, or other boron-containing additive, or a mixture thereof, or by addition of elemental boron or other boron compound.
  • Metal-containing or ash-forming detergents function as both detergents to reduce or remove deposits and as acid neutralizers or rust inhibitors, thereby reducing wear and corrosion and extending engine life.
  • Detergents generally comprise a polar head with a long hydrophobic tail.
  • the polar head comprises a metal salt of an acidic organic compound.
  • the salts may contain a substantially stoichiometric amount of the metal in which case they are usually described as normal or neutral salts, and have a total base number or TBN (as can be measured by ASTM D2896) of from 0 to less than 150, such as 0 to about 80 or 100.
  • a large amount of a metal base may be incorporated by reacting excess metal compound (e.g., an oxide or hydroxide) with an acidic gas (e.g., carbon dioxide).
  • the resulting overbased detergent comprises neutralized detergent as the outer layer of a metal base (e.g. carbonate) micelle.
  • Such overbased detergents have a TBN of 150 or greater, and typically will have a TBN of from 250 to 450 or more.
  • Detergents that may be used include oil-soluble neutral and overbased sulfonates, phenates, sulfurized phenates, thiophosphonates, salicylates, and naphthenates and other oil-soluble carboxylates of a metal, particularly the alkali or alkaline earth metals, e.g., barium, sodium, potassium, lithium, calcium, and magnesium.
  • a metal particularly the alkali or alkaline earth metals, e.g., barium, sodium, potassium, lithium, calcium, and magnesium.
  • the most commonly used metals are calcium and magnesium, which may both be present in detergents used in a lubricant, and mixtures of calcium and/or magnesium with sodium. Combinations of detergents, whether overbased or neutral or both, may be used.
  • Sulfonates may be prepared from sulfonic acids which are typically obtained by the sulfonation of alkyl substituted aromatic hydrocarbons such as those obtained from the fractionation of petroleum or by the alkylation of aromatic hydrocarbons. Examples included those obtained by alkylating benzene, toluene, xylene, naphthalene, diphenyl or their halogen derivatives such as chlorobenzene, chlorotoluene and chloronaphthalene.
  • the alkylation may be carried out in the presence of a catalyst with alkylating agents having from about 3 to more than 70 carbon atoms.
  • the alkaryl sulfonates usually contain from about 9 to about 80 or more carbon atoms, preferably from about 16 to about 60 carbon atoms per alkyl substituted aromatic moiety.
  • the oil soluble sulfonates or alkaryl sulfonic acids may be neutralized with oxides, hydroxides, alkoxides, carbonates, carboxylate, sulfides, hydrosulfides, nitrates, borates and ethers of the metal.
  • the amount of metal compound is chosen having regard to the desired TBN of the final product but typically ranges from about 100 to 220 mass % (preferably at least 125 mass %) of that stoichiometrically required.
  • Metal salts of phenols and sulfurized phenols are prepared by reaction with an appropriate metal compound such as an oxide or hydroxide and neutral or overbased products may be obtained by methods well known in the art.
  • Sulfurized phenols may be prepared by reacting a phenol with sulfur or a sulfur containing compound such as hydrogen sulfide, sulfur monohalide or sulfur dihalide, to form products which are generally mixtures of compounds in which 2 or more phenols are bridged by sulfur containing bridges.
  • Carboxylate detergents e.g., salicylates
  • an aromatic carboxylic acid can contain hetero atoms, such as nitrogen and oxygen.
  • the moiety contains only carbon atoms; more preferably the moiety contains six or more carbon atoms; for example benzene is a preferred moiety.
  • the aromatic carboxylic acid may contain one or more aromatic moieties, such as one or more benzene rings, either fused or connected via alkylene bridges.
  • the carboxylic moiety may be attached directly or indirectly to the aromatic moiety.
  • the carboxylic acid group is attached directly to a carbon atom on the aromatic moiety, such as a carbon atom on the benzene ring. More preferably, the aromatic moiety also contains a second functional group, such as a hydroxy group or a sulfonate group, which can be attached directly or indirectly to a carbon atom on the aromatic moiety.
  • a second functional group such as a hydroxy group or a sulfonate group
  • aromatic carboxylic acids are salicylic acids and sulfurized derivatives thereof, such as hydrocarbyl substituted salicylic acid and derivatives thereof.
  • Processes for sulfurizing, for example a hydrocarbyl - substituted salicylic acid are known to those skilled in the art.
  • Salicylic acids are typically prepared by carboxylation, for example, by the Kolbe - Schmitt process, of phenoxides, and in that case, will generally be obtained, normally in a diluent, in admixture with uncarboxylated phenol.
  • Preferred substituents in oil - soluble salicylic acids are alkyl substituents.
  • the alkyl groups advantageously contain 5 to 100, preferably 9 to 30, especially 14 to 20, carbon atoms. Where there is more than one alkyl group, the average number of carbon atoms in all of the alkyl groups is preferably at least 9 to ensure adequate oil solubility.
  • Detergents generally useful in the formulation of lubricating oil compositions also include "hybrid" detergents formed with mixed surfactant systems, e.g., phenate/salicylates, sulfonate/phenates, sulfonate/salicylates, sulfonates/phenates/salicylates, as described, for example, in U.S. Patent Nos. 6,153,565 ; 6,281,179 ; 6,429,178 ; and 6,429,178 .
  • Borated detergents and methods for borating detergents are well known and described, for example, in U.S. Patent Nos. 3,929,650 ; 3,480,548 ; and 4,792,410 . Borated detergents can be used to provide the lubricating oil compositions of the present invention with all, or a portion, of the requisite amount of boron.
  • Lubricating oil compositions of the present invention preferably contain a magnesium detergent, more preferably an overbased magnesium detergent, in an amount providing the lubricating oil composition with at least 0.09 mass % (900 ppm), preferably at least 0.10 mass % (1000 ppm), more preferably at least 0.115 mass % (1150 ppm) of elemental magnesium.
  • the overbased magnesium detergent will have, or have on average, a TBN of at least about 200, such as from about 200 to about 500; preferably at least about 250, such as from about 250 to about 500; more preferably at least about 300, such as from about 300 to about 450.
  • Overbased ash-containing detergents based on metals other than magnesium are preferably present in amounts contributing no greater than 40 % of the TBN of the lubricating oil composition contributed by overbased detergent. More preferably, lubricating oil compositions of the present invention contain overbased ash-containing detergents based on metals other than magnesium in amounts providing no greater than about 20% of the total TBN contributed to the lubricating oil composition by overbased detergent.
  • Lubricating oil compositions of the present invention may also contain ashless (metal-free) detergents such as oil-soluble hydrocarbyl phenol aldehyde condensates described, for example, in US-2005-0277559-A1 .
  • ashless (metal-free) detergents such as oil-soluble hydrocarbyl phenol aldehyde condensates described, for example, in US-2005-0277559-A1 .
  • detergent in total is used in an amount providing the lubricating oil composition with from about 0.35 to about 1.0 mass %, such as from about 0.5 to about 0.9 mass %, more preferably from about 0.6 to about 0.8 mass % of sulfated ash (SASH).
  • the lubricating oil composition has a TBN of from about 7 to about 15, such as from about 8 to about 13, more preferably from about 9 to about 11.
  • TBN may be contributed to the lubricating oil composition by additives other than detergents. Dispersants, antioxidants and antiwear agents may in some cases contribute 40 % or more of the total amount of lubricant TBN.
  • lubricating oil compositions formulated for use in a heavy duty diesel engine comprise from about 0.5 to about 10 mass %, preferably from about 1.5 to about 5 mass %, most preferably from about 2 to about 3 mass % of detergent, based on the total mass of the formulated lubricating oil composition.
  • Detergents are conventionally formed in diluent oil.
  • detergents are referred to by the TBN, which is the TBN of the active detergent in the diluent. Therefore, while other additives are often referred to in terms of the amount of active ingredient (A.I.), stated amounts of detergent refer to the total mass of detergent including diluent.
  • Dihydrocarbyl dithiophosphate metal salts are frequently used as antiwear and antioxidant agents.
  • the metal may be an alkali or alkaline earth metal, or aluminum, lead, tin, molybdenum, manganese, nickel or copper.
  • the zinc salts are most commonly used in lubricating oil in amounts of 0.1 to 10, preferably 0.2 to 2 mass %, based upon the total weight of the lubricating oil composition. They may be prepared in accordance with known techniques by first forming a dihydrocarbyl dithiophosphoric acid (DDPA), usually by reaction of one or more alcohol or a phenol with P 2 S 5 and then neutralizing the formed DDPA with a zinc compound.
  • DDPA dihydrocarbyl dithiophosphoric acid
  • a dithiophosphoric acid may be made by reacting mixtures of primary and secondary alcohols.
  • multiple dithiophosphoric acids can be prepared where the hydrocarbyl groups on one are entirely secondary in character and the hydrocarbyl groups on the others are entirely primary in character.
  • any basic or neutral zinc compound could be used but the oxides, hydroxides and carbonates are most generally employed.
  • Commercial additives frequently contain an excess of zinc due to the use of an excess of the basic zinc compound in the neutralization reaction.
