WO2018197312A1 - Lubricating composition - Google Patents
Lubricating composition Download PDFInfo
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- WO2018197312A1 WO2018197312A1 PCT/EP2018/059960 EP2018059960W WO2018197312A1 WO 2018197312 A1 WO2018197312 A1 WO 2018197312A1 EP 2018059960 W EP2018059960 W EP 2018059960W WO 2018197312 A1 WO2018197312 A1 WO 2018197312A1
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- nitrogen
- use according
- lubricating composition
- polymers
- ashless dispersant
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- 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
- C10M133/00—Lubricating compositions characterised by the additive being an organic non-macromolecular compound containing nitrogen
- C10M133/52—Lubricating compositions characterised by the additive being an organic non-macromolecular compound containing nitrogen having a carbon chain of 30 or more atoms
- C10M133/56—Amides; Imides
-
- 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
- C10M141/00—Lubricating compositions characterised by the additive being a mixture of two or more compounds covered by more than one of the main groups C10M125/00 - C10M139/00, each of these compounds being essential
- C10M141/10—Lubricating compositions characterised by the additive being a mixture of two or more compounds covered by more than one of the main groups C10M125/00 - C10M139/00, each of these compounds being essential at least one of them being an organic phosphorus-containing compound
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- 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
- C10M141/00—Lubricating compositions characterised by the additive being a mixture of two or more compounds covered by more than one of the main groups C10M125/00 - C10M139/00, each of these compounds being essential
- C10M141/12—Lubricating compositions characterised by the additive being a mixture of two or more compounds covered by more than one of the main groups C10M125/00 - C10M139/00, each of these compounds being essential at least one of them being an organic compound containing atoms of elements not provided for in groups C10M141/02 - C10M141/10
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- 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
- C10M169/00—Lubricating compositions characterised by containing as components a mixture of at least two types of ingredient selected from base-materials, thickeners or additives, covered by the preceding groups, each of these compounds being essential
- C10M169/04—Mixtures of base-materials and additives
-
- 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
- C10M2201/00—Inorganic compounds or elements as ingredients in lubricant compositions
- C10M2201/04—Elements
- C10M2201/041—Carbon; Graphite; Carbon black
-
- 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
- C10M2203/003—Organic non-macromolecular hydrocarbon compounds and hydrocarbon fractions as ingredients in lubricant compositions 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
- C10M2205/17—Fisher Tropsch reaction products
- C10M2205/173—Fisher Tropsch reaction products 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
- C10M2215/00—Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant compositions
- C10M2215/28—Amides; Imides
-
- 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
- C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
- C10N2030/04—Detergent property or dispersant property
- C10N2030/041—Soot induced viscosity control
-
- 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
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/25—Internal-combustion engines
Definitions
- the present invention relates to a lubricating oil composition, in particular to a lubricating oil
- Optimising lubricants through the use of high performance basestocks and novel additives represents a flexible solution to a growing challenge.
- Anti-wear additives are important to mitigate issues arising from the desire to have low viscosity
- a common anti-wear additive which is well known for use in lubricating compositions is a zinc
- dithiophosphate such as, for example, zinc dialkyl-, diaryl- or alkylaryl-dithiophosphates .
- dithiophosphate may be conveniently represented by general formula II:
- alkyl substituent containing from 1 to 20 carbon atoms preferably from 3 to 12 carbon atoms
- secondary alkyl group containing from 3 to 20 carbon atoms, preferably from 3 to 12 carbon atoms
- an aryl group or an aryl group substituted with an alkyl group said alkyl substituent containing from 1 to 20 carbon atoms
- Examples of suitable zinc dithiophosphates which are commercially available include those available ex.
- Oronite under the trade designation "OLOA 260”.
- the present invention provides the use of a nitrogen-containing ashless dispersant in a
- the nitrogen-containing ashless dispersant has a functionality (F) of greater than 1.4.
- soot contains polycyclic aromatic hydrocarbons (PAH) .
- PAH polycyclic aromatic hydrocarbons
- Soot is produced by the incomplete burning of organic matter, such as hydrocarbon based fuels. It consists of agglomerated nanoparticles with diameters between 6 and 30 nm.
- the soot particles can be mixed with metal oxides and with minerals and can be coated with sulfuric acid.
- soot can travel from the combustion chamber into the lubricant and can accumulate in the lubricant .
- the amount of soot in the lubricating composition containing the zinc dithiophosphate compound is typically at a level of from 0.1 wt% to 10 wt% . In one embodiment, the level of soot is from 2 to 7 wt%, by weight of the lubricating composition . In another embodiment, the level of soot is from 3.5 to 7 wt%, by weight of the lubricating
- the level of soot is from 5 to 6 wt%, by weight of the lubricating
- the nitrogen-containing ashless dispersant is present in the lubricating composition herein at a level so as to provide a level of nitrogen from 0.001 wt% to 0.15 wt%, preferably from 0.05 wt% to 0.1 wt%, by weight of the lubricating composition.
