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US3272746A - Lubricating composition containing an acylated nitrogen compound - Google Patents

Lubricating composition containing an acylated nitrogen compound Download PDF

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Publication number
US3272746A
US3272746A US509172A US50917265A US3272746A US 3272746 A US3272746 A US 3272746A US 509172 A US509172 A US 509172A US 50917265 A US50917265 A US 50917265A US 3272746 A US3272746 A US 3272746A
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Prior art keywords
grams
nitrogen
mixture
acid
product
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US509172A
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Suer William M Le
George R Norman
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Lubrizol Corp
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Lubrizol Corp
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    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D207/00Heterocyclic compounds containing five-membered rings not condensed with other rings, with one nitrogen atom as the only ring hetero atom
    • C07D207/02Heterocyclic compounds containing five-membered rings not condensed with other rings, with one nitrogen atom as the only ring hetero atom with only hydrogen or carbon atoms directly attached to the ring nitrogen atom
    • C07D207/30Heterocyclic compounds containing five-membered rings not condensed with other rings, with one nitrogen atom as the only ring hetero atom with only hydrogen or carbon atoms directly attached to the ring nitrogen atom having two double bonds between ring members or between ring members and non-ring members
    • C07D207/34Heterocyclic compounds containing five-membered rings not condensed with other rings, with one nitrogen atom as the only ring hetero atom with only hydrogen or carbon atoms directly attached to the ring nitrogen atom having two double bonds between ring members or between ring members and non-ring members with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
    • C07D207/36Oxygen or sulfur atoms
    • C07D207/402,5-Pyrrolidine-diones
    • C07D207/4042,5-Pyrrolidine-diones with only hydrogen atoms or radicals containing only hydrogen and carbon atoms directly attached to other ring carbon atoms, e.g. succinimide
    • C07D207/408Radicals containing only hydrogen and carbon atoms attached to ring carbon atoms
    • C07D207/412Acyclic radicals containing more than six carbon atoms
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    • C10M133/00Lubricating compositions characterised by the additive being an organic non-macromolecular compound containing nitrogen
    • C10M133/52Lubricating compositions characterised by the additive being an organic non-macromolecular compound containing nitrogen having a carbon chain of 30 or more atoms
    • C10M133/56Amides; Imides
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    • C10M2205/00Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions
    • C10M2205/02Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions containing acyclic monomers
    • C10M2205/026Butene
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    • C10M2207/40Fatty vegetable or animal oils
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    • C10M2209/02Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • C10M2209/08Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing monomers having an unsaturated radical bound to a carboxyl radical, e.g. acrylate type
    • C10M2209/084Acrylate; Methacrylate
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    • C10M2215/00Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant compositions
    • C10M2215/02Amines, e.g. polyalkylene polyamines; Quaternary amines
    • C10M2215/04Amines, e.g. polyalkylene polyamines; Quaternary amines having amino groups bound to acyclic or cycloaliphatic carbon atoms
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    • C10M2215/00Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant compositions
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    • C10M2215/082Amides containing hydroxyl groups; Alkoxylated derivatives
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    • C10M2215/102Ureas; Semicarbazides; Allophanates
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    • C10M2217/02Macromolecular compounds obtained from nitrogen containing monomers by reactions only involving carbon-to-carbon unsaturated bonds
    • C10M2217/022Macromolecular compounds obtained from nitrogen containing monomers by reactions only involving carbon-to-carbon unsaturated bonds containing monomers having an unsaturated radical bound to an amino group
    • C10M2217/023Macromolecular compounds obtained from nitrogen containing monomers by reactions only involving carbon-to-carbon unsaturated bonds containing monomers having an unsaturated radical bound to an amino group the amino group containing an ester bond
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    • C10M2219/02Sulfur-containing compounds obtained by sulfurisation with sulfur or sulfur-containing compounds
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    • C10M2223/12Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions obtained by phosphorisation of organic compounds, e.g. with PxSy, PxSyHal or PxOy
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    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2225/00Organic macromolecular compounds containing phosphorus as ingredients in lubricant compositions
    • C10M2225/04Organic macromolecular compounds containing phosphorus as ingredients in lubricant compositions obtained by phosphorisation of macromolecualr compounds not containing phosphorus in the monomers
    • C10M2225/041Hydrocarbon polymers
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    • C10M2229/00Organic macromolecular compounds containing atoms of elements not provided for in groups C10M2205/00, C10M2209/00, C10M2213/00, C10M2217/00, C10M2221/00 or C10M2225/00 as ingredients in lubricant compositions
    • C10M2229/04Siloxanes with specific structure
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    • C10N2040/00Specified use or application for which the lubricating composition is intended
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Definitions

  • This invention relates to oil-soluble nitrogen-containing compositions and to the process of preparing the same.
  • the compositions of this invention are useful as dispersing agents in lubricants, especially lubricants intended for use in the crankcase of internal combustion engines, gears, and power transmitting units.
  • compositions which are adapted for use as additives in hydrocarbon oils.
  • compositions which are effective as detergents in lubricating compositions are also an object of this invention to provide compositions which are effective as detergents in lubricating compositions.
  • a detergent composition comprising an oil-soluble, acylated nitrogen composition characterized by the presence Within its structure of (A) a hydrocarbon-substituted polar group selected from the class consisting of acyl, acylimidoyl, and acyloxy radicals wherein the substantially hydrocarbon substituent contains at least about 50 aliphatic carbon atoms and (B) a nitrogen-containing group characterized by a nitrogen atom attached directly to said relatively polar group.
  • a critical aspect of this invention is the size of the hydrocarbon substituent in the acylated nitrogen compounds.
  • acylated nitrogen compositions having at least about 50 aliphatic carbon atoms in the hydrocarbon substituent are contemplated as being within the scope of this invention.
  • the hydrocarbon substituent must then contain at least about 25 aliphatic carbon atoms per each polar group. This lower limit is based not only upon the consideration of the oilsolubility of the acylated nitrogen compositions but also upon the effectiveness of such compounds as additives in hydrocarbon oils for the purposes of this invention.
  • acylated nitrogen compositions having less than the minimum number of such aliphatic carbon atoms may be sufi iciently oil-soluble, they nevertheless are not sufficiently effective to be useful as additives of this invention. Furthermore, it has been discovered that their effectiveness diminishes sharply with a corresponding decrease in the size of the hydrocarbon substituent so that acylated nitrogen compositions having less than about 35 aliphatic car-hon atoms in such substituent either are ineffective or produce detrimental results when added to a hydrocarbon oil.
  • the radical preferably should be substantially saturated, i.e., at least about of the total number of carbonto-carbon covalent linkages are saturated linkages.
  • An excessive proportion of unsaturated linkages renders the molecule susceptible to oxidation, degradation, and polymerization and results in products unsuitable for use in hydrocarbon oils in many applications.
  • the hydrocarbon substituent of the acylated nitro gen compositions of this invention preferably should be substantially free from large oil-solubilizing pendant groups, i.e., groups having more than about 6 aliphatic carbon atoms. While some large oil-solubilizing pendant groups may be present, they preferably should be present in proportions less than about one such group for every 25 aliphatic carbon atoms in the main hydrocarbon chain. A higher proportion of large pendant groups impairs the effectiveness of the acylated nitrogen compositions of this invention as additives in hydrocarbon oils.
  • the hydrocarbon substituent may contain polar substituents provided, however, that the polar substituents are not present in proportions sufficiently large to alter significantly the hydrocarbon character of the radical.
  • the polar substituents are exemplified by chloro, bromo, keto, ethereal, aldehydro, nitro, etc.
  • the upper limit with respect to the proportion of such polar substituents in the radical is approximately based on the weight of the hydrocarbon portion of the radical.
  • the sources of the hydrocarbon substituent include principally the high molecular weight substantially saturated petroleum fractions and substantially saturated olefin polymers, particularly polymers of mono-olefins having from 2 to about 30 carbon atoms.
  • the especially useful polymers are the polymers of l-monoolefins such as ethylene, propene, l-butene, isobutene, I-hexene, l-octene, 2-methyl-1-heptene, 3-cyclohexyl-1- butene, and 2-methyl-5-propyl-l-hexene.
  • Polymers of medial olefins i.e., olefins in which the olefinic linkage is not at the terminal position, likewise are useful. They are illustrated by Z-butene, 3-pentene, and 4-octene.
  • interpolymers of the olefins such as those illustrated above with other interpolymerizable olefinic substances such as aromatic olefins, cyclic olefins, and polyolefins.
  • Such interpolymers include, for example, those prepared "by polymerizing isobutene with styrene; isobutene with butadiene; propene with isoprene; ethylene with piperylene; isobutene with chloroprene; isobutene with p-methyl styrene; l-hexene with 1,3-hexadiene; l-octene with l-hexene; I-heptene with l-pentene, 3-methyl-1-butene with l-octene; 3,3-dimethyl-l-pentene with l-hexene; isobutene with styrene and piperylene; etc.
  • the relative proportions of the mono-olefins to the other monomers in the interpolymers influence the stability and oil-solubility of the final acylated nitrogen compositions derived from such interpolymers.
  • the interpolymers contemplated for use in this invention should be substantially aliphatic and substantially saturated, i.e., they should contain at least about 80%, preferably at least about 95%, on a weight basis of units derived from the aliphatic mono-olefins and no more than about 5% of olefinic linkages based on the total number of carbon-to-carbon covalent linkages. In most instances, the percentage of olefinic linkages should be less than about 2% of the total number of carbon-tocarbon covalent linkages.