  • the preferred zinc dihydrocarbyl dithiophosphates are oil soluble salts of dihydrocarbyl dithiophosphoric acids and may be represented by the following formula: wherein R and R' may be the same or different hydrocarbyl radicals containing from 1 to 18, preferably 2 to 12, carbon atoms and including radicals such as alkyl, alkenyl, aryl, arylalkyl, alkaryl and cycloaliphatic radicals. Particularly preferred as R and R' groups are alkyl groups of 2 to 8 carbon atoms.
  • the radicals may, for example, be ethyl, n-propyl, i-propyl, n-butyl, i-butyl, sec-butyl, amyl, n-hexyl, i-hexyl, n-octyl, decyl, dodecyl, octadecyl, 2-ethylhexyl, phenyl, butylphenyl, cyclohexyl, methylcyclopentyl, propenyl, butenyl.
  • the total number of carbon atoms (i.e. R and R') in the dithiophosphoric acid will generally be about 5 or greater.
  • the zinc dihydrocarbyl dithiophosphate can therefore comprise zinc dialkyl dithiophosphates.
  • Lubricating oil compositions of the present invention have a phosphorous content of no greater than about 0.12 mass % (1200 ppm).
  • ZDDP is used in an amount close or equal to the maximum amount allowed.
  • lubricating oil compositions in accordance with the present invention formulated for use in heavy duty diesel engines, will preferably contain ZDDP or other metal salt of a dihydrocarbyl dithiophosphate, in an amount introducing from about 0.08 to about 0.12 mass % of phosphorus, based on the total mass of the lubricating oil composition.
  • ZDDP is the sole phosphorus- containing additive present.
  • Oxidation inhibitors or antioxidants reduce the tendency of mineral oils to deteriorate in service. Oxidative deterioration can be evidenced by sludge in the lubricant, varnish-like deposits on the metal surfaces, and by viscosity growth.
  • Oxidative deterioration can be evidenced by sludge in the lubricant, varnish-like deposits on the metal surfaces, and by viscosity growth.
  • Such oxidation inhibitors include hindered phenols, alkaline earth metal salts of alkylphenolthioesters having preferably C 5 to C 12 alkyl side chains, calcium nonylphenol sulfide, oil soluble phenates and sulfurized phenates, phosphosulfurized or sulfurized hydrocarbons or esters, phosphorous esters, metal thiocarbamates, oil soluble copper compounds as described in U.S. Patent No. 4,867,890 , and molybdenum-containing compounds.
  • Aromatic amines having at least two aromatic groups attached directly to the nitrogen constitute another class of compounds that is frequently used for antioxidancy.
  • Typical oil soluble aromatic amines having at least two aromatic groups attached directly to one amine nitrogen contain from 6 to 16 carbon atoms.
  • the amines may contain more than two aromatic groups.
  • Compounds having a total of at least three aromatic groups in which two aromatic groups are linked by a covalent bond or by an atom or group (e.g., an oxygen or sulfur atom, or a -CO-, - SO 2 - or alkylene group) and two are directly attached to one amine nitrogen also considered aromatic amines having at least two aromatic groups attached directly to the nitrogen.
  • the aromatic rings are typically substituted by one or more substituents selected from alkyl, cycloalkyl, alkoxy, aryloxy, acyl, acylamino, hydroxy, and nitro groups.
  • the amount of any such oil soluble aromatic amines having at least two aromatic groups attached directly to one amine nitrogen should preferably not exceed 0.4 mass %.
  • the antiwear agent ZDDP provides a strong antioxidant credit to lubricants.
  • lubricant formulators When less ZDDP is used in order to meet phosphorus and SASH limits, lubricant formulators must compensate for the resulting reduction in oxidation inhibition, preferably by use of highly effective, ashless, sulfur-free antioxidants.
  • Lubricating oil compositions in accordance with the present invention therefore preferably contain at least about 0.5 mass%, preferably at least about 0.6 mass %, such as at least 0.8 mass%, more preferably, at least 1.0 mass % of an ashless antioxidant selected from the group consisting of sulfur-free phenolic antioxidant, aminic antioxidant, or a combination thereof.
  • lubricating oil compositions in accordance with the present invention contain a combination of sulfur-free phenolic antioxidant and aminic antioxidant.
  • Dispersants maintain in suspension materials resulting from oxidation during use that are insoluble in oil, thus preventing sludge flocculation and precipitation, or deposition on metal parts.
  • the lubricating oil composition of the present invention comprises at least one dispersant, and may comprise a plurality of dispersants.
  • the dispersant or dispersants are preferably nitrogen-containing dispersants and preferably contribute, in total, from about 0.08 to about 0.19 mass %, such as from about 0.09 to about 0.18 mass %, most preferably from about 0.09 to about 0.16 mass % of nitrogen to the lubricating oil composition.
  • Dispersants useful in the context of the present invention include the range of nitrogen-containing, ashless (metal-free) dispersants known to be effective to reduce formation of deposits upon use in gasoline and diesel engines, when added to lubricating oils and comprise an oil soluble polymeric long chain backbone having functional groups capable of associating with particles to be dispersed.
  • such dispersants typically have amine, amine-alcohol or amide polar moieties attached to the polymer backbone, often via a bridging group.
  • the ashless dispersant may be, for example, selected from oil soluble salts, esters, amino-esters, amides, imides and oxazolines of long chain hydrocarbon-substituted mono- and polycarboxylic acids or anhydrides thereof; thiocarboxylate derivatives of long chain hydrocarbons; long chain aliphatic hydrocarbons having polyamine moieties attached directly thereto; and Mannich condensation products formed by condensing a long chain substituted phenol with formaldehyde and polyalkylene polyamine.
  • each mono- or dicarboxylic acid-producing moiety will react with a nucleophilic group (amine or amide) and the number of functional groups in the polyalkenyl-substituted carboxylic acylating agent will determine the number of nucleophilic groups in the finished dispersant.
  • the polyalkenyl moiety of the dispersant of the present invention has a number average molecular weight of from about 700 to about 3000, preferably between 950 and 3000, such as between 950 and 2800, more preferably from about 950 to 2500, and most preferably from about 950 to about 2400.
  • the dispersant comprises a combination of a lower molecular weight dispersant (e.g., having a number average molecular weight of from about 700 to 1100) and a high molecular weight dispersant having a number average molecular weight of from about at least about 1500, preferably between 1800 and 3000, such as between 2000 and 2800, more preferably from about 2100 to 2500, and most preferably from about 2150 to about 2400.
  • a lower molecular weight dispersant e.g., having a number average molecular weight of from about 700 to 1100
  • a high molecular weight dispersant having a number average molecular weight of from about at least about 1500, preferably between 1800 and 3000, such as between 2000 and 2800, more preferably from about 2100 to 2500, and most preferably from about 2150 to about 2400.
  • the molecular weight of a dispersant is generally expressed in terms of the molecular weight of the polyalkenyl moiety as the precise molecular weight range of the dispersant depends on numerous parameters including the type of polymer used to derive the dispersant, the number of functional groups, and the type of nucleophilic group employed.
  • the polyalkenyl moiety from which the high molecular weight dispersants are derived preferably have a narrow molecular weight distribution (MWD), also referred to as polydispersity, as determined by the ratio of weight average molecular weight (M w ) to number average molecular weight (M n ).
  • MWD molecular weight distribution
  • polymers from which the dispersants of the present invention are derived have a M w /M n of from about 1.5 to about 2.0, preferably from about 1.5 to about 1.9, most preferably from about 1.6 to about 1.8.
  • Suitable hydrocarbons or polymers employed in the formation of the dispersants of the present invention include homopolymers, interpolymers or lower molecular weight hydrocarbons.
  • such polymers comprise interpolymers of ethylene and at least one alpha-olefin of the above formula, wherein R 1 is alkyl of from 1 to 18 carbon atoms, and more preferably is alkyl of from 1 to 8 carbon atoms, and more preferably still of from 1 to 2 carbon atoms.
  • useful alpha-olefin monomers and comonomers include, for example, propylene, butene-1, hexene-1, octene-1, 4-methylpentene-1, decene-1, dodecene-1, tridecene-1, tetradecene-1, pentadecene-1, hexadecene-1, heptadecene-1, octadecene-1, nonadecene-1, and mixtures thereof (e.g., mixtures of propylene and butene-1, and the like).
  • Exemplary of such polymers are propylene homopolymers, butene-1 homopolymers, ethylene-propylene copolymers, ethylene-butene-1 copolymers, propylene-butene copolymers and the like, wherein the polymer contains at least some terminal and/or internal unsaturation.
  • Preferred polymers are unsaturated copolymers of ethylene and propylene and ethylene and butene-1.
  • the interpolymers of this invention may contain a minor amount, e.g. 0.5 to 5 mole % of a C 4 to C 18 nonconjugated diolefin comonomer.
  • the polymers of this invention comprise only alpha-olefin homopolymers, interpolymers of alpha-olefin comonomers and interpolymers of ethylene and alpha-olefin comonomers.
  • the molar ethylene content of the polymers employed in this invention is preferably in the range of 0 to 80 %, and more preferably 0 to 60 %.