- the nitrogen-containing ashless dispersant is used herein to reduce the wear exhibited by a lubricating composition in the presence of zinc dithiophosphate compounds and soot .
- reducing wear means reducing the level of wear to a level below that exhibited by a lubricating composition which contains zinc dithiophosphate and soot but which does not contain the nitrogen-containing ashless dispersant described herein.
- the nitrogen- containing ashless dispersant is used to reduce the wear by at least 5%, more preferably by at least 10%, even more preferably by at least 50%, and especially by at least 80%, even more especially by at least 90%, compared with that of an analogous lubricating composition which contains zinc dithiophosphate and soot but which does not contain the nitrogen-containing ashless dispersant described herein.
- Suitable dispersants for use herein comprise an oil soluble polymeric long chain backbone having functional groups capable of associating with particles to be dispersed.
- such dispersants have amine, amine-alcohol or amide polar moieties attached to the polymer backbone, often via a bridging group.
- the dispersant may be, for example, selected from oil soluble salts, esters, amino-esters , amides, imides and
- 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 used in 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 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 used in 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
- 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-l, decene-1,
- dodecene-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 used herein may contain a minor amount, e.g. 0.5 to 5 mole % of a C4 to Cis non- conjugated diolefin comonomer.
- the polymers used in the present 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 C3 to C28 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.
- ethenylidene unsaturation may be determined by FTIR spectroscopic analysis, titration, or C 13 NMR.
- R 1 is Ci to C 2 e alkyl, preferably Ci to Cis alkyl, more preferably Ci to Ce alkyl, and most preferably Ci to C2 alkyl, (e.g., methyl or ethyl) and wherein POLY represents the polymer chain.
- the chain length of the R 1 alkyl group will vary
- R 1 is as defined above.
- 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 C4 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
- a preferred source of monomer for making poly-n-butenes is petroleum feedstreams such as Raffinate
- polyisobutylene is a most preferred backbone herein because it is readily available by cationic polymerization from butene streams (e.g., using AICI3 or BF3 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 under the tradenames
- GlissopalTM from BASF
- UltravisTM 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
- the hydrocarbon or polymer backbone can be any hydrocarbon or polymer backbone.
- 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
- Selective functionalization can be accomplished by halogenating, e.g., chlorinating or brominating the unsaturated oc-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.
- 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
- the 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 .
- the backbone and the monounsaturated functionality reactant e.g., carboxylic reactant
- the backbone and the monounsaturated functionality 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 any hydrocarbon or polymer backbone.
- 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 used in 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 C4 to Cio dicarboxylic acid wherein (a) the carboxyl groups are vicinyl, (i.e., located on adjacent carbon atoms) and (b) at least one, preferably both, of said adjacent carbon atoms are part of said mono unsaturation; (ii)
- monounsaturated carboxylic reactants are fumaric acid, itaconic acid, maleic acid, maleic anhydride,
- chloromaleic acid chloromaleic anhydride, acrylic acid, methacrylic acid, crotonic acid, cinnamic acid, and lower alkyl (e.g., Ci to C4 alkyl) acid esters of the
- methyl maleate e.g., methyl maleate, ethyl fumarate, and methyl fumarate.
- 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, amino-alcohol, amide, or mixture thereof, to form a corresponding derivative.
- a nitrogen-containing nucleophilic reactant such as an amine, amino-alcohol, 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
- 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.
- 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;
- polyethylene tetramine triethylene tetramine
- tetraethylene pentamine polypropyleneamines
- polypropyleneamines such as 1 , 2-propylene diamine; and di- ( 1 , 2-propylene ) triamine .
- Such polyamine mixtures are commercially available.
- 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 for use herein 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 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
- the preferred dispersants for use herein have a Functionality (F) of greater than 1.4, more preferably greater than 1.5, such as from about 1.5 to about 2.2, more preferably from about 1.5 to about 2.0 or from about 1.5 to about 1.9.
- Functionality (F) can be determined according to the following formula:
- SAP saponification number (i.e., the number of milligrams of KOH consumed in the complete neutralization of the acid groups in one gram of the succinic-containing reaction product, as determined according to ASTM D94); M n is the number average
- polybutene A.I. is the percent active ingredient of the succinic-containing reaction product (the remainder being unreacted polybutene and diluent); and MW is the molecular weight of the dicarboxylic acid-producing moiety (98 for maleic anhydride) .
- each dicarboxylic acid-producing moiety succinic group
- PIBSA nucleophilic group
- Polymer molecular weight 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) .
- Another useful method for determining molecular weight, particularly for lower molecular weight polymers is vapor pressure osmometry (see, e.g., ASTM D 3592 ) .
- Suitable hydrocarbons or polymers employed in the formation of the dispersants include polymers prepared by cationic polymerization of isobutene.
- Common polymers from this class include polyisobutenes obtained by polymerization of a C4 refinery stream having a butene content of about 35 to about 75% by wt . , and an isobutene content of about 30 to about 60% by wt . , in the presence of a Lewis acid catalyst, such boron trifluoride (BF3) .