  • interpolymers include copolymer of 95% (by weight) of isobutene with 5% of styrene; terpolymer of 98% of isobutene with 1% of piperylene and 1% of chloroprene; terpolymer of 95% of isobutene with 2% of 1-butene and 3% of l-hexene; terpolymer of 60% of isobutene with of l-pentene and 20% of l-octene; copolymer of 80% of l-hexene and 20% of l-heptene; terpolymer of 90% of isobutene with 2% of cyclohexene and 8% of propene; and copolymer of 80% of ethylene and 20% of propene.
  • Another source of the substantially hydrocarbon radical comprises saturated aliphatic hydrocarbons such as highly refined high molecular weight white oils or synthetic alkanes such as are obtained by hydrogenation of high molecular weight olefin polymers illustrated above or high molectular weight olefinic substances.
  • olefin polymers having molecular weights of about 7505000 are preferred. Higher molecular weight olefin polymers having molecular weights from about 10,000 to about 100,000 or higher have been found to impart also viscosity index improving properties to the acylated nitrogen compositions of this invention. In many instances the use of such higher molecular weight olefin polymers is desirable. On the other hand, olefin polymers having molecular weights less than about 700 are not useful.
  • the relatively polar group of the acylated nitrogen compositions is selected from the class consisting of acyl, acylimidoyl, and acyloxy radicals. These radicals have the following structural configurations, respectively:
  • R represents the substantially hydrocarbon substituent described hereinbefore and R represents a hydrogen radical or an organic radical such as a hydrocarbon radical or a polar-substituted hydrocarbon radical.
  • the nitrogen-containing group of the acylated nitrogen compositions of this invention is derived from compounds characterized by a radical having the structural configuration
  • the two remaining valences of the nitrogen atom of the above radical preferably are satisfied by hydrogen, amino, or organic radicals bonded to said nitrogen atom through direct carbon-to-nitrogen linkages.
  • the compounds from which the nitrogen-containing group may be derived include principally ammonia, aliphatic amines, aromatic amines, heterocyclic amines or carbocyclic amines.
  • the amines may be primary or secondary amines and may also be polyamines such as alkylene amines, arylene amines, cyclic polyamines, and the hydroxy-substituted derivatives of such polyamines.
  • amines of these types are methylamine, N- methylethylamine, N-methyl-octylamine, N-cyclohexylanaline, dibutylamine, cyclohexylamine, aniline, di(pmethylphenyl)amine, dodecylamine, octadecylamine, ophenylenediamine, N,N di-n-butyl-p-phenylenediamine, mor-pholine, piperazine, tetrahydropyr-azine, indole, hexahydro-1,3,5-triazine, 1-H-1,2,4-triazole, melamine, bis-(paminophenyl)methane, phenyl-methylenimine, menthanediamine, cyclohexamine, pyrrolidine, 3-amino-5,6-diphenyl-1,2,4 triazine, quinonediimine, 1,3 indandii
  • a preferred source of the nitrogen-containing group consists of polyamines, especially alkylene amines conforming for the most part to the formula HN alky1eue-N H l K i).
  • A is a substantially hydrocarbon or hydrogen radical
  • the alkylene radical is preferably a lower alkylene radical having less than about 8 carbon atoms.
  • the alkylene amines include principally methylene amines, ethylene amines, butylene amines, propylene amines, pentylene amines, hexylene amines, heptylene amines, octylene amines, other polymethylene amines, and also the cyclic and the higher homologs of such amines such as piperazines and amino-alkyl-substituted piperazines. They are exemplified specifically by: ethylene diamine, triethylene.
  • the ethylene amines are especially useful. They are described in some detail under the heading Ethylene Amines in Encycylopedia of Chemical Technology Kirk and Othmer, volume 5, pages 898905, Interscience Publishers, New York (1950). Such compounds are prepared most conveniently by the reaction of an alkylene chloride with ammonia. The reaction results in the production of somewhat complex mixtures of alkylene amines, including cyclic condensation products such as piperazines. These mixtures find use in the process of this invention. On the other hand, quite satisfactory products may be obtained also by the use of pure alkylene amines.
  • alkylene amine for reasons of economy as well as effectiveness of the products derived therefrom is a mixture of ethylene amines prepared by the reaction of ethylene chloride and ammonia and having a composition which corresponds to that of tetraethylene pentamine.
  • Hydroxyalkyl-substituted alkylene amines i.e., alkylene amines having one or more hydroxyalkyl substituents on the nitrogen atoms, likewise are contemplated for use herein.
  • the hydroxyalkyl-substituted alkylene amines are preferably those in which the alkyl group is a lower alkyl group, i.e., having less than about 6 carbon atoms.
  • amines examples include N-(2-hydroxyethyl) ethylene diamine, N,N' bis(2 hydroxyethyl)ethylene diamine, 1-(Z-hydroxyethyl)piperazine, mono-hydroxypropyl-substituted diethylene triamine, 1,4-bis(2-hydroxypropyl) piperazine, di-hydroxypropyl-substituted tetraethylene pentamine, N-(3-hydroxypropyl)tetramethylene diamine, and 2-heptadecyl-1-(2-hy droxyethyl) imidazoline.
  • nitrogen-containing group examples include ureas, thioureas, hydrazines, guanidines, amidines, amides, thioamides, cyanamides, etc.
  • Specific examples illustrating such compounds are: hydrazine, phenylhydrazine, N, N'-diphenylhydrazine, octadecylhydrazine, benzoylhydrazine, urea, thiourea, N-butylurea, stearylamide, oleylamide, guanidine, 1,3-diphenylguanidine, 1,2,3-tributylguanidine, benzamidine, octadecamidine, N,N-dimethylstearamidine, cyanamide, dicyandiamide, guanylurea, aminoguanidine, etc.
  • the nitrogen-containing group in the acylated nitrogen compositions of this invention is characterized by a nitrogen atom attached directly to the relatively polar group.
  • the linkage between a nitrogen atom and an acyl radical is representative of an amide or an imide structure
  • the linkage between a nitrogen atom and an acylimidoyl radical is representative of an amidine structure
  • the linkage between a nitrogen atom and an acyloxy radical is representative of an ammonium-carboxylic acid salt structure.
  • the acylated nitrogen compositions of this invention are characterized. by amide, imide, amidine, or salt linkages and in many instances a mixture of such linkages.
  • Those containing two such linkages separated by a lower alkylene radical i.e., one having less than about 6 carbon atoms
  • succinic, glutaric, or adipic radicals are especially preferred in this invention.
  • a convenient method for preparing the acylated nitrogen compositions of this invention comprises reacting a high molecular weight acid-producing compoundv characterized by the presence within its structure of a high molecular weight oil-solubilizing group having at least about 50 aliphatic carbon atoms and at least one acid-producing group having the structural configuration o ax wherein X is selected from the class consisting of halogen, hydroxy, hydrocarbon-oxy, acyloxy, and amino radicals derived from ammonia or a lower primary amine such as a mono-alkylamine or mono-arylamine having no more than about 6 aliphatic carbon atoms with at least about one-half an equivalent amount of a nitrogen-containing compound characterized by the presence within its structure of at least one radical having the structural configuration
  • the above process involves a reaction between the acidproducing group with the nitrogen-containing radical to result in the direct attachment of the nitrogen atoms to a polar radical, i.e., acyl, acylimidoyl, or
  • the linkage formed between the nitrogen atom and the polar radical may thus be that representative of a salt, amide, imide, or amidine radical.
  • the product of the above process contains a mixture of linkages representative of such radicals.
  • the precise relative proportions of such radicals in the product usually are not known as they depend to a large measure upon the type of the acidproducing group and the nitrogen-containing radical involved in the reaction and also upon the environment (e.g., temperature) in which the reaction is carried out.
  • the reaction involving an acid or an'hydride group with an amino nitrogen-containing radical at relatively low temperatures such as below about 60 C. results predominantly in a salt linkage (i.e.,
  • the acid-producing compounds contemplated for use in the above process include mono-carboxylic and polycarboxylic acids, acid halides, esters, and anhydrides as well as imides and amides derived from ammonia or a lower primary amine, and also mixtures of such compounds.
  • the imide or amide of ammonia or a lower primary amine is especially useful for preparing the acylated nitrogen compositions having more than one nitrogencontaining radicals.
  • the nature of the oil-solubilizing group in such compounds should be the same as that which characterized the hydrocarbon substituent, described previously, in the acylated nitrogen compositions of this invention.
  • the substantially saturated, aliphatic hydrocarbon-substituted succinic acids and anhydrides are especially preferred for use as the acid-producing reactant in this process for reasons of the particular effectiveness of the products obtained from such compounds as additives in hydrocarbon oils.
  • the succinic compounds are readily available from the reaction of maleic anhydride with a high molecular Weight olefin or a chlorinated hydrocarbon such as the olefin polymer described hereinabove. The reaction involves merely heating the two reactants at a temperature about 100-200 C.
  • the product from such a reaction is an alkenyl succinic anhydride.
  • the alkenyl group may be hydrogenated to an alkyl group.
  • the anhydride may be hydrolyzed by treatment with Water or steam to the corresponding acid.
  • Either the anhydride or the acid may be converted to the corresponding acid halide or ester by reaction with, e.g., phosphorus halide, phenols or alcohols or to the corresponding imide or amide by reaction with ammonia or a lower primary amine.
  • high molecular Weight olefins or chlorinated hydrocarbons containing an activating polar substituent, i.e., a substituent which is capable of activating the hydrocarbon molecule in respect to reaction with maleic acid or anhydride may be used in the above-illustrated reaction for preparing the succinic compounds.
  • polar substituents may be illustrated by sulfide, disulfide, nitro, mercaptan, bromine, ketone, and aldehyde radicals.