  • the ethylene content of such copolymers is most preferably between 15 and 50 %, although higher or lower ethylene contents may be present.
  • These polymers may be prepared by polymerizing alpha-olefin monomer, or mixtures of alpha-olefin monomers, or mixtures comprising ethylene and at least one C 3 to C 28 alpha-olefin monomer, in the presence of a catalyst system comprising at least one metallocene (e.g., a cyclopentadienyl-transition metal compound) and an alumoxane compound.
  • a catalyst system comprising at least one metallocene (e.g., a cyclopentadienyl-transition metal compound) and an alumoxane compound.
  • the percentage of polymer chains exhibiting terminal ethenylidene unsaturation may be determined by FTIR spectroscopic analysis, titration, or C 13 NMR.
  • the chain length of the R 1 alkyl group will vary depending on the comonomer(s) selected for use in the polymerization.
  • These terminally unsaturated interpolymers may be prepared by known metallocene chemistry and may also be prepared as described in U.S. Patent Nos. 5,498,809 ; 5,663,130 ; 5,705,577 ; 5,814,715 ; 6,022,929 and 6,030,930 .
  • polymers prepared by cationic polymerization of isobutene, styrene, and the like are polymers prepared by cationic polymerization of isobutene, styrene, and the like.
  • Common polymers from this class include polyisobutenes obtained by polymerization of a C 4 refinery stream having a butene content of about 35 to about 75 mass %, and an isobutene content of about 30 to about 60 mass %, in the presence of a Lewis acid catalyst, such as aluminum trichloride or boron trifluoride.
  • a preferred source of monomer for making poly-n-butenes is petroleum feedstreams such as Raffinate II. These feedstocks are disclosed in the art such as in U.S. Patent No. 4,952,739 .
  • Polyisobutylene is a most preferred backbone of the present invention because it is readily available by cationic polymerization from butene streams (e.g., using AlCl 3 or BF 3 catalysts). Such polyisobutylenes generally contain residual unsaturation in amounts of about one ethylenic double bond per polymer chain, positioned along the chain.
  • a preferred embodiment utilizes polyisobutylene prepared from a pure isobutylene stream or a Raffinate I stream to prepare reactive isobutylene polymers with terminal vinylidene olefins.
  • these polymers referred to as highly reactive polyisobutylene (HR-PIB)
  • HR-PIB highly reactive polyisobutylene
  • these polymers have a terminal vinylidene content of at least 65%, e.g., 70%, more preferably at least 80%, most preferably, at least 85%.
  • the preparation of such polymers is described, for example, in U.S. Patent No. 4,152,499 .
  • HR-PIB is known and HR-PIB is commercially available, for example, under the tradenames Glissopal TM (from BASF) and Ultravis TM (from BP-Amoco).
  • Polyisobutylene polymers that may be employed are generally based on a hydrocarbon chain of from about 700 to 3000. Methods for making polyisobutylene are known. Polyisobutylene can be functionalized by halogenation (e.g. chlorination), the thermal "ene” reaction, or by free radical grafting using a catalyst (e.g. peroxide), as described below.
  • halogenation e.g. chlorination
  • the thermal "ene” reaction e.g. peroxide
  • a catalyst e.g. peroxide
  • the hydrocarbon or polymer backbone can be functionalized, e.g., with carboxylic acid producing moieties (preferably acid or anhydride moieties) selectively at sites of carbon-to-carbon unsaturation on the polymer or hydrocarbon chains, or randomly along chains using any of the three processes mentioned above or combinations thereof, in any sequence.
  • carboxylic acid producing moieties preferably acid or anhydride moieties
  • the polymer or hydrocarbon may be functionalized, for example, with carboxylic acid producing moieties (preferably acid or anhydride) by reacting the polymer or hydrocarbon under conditions that result in the addition of functional moieties or agents, i.e., acid, anhydride, ester moieties, etc., onto the polymer or hydrocarbon chains primarily at sites of carbon-to-carbon unsaturation (also referred to as ethylenic or olefinic unsaturation) using the halogen assisted functionalization (e.g. chlorination) process or the thermal "ene" reaction.
  • carboxylic acid producing moieties preferably acid or anhydride
  • Selective functionalization can be accomplished by halogenating, e.g., chlorinating or brominating the unsaturated ⁇ -olefin polymer to about 1 to 8 mass %, preferably 3 to 7 mass % chlorine, or bromine, based on the weight of polymer or hydrocarbon, by passing the chlorine or bromine through the polymer at a temperature of 60 to 250°C, preferably 110 to 160°C, e.g., 120 to 140°C, for about 0.5 to 10, preferably 1 to 7 hours.
  • halogenating e.g., chlorinating or brominating the unsaturated ⁇ -olefin polymer to about 1 to 8 mass %, preferably 3 to 7 mass % chlorine, or bromine, based on the weight of polymer or hydrocarbon
  • the halogenated polymer or hydrocarbon (hereinafter backbone) is then reacted with sufficient monounsaturated reactant capable of adding the required number of functional moieties to the backbone, e.g., monounsaturated carboxylic reactant, at 100 to 250°C, usually about 180°C to 235°C, for about 0.5 to 10, e.g., 3 to 8 hours, such that the product obtained will contain the desired number of moles of the monounsaturated carboxylic reactant per mole of the halogenated backbones.
  • the backbone and the monounsaturated carboxylic reactant are mixed and heated while adding chlorine to the hot material.
  • chlorination normally helps increase the reactivity of starting olefin polymers with monounsaturated functionalizing reactant, it is not necessary with some of the polymers or hydrocarbons contemplated for use in the present invention, particularly those preferred polymers or hydrocarbons which possess a high terminal bond content and reactivity.
  • the backbone and the monounsaturated functionality reactant e.g., carboxylic reactant, are contacted at elevated temperature to cause an initial thermal "ene" reaction to take place. Ene reactions are known.
  • the hydrocarbon or polymer backbone can be functionalized by random attachment of functional moieties along the polymer chains by a variety of methods.
  • the polymer in solution or in solid form, may be grafted with the monounsaturated carboxylic reactant, as described above, in the presence of a free-radical initiator.
  • the grafting takes place at an elevated temperature in the range of about 100 to 260°C, preferably 120 to 240°C.
  • free-radical initiated grafting would be accomplished in a mineral lubricating oil solution containing, e.g., 1 to 50 mass %, preferably 5 to 30 mass % polymer based on the initial total oil solution.
  • the free-radical initiators that may be used are peroxides, hydroperoxides, and azo compounds, preferably those that have a boiling point greater than about 100°C and decompose thermally within the grafting temperature range to provide free-radicals.
  • Representative of these free-radical initiators are azobutyronitrile, 2,5-dimethylhex-3-ene-2, 5-bis-tertiary-butyl peroxide and dicumene peroxide.
  • the initiator when used, typically is used in an amount of between 0.005% and 1% by weight based on the weight of the reaction mixture solution.
  • the aforesaid monounsaturated carboxylic reactant material and free-radical initiator are used in a weight ratio range of from about 1.0:1 to 30:1, preferably 3:1 to 6:1.
  • the grafting is preferably carried out in an inert atmosphere, such as under nitrogen blanketing.
  • the resulting grafted polymer is characterized by having carboxylic acid (or ester or anhydride) moieties randomly attached along the polymer chains: it being understood, of course, that some of the polymer chains remain ungrafted.
  • the free radical grafting described above can be used for the other polymers and hydrocarbons of the present invention.
  • the preferred monounsaturated reactants that are used to functionalize the backbone comprise mono- and dicarboxylic acid material, i.e., acid, anhydride, or acid ester material, including (i) monounsaturated C 4 to C 10 dicarboxylic acid wherein
  • the monounsaturated carboxylic reactant typically will be used in an amount ranging from about equimolar amount to about 100 mass % excess, preferably 5 to 50 mass % excess, based on the moles of polymer or hydrocarbon. Unreacted excess monounsaturated carboxylic reactant can be removed from the final dispersant product by, for example, stripping, usually under vacuum, if required.
  • the functionalized oil-soluble polymeric hydrocarbon backbone is then derivatized with a nitrogen-containing nucleophilic reactant, such as an amine, aminoalcohol, amide, or mixture thereof, to form a corresponding derivative.
  • a nitrogen-containing nucleophilic reactant such as an amine, aminoalcohol, amide, or mixture thereof.
  • Amine compounds are preferred.
  • Useful amine compounds for derivatizing functionalized polymers comprise at least one amine and can comprise one or more additional amine or other reactive or polar groups. These amines may be hydrocarbyl amines or may be predominantly hydrocarbyl amines in which the hydrocarbyl group includes other groups, e.g., hydroxy groups, alkoxy groups, amide groups, nitriles, imidazoline groups, and the like.
  • Particularly useful amine compounds include mono- and polyamines, e.g., polyalkene and polyoxyalkylene polyamines of about 2 to 60, such as 2 to 40 (e.g., 3 to 20) total carbon atoms having about 1 to 12, such as 3 to 12, preferably 3 to 9, most preferably form about 6 to about 7 nitrogen atoms per molecule.
  • Mixtures of amine compounds may advantageously be used, such as those prepared by reaction of alkylene dihalide with ammonia.
  • Preferred amines are aliphatic saturated amines, including, for example, 1,2-diaminoethane; 1,3-diaminopropane; 1,4-diaminobutane; 1,6-diaminohexane; polyethylene amines such as diethylene triamine; triethylene tetramine; tetraethylene pentamine; and polypropyleneamines such as 1,2-propylene diamine; and di-(1,2-propylene)triamine.