- a Lewis acid catalyst such boron trifluoride (BF3)
- the polyisobutylene is 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 60%, 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.
- Such polymers are conventionally referred to as HR-PIB and HR-PIB is commercially available from Texas Petrochemical
- monounsaturated carboxylic reactant typically will be used in an amount ranging from about 5 to about 300 % excess, preferably from about 10 to 200 %, such as 20 to 100 % excess, based on the moles of polymer. Unreacted excess monounsaturated carboxylic reactant can be removed from the final dispersant product by, for example, stripping, under vacuum, if required.
- dispersants include polyamines having, or having on average, 3 to 8 nitrogen atoms per molecule, preferably from about 5 to about 8 nitrogen atoms per molecule.
- These amines may be hydrocarbyl amines or may be
- hydrocarbyl group includes other groups, e.g., hydroxy groups, alkoxy groups, amide groups, nitriles, imidazoline groups, and the like.
- 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, polyethylene amines such as diethylene triamine; triethylene
- polypropyleneamines such as di- ( 1 , 2-propylene ) triamine .
- PAM polyamine mixtures
- Useful polyamine mixtures also include mixtures derived by distilling the light ends from PAM products.
- the resulting mixtures known as "heavy" PAM, or HPAM, are also commercially available.
- the properties and attributes of both PAM and/or HPAM are described, for example, in U.S. Patent Nos . 4,938,881; 4,927,551;
- the total amount of base oil incorporated in the lubricating oil composition of the present invention is preferably present in an amount in the range of from 60 to 92 wt . %, more preferably in an amount in the range of from 75 to 90 wt . % and most preferably in an amount in the range of from 75 to 88 wt . %, with respect to the total weight of the lubricating oil composition.
- base oil used in the present invention there are no particular limitations regarding the base oil used in the present invention, and various conventional known mineral oils and synthetic oils may be conveniently used.
- the base oil used in the present invention may conveniently comprise mixtures of one or more mineral oils and/or one or more synthetic oils.
- Mineral oils include liquid petroleum oils and solvent-treated or acid-treated mineral lubricating oils of the paraffinic, naphthenic, or mixed
- paraffinic/naphthenic type which may be further refined by hydrofinishing processes and/or dewaxing.
- Naphthenic base oils have low viscosity index (VI) (generally 40-80) and a low pour point.
- Such base oils are produced from feedstocks rich in naphthenes and low in wax content and are used mainly for lubricants in which colour and colour stability are important, and VI and oxidation stability are of secondary importance.
- Paraffinic base oils have higher VI (generally >95) and a high pour point. Said base oils are produced from feedstocks rich in paraffins, and are used for lubricants in which VI and oxidation stability are important.
- Fischer-Tropsch derived base oils may be
- the base oil in the lubricating oil composition of the present invention for example, the Fischer-Tropsch derived base oils disclosed in EP-A-
- Synthetic processes enable molecules to be built from simpler substances or to have their structures modified to give the precise properties required.
- dibasic acids esters dibasic acids esters
- polyol esters polyol esters
- dewaxed waxy raffinate dewaxed waxy raffinate
- hydrocarbon base oils sold by the Royal Dutch/Shell Group of Companies under the designation "XHVI” (trade mark) may be conveniently used.
- the base oil comprises mineral oils and/or synthetic oils which contain more than 80% wt of saturates, preferably more than 90 % wt . , as measured according to ASTM D2007.
- the base oil contains less than 1.0 wt . %, preferably less than 0.1 wt . % of sulphur, calculated as elemental sulphur and measured according to ASTM D2622, ASTM D4294, ASTM D4927 or ASTM D3120.
- the viscosity index of the base fluid is more than 80, more preferably more than 120, as measured according to ASTM D2270.
- the lubricating oil composition has a kinematic viscosity in the range of from 2 to 80 mm 2 /s at 100 °C, more preferably of from 3 to 70 mm 2 /s, most preferably of from 4 to 50 mm 2 /s.
- the total amount of phosphorus in the lubricating oil composition of the present invention is preferably in the range of from 0.04 to 0.12 wt . %, more preferably in the range of from 0.04 to 0.09 wt . % and most preferably in the range of from 0.045 to 0.08 wt . %, based on total weight of the lubricating oil composition.
- the lubricating oil composition of the present invention preferably has a sulphated ash content of not greater than 2.0 wt . %, more preferably not greater than
- the lubricating oil composition of the present invention preferably has a sulphur content of not greater than 1.2 wt . %, more preferably not greater than 0.8 wt . % and most preferably not greater than 0.2 wt . %, based on the total weight of the lubricating oil
- the lubricating oil composition of the present invention may further comprise additional additives such as anti-oxidants , anti-wear additives, detergents, dispersants, friction modifiers, viscosity index
- Antioxidants that may be conveniently used include those selected from the group of aminic antioxidants and/or phenolic antioxidants.