  • polar-substituted hydrocarbons examples include polypr-opene sulfide, di-polyisobutene disulfide, nitrated mineral oil, di-polyethylene sulfide, brominated polyethylene, etc.
  • Another method useful for preparing the succinic acids and anhydrides involves the reaction of itaconic acid with a high molecular weight olefin or a polar-substituted hydrocarbon at a, temperature usually within the range from about 100 C. to about 200 C.
  • the polycarboxylic acids and derivatives thereof having more than two carboxylic radicals per molecule which are contemplated for use in this invention are those containing at least about 50 aliphatic carbon atoms per molecule and furthermore, at least about 25 aliphatic carbon atoms per each carboxylic radical.
  • Such acids may be prepared by halogenating a high molecular weight hydrocarbon such as the olefin polymer described hereinabove to produce a poly-halogenated product, converting the polyhalogenated product to a poly-nitrile, and then hydrolyzing the poly-nitrile. They maybe prepared also by oxidation of a high molecular weight polyhydric alcohol with potassium permanganate, nitric acid, or a like oxidizing agent.
  • Another method for preparing such polycarboxylic acids involves the reaction of an olefin or a polarsubstituted hydrocarbon such as a chloro-polyisobutene with an unsaturated poly-carboxylic acid such as 2- pentene-1,3,5-tricarboxylic acid obtained by dehydration of citric acid.
  • an olefin or a polarsubstituted hydrocarbon such as a chloro-polyisobutene
  • an unsaturated poly-carboxylic acid such as 2- pentene-1,3,5-tricarboxylic acid obtained by dehydration of citric acid.
  • the mono-carboxylic acids and derivatives thereof may be obtained by oxidizing a mono-hydric alcohol with potassium permanganate or by reacting a halogenated high molecular olefin polymer with a ketene.
  • Another convenient method for preparing the monocarboxylic acids involves the reaction of metallic sodium with an acetoacetic ester or a malonic ester of an alkanol to form a sodium derivative of the ester and the subsequent reaction of the sodium derivative with a halogenated high molecular weight hydrocarbon such as brominated wax or brominated polyisobutene.
  • Other methods include the reaction of a high molecular weight olefin with ozone; the Haloform Reaction; the reaction of an organometallic complex (such as lithium-olefin complex) with carbon dioxide; the reaction of a chlorinated hydrocarbon with a lactone; the reaction of a chlorinated hydrocanbon with chloromaleic acid or mercapto-maleic anhydride.
  • organometallic complex such as lithium-olefin complex
  • the mono-carboxylic and poly-carboxylic acid anhydrides are obtained by dehydrating the corresponding acids. Dehydration is readily accomplished by heating the acid to a temperature above about 70 C. preferably in the presence of a dehydration agent, e.g., acetic anhy- 8 dride.
  • Cyclic anhydrides are usually obtained from poly-cariboxylic acids having the acid radicals separated by no more than three carbon atoms such as substituted succinic or glutaric acids, whereas linear polymeric anhydrides are obtained from poly-carboxylic acids having the acid radicals separated by four or more carbon atoms.
  • the acid halides of the mono-carboxylic and polycarboxylic acids can be prepared by the reaction of the acids or their anhydrides with a halogenation agent such as phosphorus tribromide, phosphorus pentachloride, or thionyl chloride.
  • the esters of such acids can be prepared simply by the reaction of the acids or their anhydrides With an alcohol or a phenolic compound such as methanol, ethanol, octadecanol, cyclohexanol, phenol, naphthol, octylphenol, etc.
  • the esterification is usually promoted by the use of an alkaline catalyst such as sodium hydroxide or sodium alkoxide or an acidic catalyst such as sulfuric acid.
  • the nature of the alcoholic or phenolic portion of the ester radical appears to have little infiuence on the utility of such ester as reactant in the process described herein-above.
  • the nitrogen-containing reactants useful in the above process are the compounds, described previously in this specification, from which the nitrogen-containing group the acylated nitrogen compositions of this invention can be derived.
  • the above process is usually carried out by heating a mixture of the acid-producing compound and the nitrogen-containing reactant at a temperature above about C., preferably within the range from about C. to about 250 C.
  • a temperature above about C. preferably within the range from about C. to about 250 C.
  • the process may be carried out at a lower temperature such as room temperature to obtain products having predominantly salt linkages or mixed saltamide linkages.
  • Such products may be converted, if desired, by heating to above 80 C. to products having predominantly amide, imide, or amidine linkages.
  • a solvent such as benzene, toluene, naphtha, mineral oil, xylene, n-hexane, or the like is often desirable in the above process to facilitate the control of the reaction temperature.
  • Another method for preparing the acylated nitrogen compositions of this invention involves first reacting the nitrogen-containing reactant with an olefinic acid-producing compound to form a nitrogen containing intermediate and then incorporating a large hydrocarbon substituent (i.e., having at least about 50 aliphatic carbon atoms) into the intermediate by reacting the intermediate with a high molecular weight hydrocarbon reactant, such as an olefin, a chlorinated hydrocarbon, or a polar substituted hydrocarbon illustrated previously.
  • a high molecular weight hydrocarbon reactant such as an olefin, a chlorinated hydrocarbon, or a polar substituted hydrocarbon illustrated previously.
  • the olefinic acid-producing compound useful in the process may be an acid, anhydride, acid halide, or ester and it likewise may be an imide or amide derived from ammonia or a lower primary amine such as is described previously.
  • the acid-producing compound may be that of maleic acid, itaconic acid, acrylic acid, aconitic acid, methacrylic acid, chloromaleic acid, alpha-chloroacrylic acid, alpha-butylacrylic acid, crotonic acid, citraconic acid, mesaconic acid, or a like acid preferably having less than about 8 carbon atoms and an olefinic linkage adjacent to the acid-producing radical.
  • olefinic acid-producing compound examples include maleic acid, maleic anhydride, chloromaleic anhydride, maleamic acid, acrylic acid, acrylyl chloride, acrylyl bromide, methacrylic acid, alphapropylacrylyl chloride, crotonic acid, methyl acrylate, ethyl methacrylate, dimethyl maleate, diethyl itaconate, dibutyl maleate, maleimide, maleamide, N-methyl maleamide, dimethyl maleamide, N-butyl maleamide acid, N- propyl maleimide, methyl chlo-roacrylate, dimethyl citraconate, etc.
  • the ester groups, imide groups, and amide groups of such olefinic acid-producing compounds include those discussed previously in connection with the high molecular weight acid-producing compounds useful in preparing the acylated nitrogen compositions of the invention.
  • the reaction of the nitrogen-containing reactant with an olefinic acid-producing compound may be carried out at a temperature from about 25 C. to 300 C. or any temperature below the decomposition point of the reaction mixture.
  • the reaction is sirnilar to that which characterizes the formation of acylated nitrogen compositions described previously and results in a nitrogen-containing inter-mediate.
  • the intermediate produced by such reaction is thus characterized by the presence therein of an amide, imide or amidine linkage or a mixture of such linkages.
  • a convenient method of incorporating a high molecular weight hydrocarbon substituent into the nitrogen-containing intermediate involves reacting the intermediate with a high molecular weight reactant olefin, chlorinated hydrocarbon such as a chlorinated olefin polymer, or a polar substituted high molecular Weight hydrocarbon at a temperature above about 100 C., preferably below about 200 C.
  • a high molecular Weight reactant is as described previously in connection with the preparation of the high molecular weight succinic acidproducin-g compounds of this invention.
  • the relative proportions of the acid-producing compounds and the nitrogen-containing reactants to be used in the above process are such that at least about one-half of a stoichiometrically equivalent amount of the nitrogencontaining reactant is used for each equivalent of the acidproducing compound used.
  • the equivalent weight of the nitrogen-containing reactant is based upon the number of the nitrogen-containing radicals defined by the structural configuration
  • the equivalent weight of the acid-producing compound is based upon the number of the acid-producing radicals defined by the structural configuration
  • the upper limit of the useful amount of the nitrogen-containing reactant appears to be about two moles for each equivalent of the acid-producing compound used. Such amount is required, for instance, in the formation of products having predominantly amidine linkages. Beyond this limit, the excess amount of the nitrogen-containing reactant appears not to take part in the reaction and thus simply remains in the product apparently Without any adverse effects.
  • the lower limit of about one-half equivalent of the nitrogen-containing reactant used for each equivalent of the acid-producing compound is based upon the stoichiome'try for the formation of products having predominantly imide linkages. In most instances, the preferred amount of the nitrogencontaining reactant is approximately one equivalent for each equivalent of the acid-producing compound used.
  • a high molecular weight substituted succinic acid-producing compound such as acid or anhyd-ride
  • an alkylene polyamine such as ethylene diamine or polyethylene polyamine
  • x is at least 1
  • R is a hydrocarbon group having at least about 50 aliphatic carbon atoms and at least about 25 aliphatic carbon atoms for each unit of x
  • NR' is selected from the class consist-ing of (A) radicals derived 10 from an alyklene polyamine by the removal of a hydrogen atom from an amino group and (B) radicals derived from an alkylene polyamine by the removal of a hydrogen atom from an amino group and characterized by the presence, on the nitrogen atom of at least one additional amino group, of a complex substituent having the formula
  • the value of x is at least one for each mole of the
  • the radical R is the residue derived from an alkylene polyamine by the removal of one amino group; it may further contain a complex substituent (illustrated above) on the nitrogen atom of at least one additional amino group, or on the nitrogen atom of each of the other amino groups of the alkylene polyamine residue.
  • the amide is illustrated by one present in the acylated nitrogen composition obtained by the reaction of one mole of an alkylene polyamine with as many equivalents of the substituted succinic acid or anhydride as there are amino groups in the polyamine.