  • Such polyamine mixtures known as PAM
  • Particularly preferred polyamine mixtures are mixtures derived by distilling the light ends from PAM products. The resulting mixtures, known as "heavy" PAM, or HPAM, are also commercially available.
  • amine compounds include: alicyclic diamines such as 1,4-di(aminomethyl) cyclohexane and heterocyclic nitrogen compounds such as imidazolines.
  • Another useful class of amines is the polyamido and related amido-amines as disclosed in U.S. Patent Nos. 4,857,217 ; 4,956,107 ; 4,963,275 ; and 5,229,022 .
  • TAM tris(hydroxymethyl)amino methane
  • Dendrimers, star-like amines, and comb-structured amines may also be used.
  • condensed amines as described in U.S. Patent No. 5,053,152 .
  • the functionalized polymer is reacted with the amine compound using conventional techniques as described, for example, in U.S. Patent Nos. 4,234,435 and 5,229,022 , as well as in EP-A-208,560 .
  • a preferred dispersant composition is one comprising at least one polyalkenyl succinimide, which is the reaction product of a polyalkenyl substituted succinic anhydride (e.g., PIBSA) and a polyamine (PAM) that has a coupling ratio of from about 0.65 to about 1.25, preferably from about 0.8 to about 1.1, most preferably from about 0.9 to about 1.
  • PIBSA polyalkenyl substituted succinic anhydride
  • PAM polyamine
  • “coupling ratio” may be defined as a ratio of the number of succinyl groups in the PIBSA to the number of primary amine groups in the polyamine reactant.
  • Mannich base condensation products Another class of high molecular weight ashless dispersants comprises Mannich base condensation products. Generally, these products are prepared by condensing about one mole of a long chain alkyl-substituted mono- or polyhydroxy benzene with about 1 to 2.5 moles of carbonyl compound(s) (e.g., formaldehyde and paraformaldehyde) and about 0.5 to 2 moles of polyalkylene polyamine, as disclosed, for example, in U.S. Patent No. 3,442,808 .
  • carbonyl compound(s) e.g., formaldehyde and paraformaldehyde
  • Such Mannich base condensation products may include a polymer product of a metallocene catalyzed polymerization as a substituent on the benzene group, or may be reacted with a compound containing such a polymer substituted on a succinic anhydride in a manner similar to that described in U.S. Patent No. 3,442,808 .
  • Examples of functionalized and/or derivatized olefin polymers synthesized using metallocene catalyst systems are described in the publications identified supra .
  • the dispersant(s) of the present invention are preferably non-polymeric (e.g., are mono- or bis-succinimides).
  • Dispersant(s), particularly the lower molecular weight dispersants may optionally be borated. Such dispersants can be borated by conventional means, as generally taught in U.S. Patent Nos. 3,087,936 , 3,254,025 and 5,430,105 . Boration of the dispersant is readily accomplished by treating an acyl nitrogen-containing dispersant with a boron compound such as boron oxide, boron halide boron acids, and esters of boron acids, in an amount sufficient to provide from about 0.1 to about 20 atomic proportions of boron for each mole of acylated nitrogen composition. Borated dispersants can be used to provide the lubricating oil compositions of the present invention with all, or a portion, of the requisite amount of boron.
  • a boron compound such as boron oxide, boron halide boron acids, and esters of boron acids
  • Dispersants derived from highly reactive polyisobutylene have been found to provide lubricating oil compositions with a wear credit relative to a corresponding dispersant derived from conventional polyisobutylene. This wear credit is of particular importance in lubricants containing reduced levels of ash-containing antiwear agents, such as ZDDP.
  • at least one dispersant used in the lubricating oil compositions of the present invention is derived from highly reactive polyisobutylene.
  • Non-dispersant/detergent boron sources are prepared by reacting a boron compound with an oil-soluble or oil-dispersible additive or compound.
  • Boron compounds include boron oxide, boron oxide hydrate, boron trioxide, boron trifluoride, boron tribromide, boron trichloride, boron acid such as boronic acid, boric acid, tetraboric acid and metaboric acid, boron hydrides, boron amides and various esters of boron acids.
  • Suitable "non-dispersant boron sources” may comprise any oil-soluble, boron-containing compound, but preferably comprise one or more boron-containing additives known to impart enhanced properties to lubricating oil compositions.
  • boron-containing additives include, for example, borated dispersant VI improver; alkali metal, mixed alkali metal or alkaline earth metal borate; borated overbased metal detergent; borated epoxide; borate ester; and borate amide.
  • Alkali metal and alkaline earth metal borates are generally hydrated particulate metal borates, which are known in the art.
  • Alkali metal borates include mixed alkali and alkaline earth metal borates. These metal borates are available commercially.
  • Representative patents describing suitable alkali metal and alkaline earth metal borates and their methods of manufacture include U.S. Patent Nos. 3,997,454 ; 3,819,521 ; 3,853.772 ; 3,907,601 ; 3,997,454 ; and 4,089,790 .
  • the borated amines maybe prepared by reacting one or more of the above boron compounds with one or more of fatty amines, e.g., an amine having from four to eighteen carbon atoms.
  • Borated amines may be prepared by reacting the amine with the boron compound at a temperature of from 50 to 300, preferably from 100 to 250 °C and at a ratio from 3:1 to 1:3 equivalents of amine to equivalents of boron compound.
  • Borated fatty epoxides are generally the reaction product of one or more of the above boron compounds with at least one epoxide.
  • the epoxide is generally an aliphatic epoxide having from 8 to 30, preferably from 10 to 24, more preferably from 12 to 20, carbon atoms.
  • Examples of useful aliphatic epoxides include heptyl epoxide and octyl epoxide. Mixtures of epoxides may also be used, for instance commercial mixtures of epoxides having from 14 to 16 carbon atoms and from 14 to 18 carbon atoms.
  • the borated fatty epoxides are generally known and are described in U.S. Patent 4,584,115 .
  • Borate esters may be prepared by reacting one or more of the above boron compounds with one or more alcohol of suitable oleophilicity. Typically, the alcohol contains from 6 to 30, or from 8 to 24, carbon atoms. Methods of making such borate esters are known in the art.
  • the borate esters can be borated phospholipids. Such compounds, and processes for making such compounds, are described in EP-A-0 684 298 . Borated overbased metal detergents are known in the art where the borate substitutes the carbonate in the core either in part or in full.
  • additives may be incorporated into the compositions of the invention to enable particular performance requirements to be met.
  • additives which may be included in the lubricating oil compositions of the present invention are metal rust inhibitors, viscosity index improvers, corrosion inhibitors, oxidation inhibitors, friction modifiers, anti-foaming agents, anti-wear agents and pour point depressants. Some are discussed in further detail below.
  • lubricating oil compositions particularly lubricating oil compositions for HDD engines, preferably include additives effective in the dispersion of soot.
  • each Ar independently represents an aromatic moiety having 0 to 3 substituents selected from alkyl, alkoxy, alkoxyalkyl, hydroxy, hydroxyalkyl, acyloxy, acyloxyalkyl, aryloxy, aryloxy alkyl, halo and combinations thereof; each L is independently a linking moiety comprising a carbon-carbon single bond or a linking group; each Y' is independently a moiety of the formula Z(O(CR 2 ) n ) y X-, where X is selected from (CR' 2 ) z , O and S; R and R' are each independently selected from H, C 1 to C 6 alkyl and aryl; z is 1 to 10; n is 0 to 10 when X is (CR' 2 ) z , and 2 to 10 when X is O or S; y is 1 to 30; Z is H, an acyl group, an alkyl, alkoxy, alkoxyalkyl, hydroxy, hydroxyalky
  • Friction modifiers and fuel economy agents that are compatible with the other ingredients of the final oil may also be included.
  • examples of such materials include glyceryl monoesters of higher fatty acids, for example, glyceryl mono-oleate; esters of long chain polycarboxylic acids with diols, for example, the butane diol ester of a dimerized unsaturated fatty acid; oxazoline compounds; and alkoxylated alkyl-substituted mono-amines, diamines and alkyl ether amines, for example, ethoxylated tallow amine and ethoxylated tallow ether amine.
  • Other known friction modifiers comprise oil-soluble organo-molybdenum compounds.
  • organo-molybdenum friction modifiers also provide antioxidant and antiwear credits to a lubricating oil composition.
  • oil soluble organo-molybdenum compounds include dithiocarbamates, dithiophosphates, dithiophosphinates, xanthates, thioxanthates, sulfides, and the like, and mixtures thereof.
  • Particularly preferred are molybdenum dithiocarbamates, dialkyldithiophosphates, alkyl xanthates and alkylthioxanthates.
  • the molybdenum compound may be an acidic molybdenum compound. These compounds will react with a basic nitrogen compound as measured by ASTM test D-664 or D-2896 titration procedure and are typically hexavalent. Included are molybdic acid, ammonium molybdate, sodium molybdate, potassium molybdate, and other alkaline metal molybdates and other molybdenum salts, e.g., hydrogen sodium molybdate, MoOCl 4 , MoO 2 Br 2 , Mo 2 O 3 Cl 6 , molybdenum trioxide or similar acidic molybdenum compounds.