- said antioxidants are present in an amount in the range of from 0.1 to 5.0 wt . %, more preferably in an amount in the range of from 0.3 to 3.0 wt . %, and most preferably in an amount in the range of from 0.5 to 1.5 wt . %, based on the total weight of the lubricating oil composition.
- alkylated diphenylamines phenyl-a-naphthylamines, phenyl--naphthylamines and alkylated a-naphthylamines .
- Preferred aminic antioxidants include
- dialkyldiphenylamines such as p, p ' -dioctyl-diphenylamine, p, p ' -di-OC-methylbenzyl-diphenylamine and N-p-butylphenyl- N-p ' -octylphenylamine, monoalkyldiphenylamines such as mono-t-butyldiphenylamine and mono-octyldiphenylamine, bis (dialkylphenyl) amines such as di-(2,4- diethylphenyl) amine and di (2-ethyl-4-nonylphenyl) amine, alkylphenyl-l-naphthylamines such as octylphenyl-1- naphthylamine and n-t-dodecylphenyl-l-naphthylamine, 1- naphthylamine, arylnap
- phenylenediamines such as N, N ' -diisopropyl-p- phenylenediamine and N, ' -diphenyl-p-phenylenediamine, and phenothiazines such as phenothiazine and 3,7- dioctylphenothiazine .
- Preferred aminic antioxidants include those available under the following trade designations: “Sonoflex OD-3” (ex. Seiko Kagaku Co.), “Irganox L-57” (ex. Ciba).
- phenolic antioxidants which may be conveniently used include C7-C9 branched alkyl esters of
- 2.6-di-t-butyl-4-alkoxyphenols such as 2, 6-di-t-butyl-4- methoxyphenol and 2, 6-di-t-butyl-4-ethoxyphenol, 3,5-di-t- butyl-4-hydroxybenzylmercaptooctylacetate, alkyl-3- (3, 5- di-t-butyl-4-hydroxyphenyl) propionates such as n- octadecyl-3- (3, 5-di-t-butyl-4-hydroxyphenyl) propionate, n- butyl-3- (3, 5-di-t-butyl-4-hydroxyphenyl) propionate and 2'- ethylhexyl-3- (3, 5-di-t-butyl-4-hydroxyphenyl) propionate,
- 2, 6-d-t-butyl-a-dimethylamino-p-cresol 2,2' -methylene- bis (4-alkyl-6-t-butylphenol) such as 2, 2 ' -methylenebis (4- methyl-6-t-butylphenol, and 2, 2-methylenebis (4-ethyl-6-t- butylphenol) , bisphenols such as 4 , 4 ' -butylidenebis ( 3- methyl-6-t-butylphenol, 4,4' -methylenebis (2, 6-di-t- butylphenol) , 4 , 4 ' -bis (2 , 6-di-t-butylphenol ) , 2,2-(di-p- hydroxyphenyl) propane, 2, 2-bis (3, 5-di-t-butyl-4- hydroxyphenyl) propane, 4 , 4 ' -cyclohexylidenebis (2, 6-t- butylphenol) , hexamethyleneglycol-bis [
- Preferred phenolic antioxidants include those available under the following trade designations: "Irganox
- the lubricating oil composition of the present invention may comprise mixtures of one or more phenolic antioxidants with one or more aminic antioxidants.
- the lubricating oil composition may comprise a single zinc dithiophosphate or a combination of two or more zinc dithiophosphates as anti-wear additives, the or each zinc dithiophosphate being selected from zinc dialkyl-, diaryl- or alkylaryl- dithiophosphates .
- the zinc dithiophosphate compounds are present in the lubricating composition in an amount so as to provide preferably from 0.01 wt% to 0.16 wt%, more preferably from 0.06% to 0.12%, by weight of the lubricating composition, of phosphorus.
- Zinc dithiophosphate is a well known additive in the art and may be conveniently represented by general formula II;
- R2 to may be the same or different and are each a primary alkyl group containing from 1 to 20 carbon atoms preferably from 3 to 12 carbon atoms, a secondary alkyl group containing from 3 to 20 carbon atoms, preferably from 3 to 12 carbon atoms, an aryl group or an aryl group substituted with an alkyl group, said alkyl substituent containing from 1 to 20 carbon atoms
- Zinc dithiophosphate compounds in which R2 to are all different from each other can be used alone or in admixture with zinc dithiophosphate compounds in which R 2 to R 5 are all the same.
- the or each zinc dithiophosphate used in the present invention is a zinc dialkyl dithiophosphate.
- Examples of suitable zinc dithiophosphates which are commercially available include those available ex.
- Oronite under the trade designation "OLOA 260”.
- the lubricating oil composition according to the present invention may generally comprise in the range of from 0.4 to 1.2 wt . % of zinc dithiophosphate, based on total weight of the lubricating oil composition.
- composition of the present invention may be conveniently used in the composition of the present invention .