  • Example 1 A polyisobutenyl succinic anhydride is prepared by the reaction of a chlorinated polyisobutylene with maleic anhydride at 200 C.
  • the polyisobutenyl radical has an average molecular weight of 850 and the resulting alkenyl succinic anhydride is found to have an acid number of 113 (corresponding to an equivalent weight of 500).
  • the mixture then is heated and a water-toluene azeotrope distilled from the mixture. When no more water would distill the mixture is heated to C. at reduced pressure to remove the toluene. The residue is diluted with 350 grams of mineral oil and this solution is found to have a nitrogen content of 1.6%.
  • the product is an oil solution of an acylated nitrogen composition containing an amide conforming to the structural formula where R is a polyisobutene radical, x has a value of one for each mole of the polyisobutene group, and NR is a radical derived from diethylene triamine by the removal of a hydrogen atom from an amino group and characterized by the presence on the nitrogen atom of at least one remaining amino group of a radical selected from the class consisting of Example 2
  • the procedure of Example 1 is repeated using 31 grams (1 equivalent) of ethylene diamine as the amine reactant.
  • the nitrogen content of the resulting product is 1.4%.
  • Example 3 The procedure of Example 1 is repeated using 55.5 grams (1.5 equivalents) of an ethylene amine mixture having a composition corresponding to that of triethylene tetramine. The resulting product has a nitrogen content of 1.9%.
  • the product is an oil solution of an acylated nitrogen composition containing an amide conforming to the structural formula shown in Example 1 except that R is derived from the ethylene amine mixture.
  • Example 4 The procedure of Example 1 is repeated using 55.0 grams (1.5 equivalents) of triethylene tetramine as the amine reactant. The resulting product has a nitrogen content of 2.9%.
  • the product is an oil solution of an acylated nitrogen composition containing an amide conforming to the structural formula shown in Example 1 except that R is derived from triethylene tetramine.
  • Example 5 To a mixture of 140 grams of toluene and 400 grams (0.78 equivalent) of a polyisobutenyl succinic anhydride (having an acid number of 109 and prepared from maleic anhydride and the chlorinated polyisobutylene of Example 1) there is added at room temperature 63.6 grams (1.55 equivalents) of an ethylene amine mixture having an average composition corresponding to that of tetraethylene pentamine and available from Carbide and Carbon under the trade name Polyamine H. The mixture is heated to distill the water-toluene azeotrope and then to 150 C. at reduced pressure to remove the remaining toluene. The residual polyamide has a nitrogen content of 4.7%.
  • the product is an oil solution of an acylated nitrogen composition containing an amide conforming to the structural formula shown in Example 1 except that R is derived from the ethylene amine mixture.
  • Example 6 The procedure of Example 1 is repeated using 46 grams 1.5 equivalents) of ethylene diamine as the amine reactant.
  • the product which resulted has a nitrogen content of 1.5%.
  • the product is an oil solution of an acylated nitrogen composition containing an amide conforming to the structural formula shown in Example 1 except that R is derived from ethylene diamine.
  • Example 7 A polyisobutenyl succinic anhydride having an acid number of 105 and an equivalent weight of 540 is prepared by the reaction of a chlorinated polyisobutylene (having an average molecular weight of 1,050 and a chlorine content of 4.3%) and maleic anhydride. To a mixture of 300 parts by weight of the polyisobutenyl succinic anhydride and 160 parts by weight of mineral oil there is added at 65 95 C. an equivalent amount (25 parts by weight) of Polyamine H (identified in Example 5). This mixture then is heated to 150 C. to distill all of the water formed in the reaction. Nitrogen is bubbled through the mixture at this temperature to insure removal of the last traces of water.
  • the residue is diluted by 79 parts by weight of mineral oil and this oil solution found to have a nitrogen content of 1.6%.
  • the product is an oil solution of an acylated nitrogen composition containing an amide conforming to the structural formula shown in Example 1 except that R is derived from the ethylene amine mixture.
  • Example 8 A mixture of 2,112 grams (3.9 equivalents) of the polyisobutenyl succinic anhydride of Example 7, 136
  • the product is an oil solution of an acylated nitrogen composition containing an amide conforming to the structural formula showin in Example 1.
  • Example 9 To a solution of 1,000 grams (1.87 equivalents) of the polyisobuentyl succinic anhydride of Example 7, in 500 grams of mineral oil there is added at 85-95 C. 70 grams (1.87 equivalents) of tetraethylene pentamine. The mixture then is heated at -165 C. for four hours, blowing with nitrogen to aid in the removal of Water. The residue is diluted with 200 grams of mineral oil and the oil solution found to have a nitrogen content of 1.4%. The product is an oil solution of an acylated nitrogen composition containing an amide conforming to the structural formula shown in Example 1 except that R is derived from tetraethylene pentamine.
  • Example 10 A polypropenyl succinic anhydride is prepared by the reaction of a chlorinated polypropylene (having a molecular weight of about 900 and a chlorine content of 4%) and maleic anhydride at 200 C.. The product has an acid number of 75. To a mixture of 390 grams (0.52 equivalent) of this polypropenyl succinic anhydride, 500 grams of toluene, and grams of mineral oil there is added portionwise 22 grams (0.52 equivalent) of Polyamine H. The reaction mixture is heated at reflux temperature for three hours and water removed from an azeotrope with toluene. The toluene then is removed by heating to 150 C./2O millimeters. The residue was found to contain 1.3% of nitrogen. The product is an oil solution of an acylated nitrogen composition containing an amide conforming to the structural formula shown in Example 1 except that R is derived from the ethylene amine mixture.
  • Example 11 A substituted succinic anhydride is prepared by reacting maleic anhydride with a chlorinated copolymer of isobutylene and styrene.
  • the copolymer consists of 94 parts by weight of isobutylene units and 6 parts by weight of styrene units, has an average molecular weight of 1,200, and is chlorinated to a chlorine content of 2.8% by weight.
  • the resulting substituted succinic anhydride has an acid number of 40. To 710 grams (0.51 equivalent) of this substituted succinic anhydride and 500 grams of toluene there is added portion wise 22 grams (0.51 equivalent) of Polyamine H.
  • the mixture is heated at reflux temperature for three hours to remove by azeot-ropic distillation all of the water formed in the reaction, and then at 150 C./20 millimeters to remove the toluene.
  • the residue contains 1.1% by weight of nitrogen.
  • the product is an oil solution of an acylated nitrogen composition containing an amide conforming to the structural formula shown in Example 1.
  • Example 12 A substituted succinic anhydride is prepared by reacting maleic anhydride with a chlorinated copolymer of isobutylene and isoprene.
  • the copolymer consists of 99 parts by weight of isobutylene units and 1% by weight of isoprene units.
  • the molecular weight of the copolymer is 28,000 and the chlorine content of the chlorinated copolymer is 1.95%.
  • the resulting alkenyl succinic anhydride had an acid number of 54.
  • Example 13 To a mixture of 228 grams (0.22 equivalent) of an oil solution of this alkenyl succinic anhydride, 58 grams of additional mineral oil, 500 grams of toluene and 9.3 grams (0.22 equivalent) of Example 13 A polyisobutenyl succinic anhydride is prepared by the reaction of a chlorinated polyisobutylene with maleic anhydride.
  • the chlorinated polyisobutylene has a chlorine content of 2% and an average molecular weight of 11,000.
  • the polyisobutenyl succinic anhydride has an acid number of 48.
  • Example 14 The procedure of Example is repeated except that 0.94 equivalent of Polyamine H is used instead of 1.55 equivalents.
  • the nitrogen content of the product is 3%.
  • the product is an oil solution of an acylated nitrogen composition containing an amide conforming to the structural formula shown in Example 1.
  • Example 15 A polyisobutenylsubstituted succinic acid is prepared by hydrolysis of the corresponding anhydride (prepared in turn by the condensation of a chlorinated polyisobutylene and maleic anhydride). To 1152 grams (1.5 equivalents) of a 70% mineral oil solution of this polyisobutylenyl succinic acid having an acid number of 62 there is added at room temperature 59.5 grams (1.5 equivalents) of Polyamine H. This mixture is heated at 150- 167 C. for 7 hours during which time a total of 19.5 grams of Water is distilled from the mixture. The residue is diluted with 174 grams of mineral oil and then filtered at 150 C. The filtrate has a nitrogen content of 1.6%. The product is an oil solution of an acylated nitrogen composition containing an amide conforming to the structural formula shown in Example 1.
  • the product is an oil solution of an acylated nitrogen composition containing an amide conforming to the structural formula shown in Example 1 except that R is derived from di-( 1,2-propylene triamine.
  • Example 17 A polyisobutylene having an average molecular weight of 50,000 is chlorinated to a chlorine content of by Weight. This chlorinated polyisobutylene is reacted with maleic anhydride to produce the corresponding polyisobutenyl succinic anhydride having an acid number of 24. To 6,000 grams (2.55 equivalents) of this anhydride there is added portionwise at 70-105 C. 108
  • the product is an oil solution of an acylated nitrogen composition containing an amide conforming to the structural formula shown in Example 1 except that R is derived from the ethylene amine mixture.
  • Example 18 A mixture of 1 equivalent of a polyisobutene-substituted succinic anhydride having an acid number of 98 (prepared according to the procedure described in Example 1) and 1 equivalent of an acrolein-ammonia (molar ratio of 1: 1) interpolymer having a nitrogen content of 23% by Weight is diluted with 40% by its Weight of a mineral oil. The resulting mixture is heated to 155 C. and nitrogen is bubbled through the mixture at this temperature for 5 hours. The residue is found to have a nitrogen content of 1.35%.