  • molybdenum compounds useful in the compositions of this invention are organo-molybdenum compounds of the formula Mo(ROCS 2 ) 4 and Mo(RSCS 2 ) 4 wherein R is an organo group selected from the group consisting of alkyl, aryl, aralkyl and alkoxyalkyl, generally of from 1 to 30 carbon atoms, and preferably 2 to 12 carbon atoms and most preferably alkyl of 2 to 12 carbon atoms.
  • R is an organo group selected from the group consisting of alkyl, aryl, aralkyl and alkoxyalkyl, generally of from 1 to 30 carbon atoms, and preferably 2 to 12 carbon atoms and most preferably alkyl of 2 to 12 carbon atoms.
  • dialkyldithiocarbamates of molybdenum are especially preferred.
  • molybdenum compounds described above in addition to providing friction-reducing properties, also provide antiwear credits and, therefore, molybdenum compounds have been used in lubricating oil compositions formulated with reduced amounts of ZDDP.
  • molybdenum compounds When used in such reduced phosphorus lubricating oil compositions, molybdenum compounds have been used in amounts introducing from about 10 to about 1000 ppm, such as 10 to about 350 ppm, or 10 to about 100 ppm of molybdenum (measured as atoms of molybdenum).
  • the viscosity index of the base stock is increased, or improved, by incorporating therein certain polymeric materials that function as viscosity modifiers (VM) or viscosity index improvers (VII).
  • polymeric materials useful as viscosity modifiers are those having number average molecular weights (Mn) of from about 5,000 to about 250,000, preferably from about 15,000 to about 200,000, more preferably from about 20,000 to about 150,000.
  • These viscosity modifiers can be grafted with grafting materials such as, for example, maleic anhydride, and the grafted material can be reacted with, for example, amines, amides, nitrogen-containing heterocyclic compounds or alcohol, to form multifunctional viscosity modifiers (dispersant-viscosity modifiers).
  • Polymer molecular weight, specifically M n can be determined by various known techniques. One convenient method is gel permeation chromatography (GPC), which additionally provides molecular weight distribution information (see W. W. Yau, J. J. Kirkland and D. D. Bly, "Modern Size Exclusion Liquid Chromatography", John Wiley and Sons, New York, 1979 ).
  • GPC gel permeation chromatography
  • Another useful method for determining molecular weight, particularly for lower molecular weight polymers is vapor pressure osmometry (see, e.g., ASTM D3592).
  • At least one viscosity modifier used in the lubricating oil compositions of the present invention is a linear diblock copolymer comprising one block derived primarily, preferably predominantly, from vinyl aromatic hydrocarbon monomer, and one block derived primarily, preferably predominantly, from diene monomer.
  • Useful vinyl aromatic hydrocarbon monomers include those containing from 8 to about 16 carbon atoms such as aryl-substituted styrenes, alkoxy-substituted styrenes, vinyl naphthalene, alkyl-substituted vinyl naphthalenes and the like. Dienes, or diolefins, contain two double bonds, commonly located in conjugation in a 1,3 relationship. Olefins containing more than two double bonds, sometimes referred to as polyenes, are also considered within the definition of "diene" as used herein.
  • Useful dienes include those containing from 4 to about 12 carbon atoms, preferably from 8 to about 16 carbon atoms, such as 1,3-butadiene, isoprene, piperylene, methylpentadiene, phenylbutadiene, 3,4-dimethyl-1,3-hexadiene, 4,5-diethyl-1,3-octadiene, with 1,3-butadiene and isoprene being preferred.
  • prodominantly means that the specified monomer or monomer type that is the principle component in that polymer block is present in an amount of at least 85% by weight of the block.
  • Polymers prepared with diolefins will contain ethylenic unsaturation, and such polymers are preferably hydrogenated.
  • the hydrogenation may be accomplished using any of the techniques known in the prior art.
  • the hydrogenation may be accomplished such that both ethylenic and aromatic unsaturation is converted (saturated) using methods such as those taught, for example, in U.S. Pat. Nos. 3,113,986 and 3,700,633 or the hydrogenation may be accomplished selectively such that a significant portion of the ethylenic unsaturation is converted while little or no aromatic unsaturation is converted as taught, for example, in U.S. Pat. Nos. 3,634,595 ; 3,670,054 ; 3,700,633 and Re 27,145 . Any of these methods can also be used to hydrogenate polymers containing only ethylenic unsaturation and which are free of aromatic unsaturation.
  • the block copolymers may include mixtures of linear diblock polymers as disclosed above, having different molecular weights and/or different vinyl aromatic contents as well as mixtures of linear block copolymers having different molecular weights and/or different vinyl aromatic contents.
  • the use of two or more different polymers may be preferred to a single polymer depending on the rheological properties the product is intended to impart when used to produce formulated engine oil.
  • Examples of commercially available styrene/hydrogenated isoprene linear diblock copolymers include Infineum SV140TM, Infineum SV150TM and Infineum SV160TM, available from Infineum USA L.P.
  • Suitable styrene/1, 3-butadiene hydrogenated block copolymers are sold under the tradename GlissoviscalTM by BASF.
  • LOFIs Pour point depressants
  • PPD lube oil flow improvers
  • LOFIs Pour point depressants
  • VM lube oil flow improvers
  • LOFIs can be grafted with grafting materials such as, for example, maleic anhydride, and the grafted material can be reacted with, for example, amines, amides, nitrogen-containing heterocyclic compounds or alcohol, to form multifunctional additives.
  • additives which maintains the stability of the viscosity of the blend may be necessary to include an additive which maintains the stability of the viscosity of the blend.
  • polar group- containing additives achieve a suitably low viscosity in the pre-blending stage it has been observed that some compositions increase in viscosity when stored for prolonged periods.
  • Additives which are effective in controlling this viscosity increase include the long chain hydrocarbons functionalized by reaction with mono- or dicarboxylic acids or anhydrides which are used in the preparation of the ashless dispersants as hereinbefore disclosed.
  • the lubricating oil compositions of the present invention contain an effective amount of a long chain hydrocarbons functionalized by reaction with mono- or dicarboxylic acids or anhydrides.
  • each additive is typically blended into the base oil in an amount that enables the additive to provide its desired function.
  • Representative effective amounts of such additives, when used in crankcase lubricants, are listed below. All the values listed, except for those referring to metal detergents, are stated as mass percent active ingredient (A.I.).
  • the Noack volatility of the fully formulated lubricating oil composition (oil of lubricating viscosity plus all additives) will be no greater than 20 mass %, such as no greater than 15 mass %, preferably no greater than 13 mass %.
  • additive concentrates comprising additives (concentrates sometimes being referred to as additive packages) whereby several additives can be added simultaneously to the oil to form the lubricating oil composition.
  • the final composition may employ from 5 to 25 mass %, preferably 5 to 22 mass %, typically 10 to 20 mass % of the concentrate, the remainder being oil of lubricating viscosity.
  • phosphorus content boron content, molybdenum content, magnesium content, calcium content, etc. refer to the content as measured by ASTM D5185; and sulfated ash content refers to the content as measured by ASTM D874.
  • dispersant combination of borated dispersant and non-borated dispersant
  • detergent a combination of calcium phenate, calcium sulfonate and magnesium sulfonate detergents
  • ZDDP so
  • the resulting oil had a boron content of 65 ppm, a magnesium content of 1156 ppm, a molybdenum content of 44 ppm and a TBN of 9.9; 79 % of the TBN contributed by overbased detergent (52% of the TBN of the composition), was provided by the overbased magnesium detergents.
  • Valve train wear resulting from the use of the above lubricant was measured in a Cummins ISB engine test; one of the engine tests for the API CJ-4/CI-4 specifications for HDD lubricants.
  • the ISB engine test includes two stages. Stage 1 runs for 100 hours to produce soot in the oil. Stage 2 is a 250 hour cyclic portion, intended to produce heavy load on the engine in short bursts.
  • the valve train parts are measured for wear, reported as tappet weight loss, in milligrams, and camshaft lobe wear, in microns.
  • Table 2 Oil Oil 1 Passing Limit Grade 5W40 Tappet Weight Loss (mg.) 85 100 max Cam Shaft Lobe Wear, Snap Gauge ( ⁇ m) 43 55 max
  • Oil 1 a 5W40 grade lubricant formulated with all Group III base stock and having a phosphorus content of less than 1200 ppm, was able to meet the wear performance requirements of the API CJ-4/CI-4 specifications.
  • compositions described as "comprising" a plurality of defined components are to be construed as including compositions formed by admixing the defined plurality of defined components.
  • compositions formed by admixing the defined plurality of defined components are described in the foregoing specification. What applicants submit is their invention, however, is not to be construed as limited to the particular embodiments disclosed, since the disclosed embodiments are regarded as illustrative rather than limiting. Changes may be made by those skilled in the art without departing from the spirit of the invention.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Lubricants (AREA)
EP09150505A 2008-01-22 2009-01-14 Utilisation d'une composition d'huile lubrifiante Not-in-force EP2083063B1 (fr)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US12/017,385 US20090186784A1 (en) 2008-01-22 2008-01-22 Lubricating Oil Composition