- lubricating oil of the present invention include one or more salicylate and/or phenate and/or sulphonate
- metal organic and inorganic base salts which are used as detergents can contribute to the sulphated ash content of a lubricating oil composition, in a preferred embodiment of the present invention, the amounts of such additives are minimised.
- salicylate detergents are preferred.
- the lubricating oil composition of the present invention may comprise one or more salicylate detergents.
- said detergents are preferably used in amounts in the range of 0.05 to 20.0 wt . %, more
- lubricating oil composition preferably from 1.0 to 10.0 wt . % and most preferably in the range of from 2.0 to 5.0 wt . %, based on the total weight of the lubricating oil composition.
- said detergents independently, have a TBN (total base number) value in the range of from 10 to 500 mg.KOH/g, more preferably in the range of from 30 to 350 mg.KOH/g and most preferably in the range of from 50 to 300 mg.KOH/g, as measured by
- viscosity index improvers which may be conveniently used in the lubricating oil composition of the present invention include the styrene-butadiene copolymers, styrene-isoprene stellate copolymers and the polymethacrylate copolymer and ethylene-propylene copolymers .
- Such viscosity index improvers may be conveniently employed in an amount in the range of from 1 to 20 wt . %, based on the total weight of the lubricating oil composition.
- Polymethacrylates may be conveniently employed in the lubricating oil compositions of the present invention as effective pour point depressants.
- polycyclohexane and polyacrylates may be conveniently used in the lubricating oil composition of the present
- seal fix or seal compatibility agents include, for example, commercially available aromatic esters.
- the lubricating compositions herein may be any suitable lubricating compositions herein.
- Various lubricating compositions were prepared by combining a base oil (GTL 4, a Fischer-Tropsch derived base oil having a kinematic viscosity at 100°C of
- the formulations also contained a nitrogen-containing ashless dispersant (designated as Dl, D2, D3 or D4 in Table 1 below) in varying amounts to give lubricating compositions having varying amounts of nitrogen (0.05wt% N, 0.07wt%N or
- compositions in an amount of 5wt%, by weight of the final lubricating compositions, in order to simulate the effect of the presence of soot in the lubricant.
- the nitrogen-containing ashless dispersants used in the present examples were polyisobutylene succinimides having the properties listed below in Table 1:
- the lubricant formulations were subjected to a HFRR wear test.
- the HFRR High-Friction_Reciprocating Rig
- the test uses a 6 mm diameter steel ball loaded and reciprocated against the flat surface of a stationary steel disc immersed in lubricant . At the end of each test, the ball and disc were removed from the test rig, rinsed with toluene and iso-propanol, and then treated with a 0.05 wt% solution of
- EDTA ethylenediaminetetraacetic acid
- Topography images were then obtained and analysed to determine wear volumes of the wear scars on the ball and the disc using the SWLI Veeco Wyko model NT9100.
- the instrument was set in Vertical Scanning Interferometry (VSI) mode, calibrated to measure rough surfaces with a nanometre detection range.
- VSI Vertical Scanning Interferometry
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
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- Organic Chemistry (AREA)
- Lubricants (AREA)
Abstract
Description
Claims
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
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JP2019557584A JP2020517787A (en) | 2017-04-27 | 2018-04-18 | Lubricating composition |
RU2019138210A RU2768169C2 (en) | 2017-04-27 | 2018-04-18 | Lubricating composition |
EP18724139.3A EP3615641B1 (en) | 2017-04-27 | 2018-04-18 | Use of a dispersant in a lubricating composition |
BR112019022507-2A BR112019022507B1 (en) | 2017-04-27 | 2018-04-18 | USE OF AN ASHLESS DISPERSANT CONTAINING NITROGEN IN A LUBRICANT COMPOSITION |
US16/607,927 US20200095516A1 (en) | 2017-04-27 | 2018-04-18 | Lubricating composition |
CN201880026896.7A CN110546243B (en) | 2017-04-27 | 2018-04-18 | Lubricating composition |
Applications Claiming Priority (2)
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EP17168538.1 | 2017-04-27 | ||
EP17168538 | 2017-04-27 |
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PCT/EP2018/059960 WO2018197312A1 (en) | 2017-04-27 | 2018-04-18 | Lubricating composition |
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US (1) | US20200095516A1 (en) |