  • Example 19 A cyanoethyl-substituted ethylene amine is prepared by mixing 21-2 grams of acrylonitrile with 216 grams of an ethylene amine mixture consisting of 75% by weight of triethylene tetramine and 25% by weight of diethylene triamine at room temperature and heating the mixture at l'l-0130 C. for 5 hours and then to C./mm. To a mixture of 111110 grams of the polyisobutene-substituted succinic anhydride of Example 1 and 825 grams of mineral oil there is added at 60 C. 143 grams dropwise of the above cyanoethyl-substituted ethylene amine (having a nitrogen content of 31.8%), The mixture is heated at C. C. for 5 hours while being purged with nitrogen. A total of 6 cc. of water is removed by distillation. The residue has a nitrogen content of 1.6 6%.
  • Example 20 To a mixture of 430 grams of the polyisobutenesubstituted succinic anhydride of Example 1 and 355 grams of mineral oil there is added at 60-80 C. 108 grams of N-aminopropyl morpholine throughout a period of 1 hour. The mixture is heated at 150-155 C. for 5 'hours until no more Water distills. The residue is found to have a nitrogen content of 2.3%.
  • Example 21 To a mixture of 1000 grams of the polyisobutenesubstituted succinic anhydride of Example 1 and 500 grams of mineral oil there is introduced at 150 1 60 C. beneath its surface a sufficient quantity of ammonia for formation of an imide within a period of 1 hour. The mixture is diluted with 169 grams of mineral oil, heated to 150 C. and filtered. The filtrate is found to have a nitrogen content of 0.77%.
  • Example 23 A mixture of 286 grams of polyisobutene-substituted succinic anhydride of Example 1, 96 grams of N, N-di- 'butyl ethylene-diamine and 252 grams of mineral oil is prepared at 60 C. and heated at 150-165 C. for 5 hours while being purged with nitrogen. The residue is found to have a nitrogen content of 2.24%.
  • Example 24 A mixture of 417 grams of polyisobutene-substituted succinic anhydride of Example 1, 30 grams of N-(2- aminoethyl) trimethylene diamine and 293 grams of mineral oil is prepared at 6080 C. and then heated at 150155 C. -for hours while being purged with nitrogen. The residue is found to have a nitrogen content of 1.51%.
  • Example 25 A mixture of 430 grams of the polyisobutene-substituted succinic anhydride of Example 1, 64 grams of 1,l-(dimethylaminoethyl)-4-methyl-piperazine and 324 grams of mineral oil is prepared at 60 C. and then heated at 150-155 C. while being blown with nitrogen. The residue is found to have a nitrogen content of 1.81%.
  • Example 26 A mixture of 416 grams of polyisobutene-substituted succinic anhydride of Example 1, 124 grams of N-phenyl piperazine and 356 grams of mineral oil is prepared at 60 C. and then heated at l50-155 C. for 5 hours while being purged with nitrogen. No water is removed by such heating. The residue is found to have a nitrogen content of 2.07%.
  • Example 27 A mixture of 1110 grams of polyisobutene-substituted succinic anhydride of Example 1, 105 grams of anthranilic acid and 844 grams of mineral oil is heated at 100 C. for 2 hours. The mixture is cooled and is mixed with 72 grams of a mixture consisting of 75% by weight of triethylene tetramine and 25% by weight of diethylenetriamine at 6080 C. The resulting mixture is heated at 150-155 C. for 5 hours while being purged with nitrogen. The residue is found to have a nitrogen content of 1.72%.
  • Example 28 A diisobutenyl-substituted ethylene amine is prepared by reacting 590 grams of diisobutenyl chloride and 264 grams of a mixture consisting of 75 by weight of triethylene tetramine and 20% by weight of diethylene triamine in the presence of 264 grams of potassium hydroxide (85% purity) and 2200 grams of isopropyl alcohol at 85-90 C.
  • a mixture of 528 grams of polyisobutene-substituted succinic anhydride of Example 1 101 grams of the above diisobutenyl-substituted ethylene amine and 411 grams of mineral oil is heated at 150- 160 C. while being purged with nitrogen until no more water distills. The residue has a nitrogen content of 1.98%.
  • Example 29 A mixture of 45 grams of di-(polypropoxy)cocoamine having a molecular weight of 2265, 22 grams of polyisobutene-substituted succinic anhydride of Example 1 and 44 grams of mineral oil is heated at 150155 C. for 7 hours. The residue is found to have a nitrogen content of 0.25%.
  • Example 30 A mixture of 1000 grams of the polyisobutene-substituted succinic anhydride of Example 1, 159 grams of menthane diamine and 500 grams of mineral oil is prepared at 70100 C.- and heated at 150-190 C. while being blown with nitrogen until no water distills. The residue is diluted with 258 grams of mineral oil and the solution is found to have a nitrogen content of 1.32%.
  • Example 31 A polypropylene-substituted succinic anhydride having an acid number of 84 is prepared by the reaction of a chlorinated polypropylene having a chlorine content of 3% and molecular weight of 1200 with maleic anhydride. A mixture of 813 grams of the polypropylene-substi- 16 tuted succinic anhydride, 50 grams of a commercial ethylene amine mixture having an average composition corresponding to that of tetraethylene pentamine and 566 grams of mineral oil is heated at 150 C. for 5 hours. The residue is found to have a nitrogen content of 1.18%.
  • Example 32 A mixture of 206 grams of N,N'-disecondary-butyl p-phenylene diamine, 1000 grams of the polyisobutenesubstituted succinic anhydride of Example 1 and 500 grams of mineral oil is prepared at C. and heated at 150200 C. for 9.5 hours. The mixture is diluted with 290 grams of mineral oil, heated to 160 C. and filtered. The filtrate is found to have a nitrogen content of 1.29%.
  • Example 33 To 1000 grams of the polyisobutene-substituted succinic anhydride of Example 1 and 500 grams of mineral oil there is added 17.6 grams of hydrazine at 70-80 C. The reaction is exothermic. The mixture is heated at 140150 C. for 1 hour whereupon 9 grams of water is collected as the distillate. To the residue there is then added 40 grams of an ethylene amine mixture having an average composition corresponding to that of tetraethylene pentamine at 70-80 C. The mixture i then heated at 150160 C. while being purged with nitrogen until no more water is removed by distillation. The residue is diluted with 200 grams of mineral oil, heated to 160 C. and filtered. The filtrate has a nitrogen content of 1.16%.
  • Example 34 T o a solution of 1000 grams of the polyisobutene-substituted snccinic anhydride of Example 1 in 500 grams of mineral oil there is added 28 grams of 1,1-dimethyl hydrazine at 5060 C. The mixture is heated at 60- C. for 3 hours and then mixed with 40 grams of an ethylene amine mixture having an average composition corresponding to that of tetraethylene pentamine at 85- 95C. The mixture is then heated at 150-185 C. for 6 hours whereupon 14 grams of water is collected as the distillate. The residue is diluted with 197 grams of mineral oil, heated to 160 C. and filtered. The filtrate has a nitrogen content of 1.53%.
  • Example 35 A mixture of 1000 grams of the polyisobutene-substituted succinic anhydride of Example 1, 333 grams of 1,2-di(3-aminopropoxy) ethane and 500 grams of mineral oil is heated at 170 C. for 5 hours whereupon 18 grams of Water is collected as the distillate. The residue is diluted with 380 grams of mineral oil, heated to 160 C. and filtered. The filtrate has a nitrogen content of 2.3%.
  • Example 36 A mixture of 1000 grams of the polyisobutene-substituted succinic anhydride of Example 1, 418 grams of di- (3-aminopropoxy ethyl) ether and 500 grams of mineral oil is heated at 170 C. for 4 hours. A total of 17 grams of water is collected as the distillate. The residue is diluted with 433 grams of mineral oil heated to 160 C. and filtered. The filtrate has the nitrogen content of 2.18%.
  • Example 37 A mixture of 1000 grams of the polyisobutene-substituted succinic anhydride of Example 1 and 361 grams of a technical tertiary-alkyl primary amine wherein the tertiary-alkyl radical contains 12-14 carbon atoms and 500 grams of mineral oil is heated at 250 C. for 13 hours while being purged with nitrogen. The residue is then heated to 150 C./1 mm., diluted with 337 grams of mineral oil, heated to C. and filtered. The filtrate has a nitrogen content of 0.87%.
  • Example 38 A mixture of 1000 grams of the polyisobutene-substituted succinic anhydride of Example 1, 254 grams of aminoguanidine bicarbonate and 500 grams of mineral oil is prepared at 80 C. and heated at 130-165 C. for hours. The residue is mixed with 223 grams of mineral oil, heated to 150 C., and filtered. The filtrate has the nitrogen content of 3.38%.
  • Example 39 A mixture of 1000 grams of the polyisobutene-substituted succinic anhydride of Example 1, 178 grams of Z-amino-pyridine and 500 grams of mineral oil is heated at 140175 C. for 10 hours while being purged with nitrogen. A total of 16 grams of water is collected as the distillate. The residue is diluted with 273 grams of mineral oil and filtered. The filtrate ha a nitrogen content of 2.55%.
  • Example 40 A mixture of 1000 grams of the polyisobutene-substituted succinic anhydride of Example 1, 103 grams of 2,6-diamino-pyridine and 500 grams of mineral oil is heated at 140-180 C. for 11 hours while being purged with nitrogen. A total of 16 grams of Water is collected as the distillate. The residue is diluted with 223 grams of mineral oil, heated to 150 C. and filtered. The filtrate has a nitrogen content of 2.15%.