Publications (2)

Publication Number Publication Date
EP2083063A1 true EP2083063A1 (fr) 2009-07-29
EP2083063B1 EP2083063B1 (fr) 2012-03-14

Family

ID=40436422

Family Applications (1)

Application Number Title Priority Date Filing Date
EP09150505A Not-in-force EP2083063B1 (fr) 2008-01-22 2009-01-14 Utilisation d'une composition d'huile lubrifiante

Country Status (7)

Country Link
US (1) US20090186784A1 (fr)
EP (1) EP2083063B1 (fr)
JP (1) JP2009197230A (fr)
CN (1) CN101492631A (fr)
AT (1) ATE549389T1 (fr)
CA (1) CA2650354A1 (fr)
SG (1) SG154416A1 (fr)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017148835A1 (fr) * 2016-02-29 2017-09-08 Shell Internationale Research Maatschappij B.V. Composition lubrifiante
US11268044B2 (en) 2015-07-23 2022-03-08 Total Marketing Services Long duration fuel economy lubricating composition

Families Citing this family (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8586519B2 (en) * 2007-02-12 2013-11-19 Chevron U.S.A. Inc. Multi-grade engine oil formulations comprising a bio-derived ester component
US20100152072A1 (en) * 2008-12-17 2010-06-17 Chevron Oronite Company Llc Lubricating oil compositions
US8642523B2 (en) 2010-02-01 2014-02-04 Exxonmobil Research And Engineering Company Method for improving the fuel efficiency of engine oil compositions for large low and medium speed engines by reducing the traction coefficient
US8759267B2 (en) 2010-02-01 2014-06-24 Exxonmobil Research And Engineering Company Method for improving the fuel efficiency of engine oil compositions for large low and medium speed engines by reducing the traction coefficient
WO2011094566A1 (fr) * 2010-02-01 2011-08-04 Exxonmobil Research And Engineering Company Procédé d'amélioration du rendement énergétique de compositions d'huile moteur pour grands moteurs à gaz, à faible et moyenne vitesses, par réduction du coefficient de traction
US8728999B2 (en) 2010-02-01 2014-05-20 Exxonmobil Research And Engineering Company Method for improving the fuel efficiency of engine oil compositions for large low and medium speed engines by reducing the traction coefficient
US8598103B2 (en) 2010-02-01 2013-12-03 Exxonmobil Research And Engineering Company Method for improving the fuel efficiency of engine oil compositions for large low, medium and high speed engines by reducing the traction coefficient
US8748362B2 (en) 2010-02-01 2014-06-10 Exxonmobile Research And Engineering Company Method for improving the fuel efficiency of engine oil compositions for large low and medium speed gas engines by reducing the traction coefficient
FR2968011B1 (fr) * 2010-11-26 2014-02-21 Total Raffinage Marketing Composition lubrifiante pour moteur
US20220049178A1 (en) * 2014-01-10 2022-02-17 The Lubrizol Corporation Method Of Lubricating An Internal Combustion Engine
EP3092290B1 (fr) * 2014-01-10 2019-09-04 The Lubrizol Corporation Méthode à lubrifier un moteur à combustion
CN115093893A (zh) * 2014-04-25 2022-09-23 路博润公司 多级润滑组合物
US9574158B2 (en) 2014-05-30 2017-02-21 Afton Chemical Corporation Lubricating oil composition and additive therefor having improved wear properties
FR3035663B1 (fr) 2015-04-30 2017-06-02 Total Marketing Services Composition lubrifiante ultra-fluide
JP6235549B2 (ja) * 2015-12-07 2017-11-22 Ｅｍｇルブリカンツ合同会社 潤滑油組成物
JP6661435B2 (ja) * 2016-03-23 2020-03-11 出光興産株式会社 潤滑油組成物、及び潤滑方法
US9951290B2 (en) 2016-03-31 2018-04-24 Exxonmobil Research And Engineering Company Lubricant compositions
US10329512B2 (en) * 2017-02-28 2019-06-25 Chevron Oronite Company Llc Lubrication oil composition with enhanced wear and low speed pre-ignition properties
EP3652282B1 (fr) * 2017-07-14 2025-08-06 Chevron Oronite Company LLC Compositions d'huile lubrifiante et procédé pour empêcher ou réduire le préallumage à faible vitesse dans des moteurs à allumage par étincelles à injection directe
FR3069864B1 (fr) * 2017-08-03 2019-08-16 Total Marketing Services Composition lubrifiante comprenant un diester
CN108085091B (zh) * 2017-12-08 2021-06-11 锦州新兴石油添加剂有限责任公司 高性能ci-4、ch-4和cf-4经济型阶梯式通用内燃机油复合剂及其应用
WO2021076733A1 (fr) * 2019-10-15 2021-04-22 The Lubrizol Corporation Composition lubrifiante à bon rendement énergétique

Citations (68)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3087936A (en) 1961-08-18 1963-04-30 Lubrizol Corp Reaction product of an aliphatic olefinpolymer-succinic acid producing compound with an amine and reacting the resulting product with a boron compound
US3113986A (en) 1962-01-08 1963-12-10 Hercules Powder Co Ltd Hydrogenation of unsaturated hydrocarbons
US3172892A (en) 1959-03-30 1965-03-09 Reaction product of high molecular weight succinic acids and succinic anhydrides with an ethylene poly- amine
GB989409A (en) 1962-08-24 1965-04-14 Gen Electric Organopolysiloxane compositions
US3215707A (en) 1960-06-07 1965-11-02 Lubrizol Corp Lubricant
US3231587A (en) 1960-06-07 1966-01-25 Lubrizol Corp Process for the preparation of substituted succinic acid compounds
US3272746A (en) 1965-11-22 1966-09-13 Lubrizol Corp Lubricating composition containing an acylated nitrogen compound
US3275554A (en) 1963-08-02 1966-09-27 Shell Oil Co Polyolefin substituted polyamines and lubricants containing them
US3381022A (en) 1963-04-23 1968-04-30 Lubrizol Corp Polymerized olefin substituted succinic acid esters
US3442808A (en) 1966-11-01 1969-05-06 Standard Oil Co Lubricating oil additives
US3480548A (en) 1967-06-21 1969-11-25 Texaco Inc Alkaline earth metal polyborate carbonate overbased alkaline earth metal sulfonate lube oil composition
US3565804A (en) 1965-08-23 1971-02-23 Chevron Res Lubricating oil additives
USRE27145E (en) 1969-05-20 1971-06-22 Side-chain
US3634595A (en) 1969-03-31 1972-01-11 Giorgio Pasquali A generator of harmonic signals with a helical spring
US3670054A (en) 1969-10-29 1972-06-13 Shell Oil Co Block copolymers having reduced solvent sensitivity
US3700633A (en) 1971-05-05 1972-10-24 Shell Oil Co Selectively hydrogenated block copolymers
US3819521A (en) 1971-06-07 1974-06-25 Chevron Res Lubricant containing dispersed borate and a polyol
US3853772A (en) 1971-06-01 1974-12-10 Chevron Res Lubricant containing alkali metal borate dispersed with a mixture of dispersants
US3907601A (en) 1970-02-17 1975-09-23 Union Carbide Corp Vinyl battery separators
US3912764A (en) 1972-09-29 1975-10-14 Cooper Edwin Inc Preparation of alkenyl succinic anhydrides
US3929650A (en) 1974-03-22 1975-12-30 Chevron Res Extreme pressure agent and its preparation
US3997454A (en) 1974-07-11 1976-12-14 Chevron Research Company Lubricant containing potassium borate
US4089790A (en) 1975-11-28 1978-05-16 Chevron Research Company Synergistic combinations of hydrated potassium borate, antiwear agents, and organic sulfide antioxidants
US4102798A (en) 1974-03-27 1978-07-25 Exxon Research & Engineering Co. Oxazoline additives useful in oleaginous compositions
US4110349A (en) 1976-06-11 1978-08-29 The Lubrizol Corporation Two-step method for the alkenylation of maleic anhydride and related compounds
US4113639A (en) 1976-11-11 1978-09-12 Exxon Research & Engineering Co. Lubricating oil composition containing a dispersing-varnish inhibiting combination of an oxazoline compound and an acyl nitrogen compound
US4116876A (en) 1977-01-28 1978-09-26 Exxon Research & Engineering Co. Borated oxazolines as varnish inhibiting dispersants in lubricating oils
US4152499A (en) 1977-01-22 1979-05-01 Basf Aktiengesellschaft Polyisobutenes
US4234435A (en) 1979-02-23 1980-11-18 The Lubrizol Corporation Novel carboxylic acid acylating agents, derivatives thereof, concentrate and lubricant compositions containing the same, and processes for their preparation
US4584115A (en) 1982-02-11 1986-04-22 The Lubrizol Corporation Method of preparing boron-containing compositions useful as lubricant additives
EP0208560A2 (fr) 1985-07-11 1987-01-14 Exxon Chemical Patents Inc. Additifs dispersants solubles dans l'huile dans des combustibles et des huiles lubrifiantes
US4792410A (en) 1986-12-22 1988-12-20 The Lubrizol Corporation Lubricant composition suitable for manual transmission fluids
US4857217A (en) 1987-11-30 1989-08-15 Exxon Chemical Patents Inc. Dispersant additives derived from amido-amines
US4867890A (en) 1979-08-13 1989-09-19 Terence Colclough Lubricating oil compositions containing ashless dispersant, zinc dihydrocarbyldithiophosphate, metal detergent and a copper compound
US4927551A (en) 1987-12-30 1990-05-22 Chevron Research Company Lubricating oil compositions containing a combination of a modified succinimide and a Group II metal overbased sulfurized alkylphenol
US4938881A (en) 1988-08-01 1990-07-03 The Lubrizol Corporation Lubricating oil compositions and concentrates
US4952739A (en) 1988-10-26 1990-08-28 Exxon Chemical Patents Inc. Organo-Al-chloride catalyzed poly-n-butenes process
US4956107A (en) 1987-11-30 1990-09-11 Exxon Chemical Patents Inc. Amide dispersant additives derived from amino-amines
US4963275A (en) 1986-10-07 1990-10-16 Exxon Chemical Patents Inc. Dispersant additives derived from lactone modified amido-amine adducts
US5053152A (en) 1985-03-14 1991-10-01 The Lubrizol Corporation High molecular weight nitrogen-containing condensates and fuels and lubricants containing same
US5229022A (en) 1988-08-01 1993-07-20 Exxon Chemical Patents Inc. Ethylene alpha-olefin polymer substituted mono- and dicarboxylic acid dispersant additives (PT-920)
US5241003A (en) 1990-05-17 1993-08-31 Ethyl Petroleum Additives, Inc. Ashless dispersants formed from substituted acylating agents and their production and use
CA1335895C (fr) 1989-02-07 1995-06-13 Exxon Chemical Patents Inc. Methode basse temperature utilisant un melange en zone multiple pour l'obtention de derives de substitution par une longue chaine hydrocarbylee d'acides mono- ou dicarboxyliques
EP0382450B1 (fr) 1989-02-07 1995-06-28 Exxon Chemical Patents Inc. Procédé de préparation de matériaux d'acides mono ou dicarboxyliques substitués d'hydrocarbyles à longue chaîne
US5430105A (en) 1992-12-17 1995-07-04 Exxon Chemical Patents Inc. Low sediment process for forming borated dispersant
EP0684298A2 (fr) 1994-05-23 1995-11-29 The Lubrizol Corporation Compositions pour accroître la durée de conservation de joints d'étanchéité et des lubrifiants et fluides fonctionnels les contenant
US5498809A (en) 1992-12-17 1996-03-12 Exxon Chemical Patents Inc. Polymers derived from ethylene and 1-butene for use in the preparation of lubricant dispersant additives
US5565128A (en) 1994-10-12 1996-10-15 Exxon Chemical Patents Inc Lubricating oil mannich base dispersants derived from heavy polyamine
US5705577A (en) 1992-12-17 1998-01-06 Exxon Chemical Patents Inc. Dilute process for the polymerization of ethylene/α-olefin copolymer using metallocene catalyst systems
US5756431A (en) 1994-06-17 1998-05-26 Exxon Chemical Patents Inc Dispersants derived from heavy polyamine and second amine
US5777025A (en) 1996-02-09 1998-07-07 Exxon Chemical Patents Inc. Process for preparing polyalkenyl substituted C4 to C10 dicarboxylic acid producing materials
US5792730A (en) 1994-07-11 1998-08-11 Exxon Chemical Patents, Inc. Lubricating oil succinimide dispersants derived from heavy polyamine
US5814715A (en) 1992-12-17 1998-09-29 Exxon Chemical Patents Inc Amorphous olefin polymers, copolymers, methods of preparation and derivatives thereof
US5891953A (en) 1996-02-09 1999-04-06 Exxon Chemical Patents Inc Process for preparing polyalkenyl substituted mono- and dicarboxylic acid producing materials (PT-1302)
US6153565A (en) 1996-05-31 2000-11-28 Exxon Chemical Patents Inc Overbased metal-containing detergents
WO2000071649A1 (fr) * 1999-05-19 2000-11-30 Infineum International Limited Composition d'huile lubrifiante contenant moins de 350 ppm de molybdene
US6281179B1 (en) 1996-05-31 2001-08-28 Infineum Usa L.P. Process for preparing an overbased metal-containing detergents
US6429178B1 (en) 1996-05-31 2002-08-06 Infineum Usa L.P. Calcium overbased metal-containing detergents
US20020115575A1 (en) * 2000-12-22 2002-08-22 Antonio Gutierrez Lubricating oil composition
US20020115576A1 (en) * 2000-12-22 2002-08-22 Antonio Gutierrez Hydroxy aromatic mannich base condensation products and the use thereof as soot dispersants in lubricating oil compositions
EP1361263A1 (fr) * 2002-05-07 2003-11-12 Chevron Texaco Japan Ltd. Composition d'huile lubrifiante
US20050009998A1 (en) * 2001-12-19 2005-01-13 Rath Hans Peter Polyisobutene and polyisobutene derivatives for use in lubricant compositions
US20050043191A1 (en) * 2003-08-22 2005-02-24 Farng L. Oscar High performance non-zinc, zero phosphorus engine oils for internal combustion engines
US20050070444A1 (en) * 2003-08-07 2005-03-31 Shaw Robert W. Lubricating oil composition
US20050277559A1 (en) 2004-06-11 2005-12-15 Shaw Robert W Detergent additives for lubricating oil compositions
US20060189492A1 (en) 2005-02-18 2006-08-24 Bera Tushar K Soot dispersants and lubricating oil compositions containing same
US20060276353A1 (en) * 2005-06-01 2006-12-07 Irving Matthew D Lubricating oil composition
US20080194438A1 (en) 2007-02-08 2008-08-14 Bera Tushar K Soot Dispersants and Lubricating Oil Compositions Containing Same