EP (1) | EP3615641B1 (en) |
JP (1) | JP2020517787A (en) |
CN (1) | CN110546243B (en) |
BR (1) | BR112019022507B1 (en) |
RU (1) | RU2768169C2 (en) |
WO (1) | WO2018197312A1 (en) |
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CN112368359B (en) | 2018-07-02 | 2023-03-28 | 国际壳牌研究有限公司 | Liquid fuel composition |
Citations (53)
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 |
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 |
US3565804A (en) | 1965-08-23 | 1971-02-23 | Chevron Res | Lubricating oil additives |
US3912764A (en) | 1972-09-29 | 1975-10-14 | Cooper Edwin Inc | Preparation of alkenyl succinic anhydrides |
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 |
US4178258A (en) * | 1978-05-18 | 1979-12-11 | Edwin Cooper, Inc. | Lubricating oil composition |
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 |
EP0208560A2 (en) | 1985-07-11 | 1987-01-14 | Exxon Chemical Patents Inc. | Oil-soluble dispersant additives in fuels and lubricating oils |
US4857217A (en) | 1987-11-30 | 1989-08-15 | Exxon Chemical Patents Inc. | Dispersant additives derived from amido-amines |
EP0355895A2 (en) | 1988-08-05 | 1990-02-28 | Shell Internationale Researchmaatschappij B.V. | Process for the preparation of succinic anhydride derivatives |
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 (en) | 1989-02-07 | 1995-06-13 | Exxon Chemical Patents Inc. | Low temperature method for the production of long chain hydrocarbyl substituted mono- or dicarboxylic acid materials employing plural zone mixing |
EP0382450B1 (en) | 1989-02-07 | 1995-06-28 | Exxon Chemical Patents Inc. | Method for the production of long chain hydrocarbyl substituted mono-or dicarboxylic acid materials |
EP0668342A1 (en) | 1994-02-08 | 1995-08-23 | Shell Internationale Researchmaatschappij B.V. | Lubricating base oil preparation process |
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 |
EP0776959A2 (en) | 1995-11-28 | 1997-06-04 | Shell Internationale Researchmaatschappij B.V. | Process for producing lubricating base oils |
WO1997021788A1 (en) | 1995-12-08 | 1997-06-19 | Exxon Research And Engineering Company | Biodegradable high performance hydrocarbon base oils |
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) |
WO1999041332A1 (en) | 1998-02-13 | 1999-08-19 | Exxon Research And Engineering Company | Low viscosity lube basestock |
WO2000008115A1 (en) | 1998-08-04 | 2000-02-17 | Exxon Research And Engineering Company | A lubricant base oil having improved oxidative stability |
WO2000014188A2 (en) | 1998-09-04 | 2000-03-16 | Exxon Research And Engineering Company | Premium wear resistant lubricant |
WO2000014187A2 (en) | 1998-09-04 | 2000-03-16 | Exxon Research And Engineering Company | Premium synthetic lubricants |
WO2000014179A1 (en) | 1998-09-04 | 2000-03-16 | Exxon Research And Engineering Company | Premium synthetic lubricant base stock |
WO2000014183A1 (en) | 1998-09-04 | 2000-03-16 | Exxon Research And Engineering Company | Production on synthetic lubricant and lubricant base stock without dewaxing |
WO2000015736A2 (en) | 1998-09-11 | 2000-03-23 | Exxon Research And Engineering Company | Wide-cut synthetic isoparaffinic lubricating oils |
EP1029029A1 (en) | 1997-10-20 | 2000-08-23 | Mobil Oil Corporation | Isoparaffinic lube basestock compositions |
WO2001018156A1 (en) | 1999-09-08 | 2001-03-15 | Total Raffinage Distribution S.A. | Novel hydrocarbon base oil for lubricants with very high viscosity index |
WO2001057166A1 (en) | 2000-02-04 | 2001-08-09 | Mobil Oil Corporation | Formulated lubricant oils containing high-performance base oils derived from highly paraffinic hydrocarbons |
US20050124509A1 (en) * | 2003-12-04 | 2005-06-09 | Antonio Gutierrez | Lubricating oil compositions |
Family Cites Families (23)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4863624A (en) * | 1987-09-09 | 1989-09-05 | Exxon Chemical Patents Inc. | Dispersant additives mixtures for oleaginous compositions |
US4767551A (en) * | 1985-12-02 | 1988-08-30 | Amoco Corporation | Metal-containing lubricant compositions |
CA1333596C (en) * | 1986-10-16 | 1994-12-20 | Robert Dean Lundberg | High functionality low molecular weight oil soluble dispersant additives useful in oleaginous compositions |
US4889646A (en) * | 1987-06-30 | 1989-12-26 | Amoco Corporation | Nitrogen containing dispersants treated with mineral acids |
US5035821A (en) * | 1988-07-18 | 1991-07-30 | Exxon Chemical Patents Inc. | End-capped multifunctional viscosity index improver |
CA2090200C (en) * | 1992-03-20 | 2005-04-26 | Chung Y. Lai | Ashless dispersant polymethacrylate polymers |