  • Example 41 A mixture of 1000 grams of polyisobutene-substituted succinic anhydride of Example 1, 159 grams of cyanoguanidine and 233 grams of toluene is heated at the reflux temperature of 14 hours while 7.15 grams of water is removed by azeotropic distillation. The mixture is diluted With 740 grams of mineral oil and toluene is then removed by heating the mixture to 150 C. The residue is filtered and the filtrate has the nitrogen content of 4.74%.
  • Example 42 A mixture of 1632 grams of polyisobutene-substituted succinic anhydride of Example 1, 207 grams of a condensation product of acrolein with ammonia (molar ratio of 1:1) having a nitrogen content of 20%, 604 grams of mineral oil and 1750 grams of toluene is heated at the reflux temperature for 3 hours. A total of 31 grams of water is removed as the distillate. Toluene is then removed by heating the mixture to 150 C./ 20 mm. The residue is found to have a nitrogen content of 1.89%.
  • Example 43 I A nitrogen-containing compound is prepared by mixing 100 grams of cyanoguanidine with 500 grams of ethylene amine mixture having an average composition corresponding to that of tetraethylene pentamine and heating the mixture at 70-80 C. for 3 hours to obtain a homogeneous mass and filtering the mass.
  • a mixture of 1000 grams of the polyisobutene-substituted succinic anhydride of Example 1, 96 grams of the above filtrate and 164 grams of toluene is heated at the reflux temperature for 10 hours. The toluene is then removed by heating the mixture to 150 C./2O mm. The residue is diluted with 400 grams of mineral oil and filtered. The filtrate has a nitrogen content of 3.43%.
  • Example 44 To a mixture of 544 .grams of the polyisobutene-substituted succinic anhydride of Example 1, 283 grams of mineral oil and 281 grams of toluene there is added 30 grams of urea at 45 C. The resulting mixture is heated at 130-135 C. for 11 hours whereupon 2.5 cc. of Water is removed as the distillate. The residue is then heated to 140 C./20 mm. and filtered. The filtrate has a nitrogen content of 1%.
  • Example 45 A mixture of 1088 grams of the polyisobutene-substituted succinic anhydride of Example 1, 106 grams of dipropylene triamine, 500 grams of toluene is heated at the reflux temperature for 4 hours until no more Water distills. The residue is then heated to C./20 mm. and diluted with 392 grams of mineral oil. The oil solution is found to have a nitrogen content of 1.74%.
  • Example 46 A mixture of 1000 grams of the polyisobutene-substituted succinic anhydride of Example 1, 174 grams of phenylbiguanide and 270 grams of toluene is heated at the reflux temperature for 6.5 hours whereupon 25 grams of water is removed by distillation. The residue is diluted With 500 grams of mineral oil and heated to C./2O mm. to distill ofi toluene. The residue is diluted further with 265 grams of mineral oil, heated to 150 C. and filtered. The filtrate has a nitrogen content of 3.4%.
  • Example 47 A mixture of 920 grams of the polyisobutene-substituted succinic anhydride of Example 1, and 249 grams of bis-(dimethylaminopropyl) amine is heated at reflux temperature until no more water distills. The residue has a nitrogen content of 4%.
  • Example 48 A mixture of 1000 grams of the polyisobutene-substituted succinic anhydride of Example 1, 363 grams of aminopropyl octadecylamine and 1314 grams of mineral oil is heated at 200 C. for 24 hours. The residue is filtered. The filtrate has a nitrogen content of 1.02%.
  • Example 49 A mixture of 1000 grams of the polyisobutene-substituted succinic anhydride of Example 1, and 258 grams of di-n-butylamine is heated at C. for 12 hours and then to 200 C./ 25 mm. The residue is diluted with 1157 grams of mineral oil and filtered. The filtrate has a nitrogen content of 0.8%.
  • Example 50 A mixture of 297 grams of the polyisobutene-substituted succinic anhydride of Example 1, 25 grams of melamine and 200 grams of mineral oil is heated at -260 C. for 9 hours and then at 290295 C. for 7 more hours. The residue is mixed with 50 grams of water, heated at reflux for 7 hours, dried and filtered. The filtrate has a nitrogen content of 2%.
  • Example 51 A mixture of 100 grams of the polyisobutene-substituted anhydride of Example 1 and 67 grams of mineral oil is heated to 50 C. To this mixture there is added 59 grams of an 85% aqueous solution of hydrazine hydrate. The mixture is heated at 100110 C. for 1.25 hours, diluted with toluene, and heated at 107 C. until no more water distills. Toluene is removed by distillation. The residue has a nitrogen content of 0.8%.
  • Example 52 A mixture of 1.0 equivalent of a mono-carboxylic acid (prepared by chlorinating a polyisobutene having a molecular weight of 750 to a product having a chlorine content of 3.6% by weight, converting the product to the corresponding nitrile by reaction with an equivalent amount of potassium cyanide in the presence of a catalytic amount of cuprous cyanide and hydrolyzing the resulting nitrile by treatment with 50% excess of a dilute aqueous sulfuric acid at the reflux temperautre) and 0.5 equivalent of ethylene diamine is mixed with twice its volume of xylene. The resulting mixture is heated at the reflux temperature until no more water is removed by distillation. The mixture is heated further and the xylene is 19 removed by distillation under reduced pressure. residue is the acylated nitrogen compound.
  • a mono-carboxylic acid prepared by chlorinating a polyisobutene having a molecular weight of 750 to a product having a chlorine content of 3.6% by weight, converting the
  • Example 53 A methyl ester of a high molecular weight mono-carboxylic acid is prepared by heating an equi-molar mixture of a chlorinated polyisobutene having a molecular weight of 1000 and a chlorine content of 4.7% by weight and methyl methacrylate at l40220 C. The resulting ester is then heated with a stoichiometrically equivalent amount of triethylene tetramine at 100200 C. to produce an acylated nitrogen compound of this invention.
  • Example 54 A dimethyl wax-substituted malonate is prepared by reacting dimethyl malonate with sodium ethoxide to form a sodium derivative of the ester, heating the sodium derivative with a brominated wax having 75 carbon atoms and 1 bromine atom per molecule.
  • a mixture of 1.0 equivalent of the ester of 1.0 equivalent of N,N-dibuty1 thiourea is dissolved in five times its volume of xylene. The resulting mixture is heated at the reflux temperature until no more water is removed by azeotropic distillation. The mixture is heated further and the xylene is removed by distillation. The residue is the acylated nitrogen compound.
  • Example 55 A high molecular weight mono-carboxylic acid is prepared by telomerizing ethylene with carbon tetrachloride to a telomer having an average of 35 ethylene radicals per molecule and hydrolyzing the telomer to the corresponding acid in accordance with the procedure described in British Patent No. 581,899.
  • a mixture of 1.5 equivalent of the acid and 0.75 equivalent of amino-propy-l octylamine is mixed with twice its volume of a mineral oil and twice its volume of xylene. The resulting mixture is heated at the reflux temperature until no more water is removed by azeotropic distillation. Xylene is then removed by distillation under reduced pressure and the residue is filtered.
  • Example 56 A mixture of 2000 grams of mineral oil, 3 equivalents of trimethylene diamine and 3 equivalents of a high molecular weight tricarboxylic acid prepared by the reaction of a brominated poly (l-hexene) having a molecular weight of 2000 and a bromine content of 4% by weight of 2-pentene-1,3,5-tricarboxylic acid (prepared by dehydration of citric acid) is heated at 150 C. for 20 hours. The residue is filtered to give a homogeneous mineral oil solution of the acylated nitrogen product.
  • a brominated poly l-hexene
  • 2-pentene-1,3,5-tricarboxylic acid prepared by dehydration of citric acid
  • Example 57 An equi-molar mixture of 2-aminoethyl morpholine and a mono-carboxylic acid (prepared by the reaction of ketene with a brominated poly(1-octene) having a molecular weight of 1500 and one atom of bromine per molecule) is diluted with three times its volume of xylene. The resulting mixture is heated at the reflux temperature until no more water is removed by distillation. The residue is an xylene solution of the :acylated nitrogen compound.
  • Example 58 A mixture of 1 equivalent of methane diamine and 1 equivalent of a high molecular glutaric acid-ester (prepared by the reaction of silver with an equi-molar mixture of beta-iodopropanoic acid and alpha-iodo derivative of the methyl ester of the mono-carboxylic acid of the preceding example) is diluted with an equal weight of a mineral oil and the resulting solution is heated at 180 C. until no more water distills. The residue is then filtered.
  • a high molecular glutaric acid-ester prepared by the reaction of silver with an equi-molar mixture of beta-iodopropanoic acid and alpha-iodo derivative of the methyl ester of the mono-carboxylic acid of the preceding example
  • Example 59 An equi-molar mixture of a technical ethylene amine mixture having an average composition corresponding to A high molecular weight dicarboxylic acid is prepared by reacting two moles of the Omega-brorno derivative of the hexapentacontanoic acid of the preceding example with one mole of zinc. The dicarboxylic acid is then treated with 2 equivalents of ethylene diamine to produce a diamide.
  • Example 61 A mixture of 1 equivalent of 1-aminoethyl-2-octadecylimidazoline with 1 equivalent of the high molecular weight monocarboxylic acid of Example is mixed with twice its volume of diphenyl oxide. The resulting mixture is heated at the reflux temperature until no more water distills. The residue is then filtered.
  • Example 62 A product is obtained by the procedure described in the preceding example except that N,N'-di-n-butyl-p-phenylenediamine (1 equivalent) is used in lieu of the imidazoline used.
  • Example 63 To a solution of 1 equivalent of di-methyl ester of a polyethylene (molecular weight of 1500)-substituted malonic acid in 5000 grams of xylene, there is added 1 mole of melamine at C. The resulting mixture is heated at the reflux temperature for 25 hours. The residue is mixed with 2000 grams of mineral oil and xylene is removed by heating the oil solution to 180 C./2 mm.