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7407918B2 (en) * 2003-12-11 2008-08-05 Afton Chemical Corporation Lubricating oil compositions

Patent Citations (77)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3172892A (en) 1959-03-30 1965-03-09 Reaction product of high molecular weight succinic acids and succinic anhydrides with an ethylene poly- amine
US3215707A (en) 1960-06-07 1965-11-02 Lubrizol Corp Lubricant
US3231587A (en) 1960-06-07 1966-01-25 Lubrizol Corp Process for the preparation of substituted succinic acid compounds
US3254025A (en) 1961-08-18 1966-05-31 Lubrizol Corp Boron-containing acylated amine and lubricating compositions containing the same
US3087936A (en) 1961-08-18 1963-04-30 Lubrizol Corp Reaction product of an aliphatic olefinpolymer-succinic acid producing compound with an amine and reacting the resulting product with a boron compound
US3113986A (en) 1962-01-08 1963-12-10 Hercules Powder Co Ltd Hydrogenation of unsaturated hydrocarbons
GB989409A (en) 1962-08-24 1965-04-14 Gen Electric Organopolysiloxane compositions
US3381022A (en) 1963-04-23 1968-04-30 Lubrizol Corp Polymerized olefin substituted succinic acid esters
US3275554A (en) 1963-08-02 1966-09-27 Shell Oil Co Polyolefin substituted polyamines and lubricants containing them
US3565804A (en) 1965-08-23 1971-02-23 Chevron Res Lubricating oil additives
US3272746A (en) 1965-11-22 1966-09-13 Lubrizol Corp Lubricating composition containing an acylated nitrogen compound
US3442808A (en) 1966-11-01 1969-05-06 Standard Oil Co Lubricating oil additives
US3480548A (en) 1967-06-21 1969-11-25 Texaco Inc Alkaline earth metal polyborate carbonate overbased alkaline earth metal sulfonate lube oil composition
US3634595A (en) 1969-03-31 1972-01-11 Giorgio Pasquali A generator of harmonic signals with a helical spring
USRE27145E (en) 1969-05-20 1971-06-22 Side-chain
US3670054A (en) 1969-10-29 1972-06-13 Shell Oil Co Block copolymers having reduced solvent sensitivity
US3907601A (en) 1970-02-17 1975-09-23 Union Carbide Corp Vinyl battery separators
US3700633A (en) 1971-05-05 1972-10-24 Shell Oil Co Selectively hydrogenated block copolymers
US3853772A (en) 1971-06-01 1974-12-10 Chevron Res Lubricant containing alkali metal borate dispersed with a mixture of dispersants
US3819521A (en) 1971-06-07 1974-06-25 Chevron Res Lubricant containing dispersed borate and a polyol
US3912764A (en) 1972-09-29 1975-10-14 Cooper Edwin Inc Preparation of alkenyl succinic anhydrides
GB1440219A (en) 1972-09-29 1976-06-23 Cooper Ltd Ethyl Preparation of alkenyl succinic anhydrides
US3929650A (en) 1974-03-22 1975-12-30 Chevron Res Extreme pressure agent and its preparation
US4102798A (en) 1974-03-27 1978-07-25 Exxon Research & Engineering Co. Oxazoline additives useful in oleaginous compositions
US3997454A (en) 1974-07-11 1976-12-14 Chevron Research Company Lubricant containing potassium borate
US4089790A (en) 1975-11-28 1978-05-16 Chevron Research Company Synergistic combinations of hydrated potassium borate, antiwear agents, and organic sulfide antioxidants
US4110349A (en) 1976-06-11 1978-08-29 The Lubrizol Corporation Two-step method for the alkenylation of maleic anhydride and related compounds
US4113639A (en) 1976-11-11 1978-09-12 Exxon Research & Engineering Co. Lubricating oil composition containing a dispersing-varnish inhibiting combination of an oxazoline compound and an acyl nitrogen compound
US4152499A (en) 1977-01-22 1979-05-01 Basf Aktiengesellschaft Polyisobutenes
US4116876A (en) 1977-01-28 1978-09-26 Exxon Research & Engineering Co. Borated oxazolines as varnish inhibiting dispersants in lubricating oils
US4234435A (en) 1979-02-23 1980-11-18 The Lubrizol Corporation Novel carboxylic acid acylating agents, derivatives thereof, concentrate and lubricant compositions containing the same, and processes for their preparation
US4867890A (en) 1979-08-13 1989-09-19 Terence Colclough Lubricating oil compositions containing ashless dispersant, zinc dihydrocarbyldithiophosphate, metal detergent and a copper compound
US4584115A (en) 1982-02-11 1986-04-22 The Lubrizol Corporation Method of preparing boron-containing compositions useful as lubricant additives
US5053152A (en) 1985-03-14 1991-10-01 The Lubrizol Corporation High molecular weight nitrogen-containing condensates and fuels and lubricants containing same
US5230714A (en) 1985-03-14 1993-07-27 The Lubrizol Corporation High molecular weight nitrogen-containing condensates and fuels and lubricants containing same
EP0208560A2 (fr) 1985-07-11 1987-01-14 Exxon Chemical Patents Inc. Additifs dispersants solubles dans l'huile dans des combustibles et des huiles lubrifiantes
US4963275A (en) 1986-10-07 1990-10-16 Exxon Chemical Patents Inc. Dispersant additives derived from lactone modified amido-amine adducts
US4792410A (en) 1986-12-22 1988-12-20 The Lubrizol Corporation Lubricant composition suitable for manual transmission fluids
US4857217A (en) 1987-11-30 1989-08-15 Exxon Chemical Patents Inc. Dispersant additives derived from amido-amines
US4956107A (en) 1987-11-30 1990-09-11 Exxon Chemical Patents Inc. Amide dispersant additives derived from amino-amines
US4927551A (en) 1987-12-30 1990-05-22 Chevron Research Company Lubricating oil compositions containing a combination of a modified succinimide and a Group II metal overbased sulfurized alkylphenol
US4938881A (en) 1988-08-01 1990-07-03 The Lubrizol Corporation Lubricating oil compositions and concentrates
US5229022A (en) 1988-08-01 1993-07-20 Exxon Chemical Patents Inc. Ethylene alpha-olefin polymer substituted mono- and dicarboxylic acid dispersant additives (PT-920)
US4952739A (en) 1988-10-26 1990-08-28 Exxon Chemical Patents Inc. Organo-Al-chloride catalyzed poly-n-butenes process
CA1335895C (fr) 1989-02-07 1995-06-13 Exxon Chemical Patents Inc. Methode basse temperature utilisant un melange en zone multiple pour l'obtention de derives de substitution par une longue chaine hydrocarbylee d'acides mono- ou dicarboxyliques
EP0382450B1 (fr) 1989-02-07 1995-06-28 Exxon Chemical Patents Inc. Procédé de préparation de matériaux d'acides mono ou dicarboxyliques substitués d'hydrocarbyles à longue chaîne
US5241003A (en) 1990-05-17 1993-08-31 Ethyl Petroleum Additives, Inc. Ashless dispersants formed from substituted acylating agents and their production and use
US6030930A (en) 1992-12-17 2000-02-29 Exxon Chemical Patents Inc Polymers derived from ethylene and 1-butene for use in the preparation of lubricant disperant additives
US5498809A (en) 1992-12-17 1996-03-12 Exxon Chemical Patents Inc. Polymers derived from ethylene and 1-butene for use in the preparation of lubricant dispersant additives
US5663130A (en) 1992-12-17 1997-09-02 Exxon Chemical Patents Inc Polymers derived from ethylene and 1-butene for use in the preparation of lubricant dispersant additives
US5705577A (en) 1992-12-17 1998-01-06 Exxon Chemical Patents Inc. Dilute process for the polymerization of ethylene/α-olefin copolymer using metallocene catalyst systems
US6022929A (en) 1992-12-17 2000-02-08 Exxon Chemical Patents Inc. Amorphous olefin polymers, copolymers, methods of preparation and derivatives thereof
US5814715A (en) 1992-12-17 1998-09-29 Exxon Chemical Patents Inc Amorphous olefin polymers, copolymers, methods of preparation and derivatives thereof
US5430105A (en) 1992-12-17 1995-07-04 Exxon Chemical Patents Inc. Low sediment process for forming borated dispersant
EP0684298A2 (fr) 1994-05-23 1995-11-29 The Lubrizol Corporation Compositions pour accroître la durée de conservation de joints d'étanchéité et des lubrifiants et fluides fonctionnels les contenant
US5756431A (en) 1994-06-17 1998-05-26 Exxon Chemical Patents Inc Dispersants derived from heavy polyamine and second amine
US5854186A (en) 1994-06-17 1998-12-29 Exxon Chemical Patents, Inc. Lubricating oil dispersants derived from heavy polyamine
US5792730A (en) 1994-07-11 1998-08-11 Exxon Chemical Patents, Inc. Lubricating oil succinimide dispersants derived from heavy polyamine
US5565128A (en) 1994-10-12 1996-10-15 Exxon Chemical Patents Inc Lubricating oil mannich base dispersants derived from heavy polyamine
US5891953A (en) 1996-02-09 1999-04-06 Exxon Chemical Patents Inc Process for preparing polyalkenyl substituted mono- and dicarboxylic acid producing materials (PT-1302)
US5777025A (en) 1996-02-09 1998-07-07 Exxon Chemical Patents Inc. Process for preparing polyalkenyl substituted C4 to C10 dicarboxylic acid producing materials
US6153565A (en) 1996-05-31 2000-11-28 Exxon Chemical Patents Inc Overbased metal-containing detergents
US6281179B1 (en) 1996-05-31 2001-08-28 Infineum Usa L.P. Process for preparing an overbased metal-containing detergents
US6429178B1 (en) 1996-05-31 2002-08-06 Infineum Usa L.P. Calcium overbased metal-containing detergents
WO2000071649A1 (fr) * 1999-05-19 2000-11-30 Infineum International Limited Composition d'huile lubrifiante contenant moins de 350 ppm de molybdene
US20020115575A1 (en) * 2000-12-22 2002-08-22 Antonio Gutierrez Lubricating oil composition
US20020115576A1 (en) * 2000-12-22 2002-08-22 Antonio Gutierrez Hydroxy aromatic mannich base condensation products and the use thereof as soot dispersants in lubricating oil compositions
US6495496B2 (en) 2000-12-22 2002-12-17 Infineum International Ltd. Hydroxy aromatic mannich base condensation products and the use thereof as soot dispersants in lubricating oil compositions
US6750183B2 (en) 2000-12-22 2004-06-15 Infineum International Ltd. Lubricating oil composition
US20050009998A1 (en) * 2001-12-19 2005-01-13 Rath Hans Peter Polyisobutene and polyisobutene derivatives for use in lubricant compositions
EP1361263A1 (fr) * 2002-05-07 2003-11-12 Chevron Texaco Japan Ltd. Composition d'huile lubrifiante
US20050070444A1 (en) * 2003-08-07 2005-03-31 Shaw Robert W. Lubricating oil composition
US20050043191A1 (en) * 2003-08-22 2005-02-24 Farng L. Oscar High performance non-zinc, zero phosphorus engine oils for internal combustion engines
US20050277559A1 (en) 2004-06-11 2005-12-15 Shaw Robert W Detergent additives for lubricating oil compositions
US20060189492A1 (en) 2005-02-18 2006-08-24 Bera Tushar K Soot dispersants and lubricating oil compositions containing same
US20060276353A1 (en) * 2005-06-01 2006-12-07 Irving Matthew D Lubricating oil composition
US20080194438A1 (en) 2007-02-08 2008-08-14 Bera Tushar K Soot Dispersants and Lubricating Oil Compositions Containing Same