US5968880A (en) * | 1997-10-23 | 1999-10-19 | The Lubrizol Corporation | Lubricating compositions, functional fluids and greases containing thiophosphorus esters or their salts with a oxyalkylene group, and methods of using the same |
EP1151994A1 (en) * | 2000-05-01 | 2001-11-07 | Ethyl Corporation | Succinimide-acid compounds and derivatives thereof |
US6750183B2 (en) * | 2000-12-22 | 2004-06-15 | Infineum International Ltd. | Lubricating oil composition |
US6734148B2 (en) * | 2001-12-06 | 2004-05-11 | Infineum International Ltd. | Dispersants and lubricating oil compositions containing same |
US6743757B2 (en) * | 2001-12-06 | 2004-06-01 | Infineum International Ltd. | Dispersants and lubricating oil compositions containing same |
JP4038388B2 (en) * | 2002-05-07 | 2008-01-23 | 新日本石油株式会社 | Engine oil composition |
ATE521686T1 (en) * | 2004-09-07 | 2011-09-15 | Infineum Int Ltd | LUBRICANT OIL COMPOSITION |
US8361940B2 (en) * | 2006-09-26 | 2013-01-29 | Chevron Japan Ltd. | Low sulfated ash, low sulfur, low phosphorus, low zinc lubricating oil composition |
US7786057B2 (en) * | 2007-02-08 | 2010-08-31 | Infineum International Limited | Soot dispersants and lubricating oil compositions containing same |
JP5101915B2 (en) * | 2007-03-27 | 2012-12-19 | Jx日鉱日石エネルギー株式会社 | Lubricating oil composition for diesel engines |
JP4964014B2 (en) * | 2007-04-23 | 2012-06-27 | コスモ石油ルブリカンツ株式会社 | Engine oil composition |
JP5764326B2 (en) * | 2007-05-24 | 2015-08-19 | ザ ルブリゾル コーポレイションThe Lubrizol Corporation | Lubricating aluminum silicate composite surfaces with lubricants containing ashless, sulfur-free, and phosphorus-free wear agents |
JP5079407B2 (en) * | 2007-06-28 | 2012-11-21 | シェブロンジャパン株式会社 | Lubricating oil composition for lubricating fuel-saving diesel engines |
US9181511B2 (en) * | 2009-04-01 | 2015-11-10 | Infineum International Limited | Lubricating oil composition |
US9574158B2 (en) * | 2014-05-30 | 2017-02-21 | Afton Chemical Corporation | Lubricating oil composition and additive therefor having improved wear properties |
US9926509B2 (en) * | 2015-01-19 | 2018-03-27 | Exxonmobil Research And Engineering Company | Lubricating oil compositions with engine wear protection and solubility |
US10472584B2 (en) * | 2015-07-30 | 2019-11-12 | Infineum International Ltd. | Dispersant additives and additive concentrates and lubricating oil compositions containing same |
-
2018
- 2018-04-18 EP EP18724139.3A patent/EP3615641B1/en active Active
- 2018-04-18 US US16/607,927 patent/US20200095516A1/en not_active Abandoned
- 2018-04-18 WO PCT/EP2018/059960 patent/WO2018197312A1/en unknown
- 2018-04-18 BR BR112019022507-2A patent/BR112019022507B1/en active IP Right Grant
- 2018-04-18 CN CN201880026896.7A patent/CN110546243B/en active Active
- 2018-04-18 JP JP2019557584A patent/JP2020517787A/en active Pending
- 2018-04-18 RU RU2019138210A patent/RU2768169C2/en active
Patent Citations (59)
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 |
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 |
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 |
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 |
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 |
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 |
US4178258A (en) * | 1978-05-18 | 1979-12-11 | Edwin Cooper, Inc. | Lubricating oil composition |
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 |
US5230714A (en) | 1985-03-14 | 1993-07-27 | The Lubrizol Corporation | High molecular weight nitrogen-containing condensates and fuels and lubricants containing same |
US5053152A (en) | 1985-03-14 | 1991-10-01 | The Lubrizol Corporation | High molecular weight nitrogen-containing condensates and fuels and lubricants containing same |
EP0208560A2 (en) | 1985-07-11 | 1987-01-14 | Exxon Chemical Patents Inc. | Oil-soluble dispersant additives in fuels and lubricating oils |
US4963275A (en) | 1986-10-07 | 1990-10-16 | Exxon Chemical Patents Inc. | Dispersant additives derived from lactone modified amido-amine adducts |
US4956107A (en) | 1987-11-30 | 1990-09-11 | Exxon Chemical Patents Inc. | Amide dispersant additives derived from amino-amines |
US4857217A (en) | 1987-11-30 | 1989-08-15 | Exxon Chemical Patents Inc. | Dispersant additives derived from amido-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) |
EP0355895A2 (en) | 1988-08-05 | 1990-02-28 | Shell Internationale Researchmaatschappij B.V. | Process for the preparation of succinic anhydride derivatives |
US4952739A (en) | 1988-10-26 | 1990-08-28 | Exxon Chemical Patents Inc. | Organo-Al-chloride catalyzed poly-n-butenes process |