  • Example 64 A product is obtained by the procedure of Example 1, except that pyrrolidine (1 equivalent) is used in lieu of the diethylene triamine used.
  • Example 65 A product is obtained by the procedure of Example 1, except that hexahydro-1,3,5-triazine (1 equivalent) is used in lieu of the diethylene triamine used.
  • Example 66 A product is obtained by the procedure of Example 1, except that 1,3,4-dithiazolidine (1 equivalent) is used in lieu of the ethylene diamine used.
  • Example 67 A product is obtained by the procedure of Example 1, except that hexamethylene tetramine (2 equivalents) is used in lieu of the ethylene diamine used.
  • Example 68 A product is obtained by the procedure of Example 1, except that tripentylene tetramine (3 equivalents) is used in lieu of the ethylene diamine used.
  • Example 69 An equi-molar mixture of the polyisobutene-substituted succinic anhydride of Example 1 and N-octyl thiourea is diluted with an equal volume of xylene. The resulting mixture is heated at the reflux temperature for 30 hours. The residue is a xylene solution of the product.
  • Example 70 A product is obtained by the procedure of Example 69 except that oleylamide is used in lieu of the thiourea used.
  • Example 71 A product is obtained by the procedure of Example 69 except that 1,3-diphenyl guanidine is used in lieu of the thiourea used.
  • Example 72 A product is obtained by the procedure of Example 69 except that octadecamidine is used in lieu of the thiourea used.
  • Example 73 A product is obtained by the procedure of Example 69 except that guanylurea is used in lieu of the thiourea used.
  • Example 74 To a mixture of 396 grams of the polyisobutene-substituted succinic anhydride of Example 1 and 282 grams of mineral oil there was added 34 grams of N-methyltrimethylene diamine at 60 C. Within a period of one hour. The mixture was blown with nitrogen at 150- 155 C. for hours. The residue was found to have a nitrogen content of 1.41%.
  • Example 75 A mixture of 308 grams of mineral oil, 400 grams of the polyisobutene-substituted succinic anhydride of Example 1, and 70 grams of N-(2-ethylhexyl)-trimethylene diamine was prepared at 60 C. The mixture was heated to 250 C. and was then blown with nitrogen at 150- 155 C. for 5 hours. The residue had a nitrogen content of 1.4%.
  • Example 76 A mixture of 386 grams of mineral oil, 528 grams of the polyisobutene-suostituted succinic anhydride of Example 1, and 59 grams of N-(2-hydroxyethyl)-trimethylenediamine was prepared at 60 C. The mixture was blown with nitrogen at 150-155 C. for 5 hours. The residue had a nitrogen content of 1.56%.
  • Example 77 A mixture of 185 grams of mineral oil, 330 grams of the polyisobutene-substituted succinic anhydride of Example 1, and 88.5 grams of 1,4-bis(2-hydroxypropyl)-2- methyl piperazine was prepared at 60 C. The mixture was heated at 180-276 C./40 mm. for 14.5 hours. The residue had a nitrogen content of 1.12%.
  • Example 78 To a mixture of 314 grams of mineral oil and 430 grams of of the polyisobutene-substituted succinic anhydride of Example 1 there was added at 60 C., 49 grams of 1-(2-hydroxyethyl)piperazine. The mixture was heated to 150 C. and blown with nitrogen at this temperature for 5 hours. The residue had a nitrogen content of 1.38%.
  • Example 79 A mixture of 382 grams of mineral oil, 528 grams of polyisobutene-substituted succinic anhydride of Example 1, and 53 grams of 1-methyl-4-(3-aminopropyl)piperazine was prepared at 60 C., heated to 150 C., and blown with nitrogen at 150155 C. for 5 hours. The residue had a nitrogen content of 1.57%.
  • Example 80 To a mixture of 800 grams of the polyisobutene-substituted succinic anhydride of Example 1 and 175 grams of toluene there was added 77 grams of a commercial mixture of alkylene amines and hydroxy alkyl-substituted alkylene amines consisting of approximately 2% (by weight) of diethylene triamine, 36% of 1-(2-aminoethyl)piperazine, 11% of 1-(Z-hydroxyethyl)piperazine, 11% of NlZ-hydroxyethyl)ethylenediamine, and 40% of higher homologues obtained as a result of condensation of the above-indicated amine components.
  • the result- 22 ing mixture was heated at the reflux temperature for 16.5 hours whereupon 12 cc. of water was collected as the distillate. The residue was then heated to 160 C./25 mm. and diluted with 570 grams of mineral oil. The final product was found to have a nitrogen content of 1.57%.
  • Example 81 A product is obtained by the procedure of Example 69 except that an equimolar mixture of ammonia and bis(2-hydroxyethyl)amine is used in lieu of the thiourea used.
  • Example 82 A product is obtained by the procedure of Example 69 except that an equimolar mixture of benzidine is is used in lieu of the thiourea used.
  • Example 83 An alkenyl succinic anhydride in which the alkenyl group has less than 50 carbon atoms is prepared from a polyisobutylene having an average molecular weight of 375. This polymer is chlorinated to a chlorine content of 9.7% and then reacted with maleic anhydride. The resulting polyisobutenyl succinic anhydride has an acid number of 190 and an equivalent weight of 300. The procedure of Example 1 is followed using 1.0 equivalent of this polyisobutenyl succinic anhydride and 1.0 equivalent of Polyamine H. The resulting product then is diluted with mineral oil to a 58% solution therein; the nitrogen content is 3.2%
  • Example 84 Another alkenyl succinic anhydride in which the alkenyl group has less than 50 carbons is prepared by alkylation of maleic anhydride with tetra-propylene. Equivalent amounts of this tetrapropenyl succinic anhydride and triethylene tetramine in toluene are heated at reflux temperature until substantially all of the water is removed. The toluene then is removed by heating at 155 C. under reduced pressure and the residue is dissolved in mineral oil to a 60% solution. This oil solution is found to have a nitrogen content of 4.8%.
  • Example 85 A polyisobutene having an average molecular weight of 520 corresponding to 37 carbon atoms) is chlorinated to a chlorine content of 6.25% and then is made to react with an equivalent amount of maleic anhydride to yield a polyisobutene-substituted succinic anhydride having a saponification of 152. To 552 grams (1.5 equivalents) of this anhydride dissolved in 276 grams of mineral oil there is added at 60 C. 63 grams (1.5 equivalents) of Polyamine H portionwise over a period of 1 hour. The resulting mixture is heated for 6 hours at 150 C. and then blown with nitrogen at this temperature for 1 hour. The residue is diluted with grams of mineral oil and the final oil solution is found to have a nitrogen content of 2.1%.
  • Example 87 A mixture of 1 equivalent of N-butyl maleimide and 1 equivalent of a chlorinated polyisobutene having a chlorine content of 4.33% and a molecular wieght of 850 is heated at 100 C".210 C. in nitrogen atmosphere and then heated at l03114 C./12l mm. The reaction mixture is then filtered and the filtrate is an N-butyl polyisobutene substituted succinimide having a nitrogen content of 1.23%. A mixture of this substituted N-butyl succinimide (177 grams, 0.156 equivalent of nitrogen) and tetraethylene pentamine (12.8 grams, 0.311 equivalent of nitrogen) is diluted with mineral oil (86 grams) and heated at 150158 C. in nitrogen atmosphere.
  • the reaction mixture is diluted with mineral oil (41 grams) and filtered.
  • the filtrate is blown with nitrogen at 190204 C. for 5 hours, heated at 140/1 mm. and again blown with nitrogen at 24025S C. for 5.9 hours.
  • the mixture is filtered.
  • the filtrate is an oil solution of an acylated polyamine and has a nitrogen content of 1.13
  • Example 88 A mixture of 1 equivalent of maleic anhydride and 2 equivalents of tetraethylene pentamine is heated at a temperature of 100-180 C. to form an intermediate product. The intermediate product is then mixed with 1 equivalent of a chlorinated polyisobutene having a chlorine content of 4% and a molecular weight of 1500 at 150-2l0 C. The product is diluted with equal Weight of mineral oil and filtered. The filtrate is an oil solution of the acylated polyamine.
  • Example 89 The procedure of Example 88 is repeated except the chlorinated polyisobutene is replaced on a weight basis with a polyisobutene having a molecular weight of 2000.
  • Example 90 A polyisobutene having a molecular weight of 1000 (1000 grams) and maleic anhydride (100 grams), is heated at 150220 C. to form a polyisobutene-substituted maleic anhydride. The anhydride is then mixed with tetraethylene pentamine (1.5 equivalents per equivalent of anhydride) and the mixture is heated at 18020'0 C. to form an acylated polyamine.
  • Example 91 An acid producing compound is prepared by heating chloromaleic anhydride (1 equivalent) and 1 equivalent of a chlorinated polyisobutene having a chlorine content of 4% and a molecular weight of 2500 at 150200 C. The product of the reaction is then mixed with tetraethylene pentamine (2.5 equivalents) at 50 C. and the mixture is heated at 180-210 C. to form an acylated polyamine.
  • Example 92 A substituted monocarboxylic acid producing compound is obtained by reacting acrylic acid (1 equivalent) with a chlorinated polyisobutene (1 equivalent) having a chlorine content of 4.5% and a. molecular weight of 850 at 150200 C. The product of the reaction is then mixed with 1.25 equivalents of pentaethylene hexamine at 5075 C. and the resulting mixture is heated at 180-200 C. to form an acylated polyamine.