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
W. W. YAU; J. J. KIRKLAND; D. D. BLY: "Modern Size Exclusion Liquid Chromatography", 1979, JOHN WILEY AND SONS
W.W. YAU; J.J KIRKLAND; D.D BLY: "Modern Size Exclusion Liquid Chromatography", 1979, JOHN WILEY AND SONS

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11268044B2 (en) 2015-07-23 2022-03-08 Total Marketing Services Long duration fuel economy lubricating composition
WO2017148835A1 (fr) * 2016-02-29 2017-09-08 Shell Internationale Research Maatschappij B.V. Composition lubrifiante

Also Published As

Publication number Publication date
ATE549389T1 (de) 2012-03-15
JP2009197230A (ja) 2009-09-03
US20090186784A1 (en) 2009-07-23
CA2650354A1 (fr) 2009-07-22
SG154416A1 (en) 2009-08-28
CN101492631A (zh) 2009-07-29
EP2083063B1 (fr) 2012-03-14

Similar Documents

Publication Publication Date Title
EP2083063B1 (fr) Utilisation d'une composition d'huile lubrifiante
EP1887076B1 (fr) Compositions d'huile lubrifiante
EP2940110B1 (fr) Compositions d'huile de lubrification
EP1398365B1 (fr) Compositions lubrifiantes pour des moteurs diesel pourvu d'un système RGE
EP1387066B1 (fr) Compositions lubrifiantes pour des moteurs diesels pourvus d'un système RGE
EP3369802B1 (fr) Améliorations apportées et relatives à des compositions de lubrification
EP1318189B1 (fr) Agents dispersants et composition lubrifiante les comportant
CA2413685C (fr) Agents dispersants et compositions d'huile lubrifiante contenant ces agents
US20220135899A1 (en) Lubricating Composition
CA2997166C (fr) Compositions de lubrification pour reduire le preallumage basse vitesse (lspi) dans les moteurs a combustion interne allumes par etincelle

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 20090114

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO SE SI SK TR

AX Request for extension of the european patent

Extension state: AL BA RS

17Q First examination report despatched

Effective date: 20090929

AKX Designation fees paid

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO SE SI SK TR

REG Reference to a national code

Ref country code: DE

Ref legal event code: R079

Ref document number: 602009005837

Country of ref document: DE

Free format text: PREVIOUS MAIN CLASS: C10M0169040000

Ipc: C10M0167000000

RIC1 Information provided on ipc code assigned before grant

Ipc: C10M 167/00 20060101AFI20111018BHEP

RTI1 Title (correction)

Free format text: USE OF A LUBRICATING OIL COMPOSITION

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO SE SI SK TR

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

REG Reference to a national code

Ref country code: AT

Ref legal event code: REF

Ref document number: 549389

Country of ref document: AT

Kind code of ref document: T

Effective date: 20120315

Ref country code: CH

Ref legal event code: EP

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

REG Reference to a national code

Ref country code: DE

Ref legal event code: R096

Ref document number: 602009005837

Country of ref document: DE

Effective date: 20120510

REG Reference to a national code

Ref country code: NL

Ref legal event code: T3

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20120314

Ref country code: NO

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20120614

Ref country code: HR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20120314

LTIE Lt: invalidation of european patent or patent extension

Effective date: 20120314

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LV

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20120314

Ref country code: GR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20120615

Ref country code: FI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20120314

REG Reference to a national code

Ref country code: AT

Ref legal event code: MK05

Ref document number: 549389

Country of ref document: AT

Kind code of ref document: T

Effective date: 20120314

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: CY

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20120314

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: EE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20120314

Ref country code: SE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20120314

Ref country code: IS

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20120714

Ref country code: PL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20120314

Ref country code: CZ

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20120314

Ref country code: RO

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20120314

Ref country code: SI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20120314

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: PT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20120716

Ref country code: SK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20120314

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20120314

Ref country code: AT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20120314

26N No opposition filed

Effective date: 20121217

REG Reference to a national code

Ref country code: DE

Ref legal event code: R097

Ref document number: 602009005837

Country of ref document: DE

Effective date: 20121217

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: ES

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20120625

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: BG

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20120614

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MC

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20130131

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

REG Reference to a national code

Ref country code: IE

Ref legal event code: MM4A

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20130131

Ref country code: LI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20130131

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20130114

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20120314

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: TR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20120314

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LU

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20130114

Ref country code: MK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20120314

Ref country code: HU

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT; INVALID AB INITIO

Effective date: 20090114

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 8

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 9

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: NL

Payment date: 20221220

Year of fee payment: 15

Ref country code: GB

Payment date: 20221214

Year of fee payment: 15

Ref country code: FR

Payment date: 20221216

Year of fee payment: 15

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: BE

Payment date: 20221220

Year of fee payment: 15

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: IT

Payment date: 20230116

Year of fee payment: 15

Ref country code: DE

Payment date: 20221215

Year of fee payment: 15

REG Reference to a national code

Ref country code: DE

Ref legal event code: R119

Ref document number: 602009005837

Country of ref document: DE

REG Reference to a national code

Ref country code: NL

Ref legal event code: MM

Effective date: 20240201

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 20240114

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20240801

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20240114

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: BE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20240131

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20240131

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20240201

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20240201

Ref country code: GB

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20240114

Ref country code: FR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20240131

Ref country code: DE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20240801

Ref country code: BE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20240131

REG Reference to a national code

Ref country code: BE

Ref legal event code: MM

Effective date: 20240131

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20240114