CA1335895C (en) | 1989-02-07 | 1995-06-13 | Exxon Chemical Patents Inc. | Low temperature method for the production of long chain hydrocarbyl substituted mono- or dicarboxylic acid materials employing plural zone mixing |
EP0382450B1 (en) | 1989-02-07 | 1995-06-28 | Exxon Chemical Patents Inc. | Method for the production of long chain hydrocarbyl substituted mono-or dicarboxylic acid materials |
US5241003A (en) | 1990-05-17 | 1993-08-31 | Ethyl Petroleum Additives, Inc. | Ashless dispersants formed from substituted acylating agents and their production and use |
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 |
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 |
US6022929A (en) | 1992-12-17 | 2000-02-08 | Exxon Chemical Patents Inc. | Amorphous olefin polymers, copolymers, methods of preparation and derivatives thereof |
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 |
US5814715A (en) | 1992-12-17 | 1998-09-29 | Exxon Chemical Patents Inc | Amorphous olefin polymers, copolymers, methods of preparation and derivatives thereof |
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 |
EP0668342A1 (en) | 1994-02-08 | 1995-08-23 | Shell Internationale Researchmaatschappij B.V. | Lubricating base oil preparation process |
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 |
EP0776959A2 (en) | 1995-11-28 | 1997-06-04 | Shell Internationale Researchmaatschappij B.V. | Process for producing lubricating base oils |
WO1997021788A1 (en) | 1995-12-08 | 1997-06-19 | Exxon Research And Engineering Company | Biodegradable high performance hydrocarbon base oils |
US5777025A (en) | 1996-02-09 | 1998-07-07 | Exxon Chemical Patents Inc. | Process for preparing polyalkenyl substituted C4 to C10 dicarboxylic acid producing materials |
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) |
EP1029029A1 (en) | 1997-10-20 | 2000-08-23 | Mobil Oil Corporation | Isoparaffinic lube basestock compositions |
WO1999041332A1 (en) | 1998-02-13 | 1999-08-19 | Exxon Research And Engineering Company | Low viscosity lube basestock |
WO2000008115A1 (en) | 1998-08-04 | 2000-02-17 | Exxon Research And Engineering Company | A lubricant base oil having improved oxidative stability |
WO2000014188A2 (en) | 1998-09-04 | 2000-03-16 | Exxon Research And Engineering Company | Premium wear resistant lubricant |
WO2000014187A2 (en) | 1998-09-04 | 2000-03-16 | Exxon Research And Engineering Company | Premium synthetic lubricants |
WO2000014179A1 (en) | 1998-09-04 | 2000-03-16 | Exxon Research And Engineering Company | Premium synthetic lubricant base stock |
WO2000014183A1 (en) | 1998-09-04 | 2000-03-16 | Exxon Research And Engineering Company | Production on synthetic lubricant and lubricant base stock without dewaxing |
WO2000015736A2 (en) | 1998-09-11 | 2000-03-23 | Exxon Research And Engineering Company | Wide-cut synthetic isoparaffinic lubricating oils |
WO2001018156A1 (en) | 1999-09-08 | 2001-03-15 | Total Raffinage Distribution S.A. | Novel hydrocarbon base oil for lubricants with very high viscosity index |
WO2001057166A1 (en) | 2000-02-04 | 2001-08-09 | Mobil Oil Corporation | Formulated lubricant oils containing high-performance base oils derived from highly paraffinic hydrocarbons |
US20050124509A1 (en) * | 2003-12-04 | 2005-06-09 | Antonio Gutierrez | Lubricating oil compositions |
Non-Patent Citations (6)
Title |
---|
DIATTO P ET AL: "Investigation on soot dispersant properties and wear effects in the boundary lubrication regime", TRIBOLOGY SE, ELSEVIER, AMSTERDAM, NL, vol. 36, 1 January 1999 (1999-01-01), pages 809 - 819, XP009176692, ISSN: 0167-8922, DOI: 10.1016/S0167-8922(99)80099-6 * |
M. RATOI ET AL: "The influence of soot and dispersant on ZDDP film thickness and friction", LUBRICATION SCIENCE, vol. 17, no. 1, 1 November 2004 (2004-11-01), US, pages 25 - 43, XP055414046, ISSN: 0954-0075, DOI: 10.1002/ls.3010170103 * |
OLOMOLEHIN, Y.; KAPADIA, R.G.; SPIKES, H.A.: "Antagonistic interaction of antiwear additives and carbon black", TRIB LETTERS, vol. 37, 2009, pages 49 - 58, XP019775039 |
SALEHI, F. MOTAMEN; D.N. KHAEMBA; A. MORINA; A. NEVILLE: "Corrosive-Abrasive Wear Induced by Soot in Boundary Lubrication Regime", TRIB LETTERS, vol. 63, 2016, pages 1 - 11, XP036012445, DOI: doi:10.1007/s11249-016-0704-9 |
W. W. YAU; J. J. KIRKLAND; D. D. BLY: "Modern Size Exclusion Liquid Chromatography", 1979, JOHN WILEY AND SONS |
YEWANDE OLOMOLEHIN ET AL: "Antagonistic Interaction of Antiwear Additives and Carbon Black", TRIBOLOGY LETTERS, KLUWER ACADEMIC PUBLISHERS-PLENUM PUBLISHERS, NE, vol. 37, no. 1, 28 July 2009 (2009-07-28), pages 49 - 58, XP019775039, ISSN: 1573-2711 * |
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