  • Example 93 The procedure of Example 92 is repeated except that the acrylic acid is replaced on a chemically equivalent basis with alpha-chloroacrylic acid and the pentaethylene hexamine is replaced on a nitrogen basis with ethylene diamine.
  • Example 94 The procedure of Example 91 is repeated except that the acid-producing compound used is one which is obtained by the reaction (Haloform reaction) of methyl heptapentacontanyl ketone with iodine, sodium hydroxide, and acidification of the haloform product.
  • the acid-producing compound used is one which is obtained by the reaction (Haloform reaction) of methyl heptapentacontanyl ketone with iodine, sodium hydroxide, and acidification of the haloform product.
  • Example 95 The procedure of Example 91 is repeated except that the acid-producing compound used is one which is obtained by the reaction of equivalent amounts of the chlorinated polyisobutene with methyl ester of N-butyl maleamic acid.
  • Example 96 The polyisobutene-substituted succinimide is obtained by reacting the polyisobutene-substituted succinic anhydride of Example 1 with ammonia (0.5 equivalent per equivalent of the anhydride). A mixture of the succinimide (1 equivalent of nitrogen) and tetraethylene penta mine (1 equivalent of nitrogen) is diluted with an equal weight of mineral oil and heated at 180 -250 C. to effect trans-amidation. The product is an acylated tetraethylene pentamine.
  • Example 97 The procedure of Example 96 is repeated except that the succinimide is N-methyl polyisobutene-substituted succinimide obtained by reacting the corresponding polyisobutene-substituted succinic anhydride with methylamine (0.5 equivalent per equivalent of the anhydride).
  • Example 98 The procedure of Example 96 is repeated except that the succinimide is N phenyl polyisobutene-substituted succinimide obtained by reacting the corresponding polyisobutene-substituted succinic anhydride with aniline (0.5 equivalent per equivalent of the anhydride).
  • Example 99 A polyisobutene-substituted succinamide is obtained by reacting 1 equivalent of the polyisobutene-substituted succinic anhydride of Example 1 with 1 equivalent of dimethylamine. The succinamide so obtained is then reacted with 2 equivalents of pentaethylene hexamine at 160-210 C. to effect trans-amidation and form an acylated polyamine.
  • Example 100 The procedure of Example 88 is repeated except that maleic anhydride used is replaced with itaconic acid on a stoichiometrically equivalent basis.
  • acylated nitrogen-containing composition is usually present in lubricating oils in amounts ranging from about 0.1% to about 10% by weight.
  • the optimum amounts for a particular application depend to a large measure upon the type of surface to which the lubricating composition is to be subjected.
  • lubricating compositions for use in gasoline internal combustion engines may contain from about 0.5 to about 5% of an acylated nitrogen-containing composition, whereas lubricating compositions for use in gears and diesel engines may contain as much as 10% or even more of the additive.
  • additives include, for example, detergents of the ash-containing type, viscosity index improving agents, pour point depressing agents, anti-foam agents, extreme pressure agents, rust-inhibiting agents, and oxidation and corrosion inhibiting agents.
  • the ash-containing detergents are exemplified by oilsoluble neutral and basic salts of alkali or alkaline earth metals with sulf-onic acids, carboxylic acids, or organic phosphorus acids characterized by at least one direct carbon-to-phosphorus linkage such as those prepared by the treatment of an olefin polymer (e.g., polyisobutene having a molecular weight of 1000) with a phosphorizing agent such as phosphorus trichloride, phosphorus heptasulfide, phosphorus pentasulfide, phosphorus trichloride and sulfur, white phosphorus and a sulfur halide, or phosphorothioic chloride.
  • olefin polymer e.g., polyisobutene having a molecular weight of 1000
  • a phosphorizing agent such as phosphorus trichloride, phosphorus heptasulfide, phosphorus pentasulfide,
  • the term basic salt is used to designate the metal salts wherein the metal is present in stoichiometrically larger amounts than the organic acid radical.
  • the commonly employed methods for preparing the basic salts involves heating a mineral oil solution of an acid with a stoichiometric excess of a metal neutralizing agent such as the metal oxide, hydroxide, carbonate, bicarbonate, or sulfide at a temperature above 50 C. and filtering the resulting mass.
  • a metal neutralizing agent such as the metal oxide, hydroxide, carbonate, bicarbonate, or sulfide
  • Examples of compounds useful as the promoter include phenolic substances such as phenol, naphthol, alkylphenol, thiophenol, sulfurized alkylphenol, and condensation products of formaldehyde with a phenolic substance; alcohols such as methanol, 2-propanol, octyl alcohol, cellosolve, carbitol, ethylene glycol, stearyl alcohol, and cyclohexyl alcohol; amines such as aniline, phenylenediamine, phenothiazine, phenylbeta-naphthylamine, and dodecylamine.
  • a particularly effective method for preparing the basic salts comprises mixing an acid with an excess of a basic alkaline earth metal neutralizing agent, a phenolic promoter compound, and a small amount of water and carbonating the mixture at an elevated temperature such as 60-200 C.
  • chlorinated aliphatic hydrocarbons such as chlorinated wax
  • organic sulfides and polysulfides such as benzyl disulfide, bis- (chlorobenzyDdisulfide, dibutyl tetrasulfide, sulfurized sperm oil, sulfurized methyl ester of oleic acid, sulfurized alkyphenol, sulfurized dipentene, and sulfurized terpene
  • phosphosulfurized hydrocarbons such as the reaction product of a phosphorus sulfide with turpentine or methyl oleate
  • phosphorus esters including principally dihydrocarbon and trihydrocarbon phosphites such as dibutyl phosphite, diheptyl phosphite, dicyclohexyl phosphite, pentyl phenyl phosphite, dipentyl phen
  • the lubricating compositions may also contain metal detergent additives in amounts usually within the range of about 0.1% to about 20% by weight. In some applications such as in lubricating marine diesel engines the lubricating compositions may contain as much as of a metal detergent additive. They may also contain extreme pressure addition agents, viscosity index improving agents, and pour point depressing agents, each in amounts within the range of from about 0.1% to about 10%.
  • Example B SAE 30 mineral lubricating oil containing 0.75% of the product of Example 2 and 0.1% of phosphorus as the barium salt of di-n-nonylphosphorodithioic acid.
  • Example C SAE 10W-30 mineral lubricating oil containing 0.4% of the product of Example 7.
  • Example D SAE mineral lubricating oil containing 0.1% of the product of Example 7 and 0.15% of the zinc salt of an equimolar mixture of di-cylohexylphosphorodithioic acid and di-isobutyl phosphorodithioc acid.
  • Example E SAE 30 mineral lubricating oil containing 2% of the product of Example 3.
  • Example F SAE 20W-30 mineral lubricating oil containing 5% of the product of Example 14.
  • Example G SAE 10W-30 mineral lubricating oil containing 1.5% of the product of Example 25 and 0.05% of phosphorous as the zinc salt of a phosphorodithioic acid prepared by the reaction of phosphorus pentasulfide with a mixture of 60% (mole) of p-butylphenol and 40% (mole) of npentyl alcohol.
  • Example I SAE 10W-30 mineral lubricating oil containing 2% of the product of Example 48, 0.06% of phosphorus as zinc di-n-octyl-phosphorodithioate, and 1% of sulfate ash as barium mahogany sulfonate.
  • Example I SAE 10W-30 mineral lubricating oil containing 6% of the product of Example 60, 0.075% of phosphorus as zinc di-n-octylphosphorodithioate, and 5% of the barium salt of an acidic composition prepared by the reaction of 1000 parts of a polyisobutene having a molecular weight of 60,000 with parts of phosphorus pentasulfide at 200 C. and hydrolyzing the product with steam at C.
  • a basic calcium detergent prepared by carbonating a mixture comprising mineral oil, calcium mahogany sulfonate and 6 moles of calcium hydroxide in the presence of an equi-molar mixture 10% of the mixture) of methyl alcohol and n-butyl alcohol as the promoter at the reflux temperature.
  • Example SAE 10 mineral lubricating oil containing 2% of the product of Example 7, 0.07% of phosphorus as zinc diocytlphosphorodithioate, 2% of a barium detergent prepared by neutralizing with barium hydroxide the hydrolyzed reaction product of a polypropylene (molecular weight 2000) with 1 mole of phosphorus pentasulfide and 1 mole of sulfur, 3% of a barium sulfonate detergent prepared by carbonating a mineral oil solution of mahogany acid, and a 500% stoichiometrically excess amount of barium hydroxide in the presence of phenol as the promoter at 180 C., 3% of a supplemental ashless detergent prepared by copolymerizing a mixture of 95% (weight) of decyl-methacrylate and (weight) of diethylamino-ethylacrylate.
  • Example Q SAE 10 mineral lubricating oil containing 3% of the product of Example 16, 0.075% of phosphorus as the zinc salt of a phosphorodithioic acid prepared by the reaction of phosphorus pentasulfide with an equimolar mixture of n-butyl alcohol and dodecyl alcohol, 3% of a barium detergent prepared by carbonating a mineral oil solution containing 1 mole of sperm oil, 0.6 mole of octylphenol, 2 moles of barium oxide, and a small amount of water at 150 C.
  • crankcase lubricant used in taxicabs which had been operated for over 50,000 miles each.
  • ten 6-cylinder 1958 Chevrolet cars (with no oil filters) were operated as a fleet of taxicabs.
  • the crankcase lubricant was a solvent refined Mid-Continent petroleum oil having a viscosity of 185 SUS/ F. and a viscosity index of 112, and containing 5.9% by volume of a poly-alkylrnethacrylate viscosity index improver and 0.59% by volume of a zinc dialky'l phosphorodithioate (the alkyl groups being isobutyl and a mixture of primary amyl).
  • Crankcase oil drains were taken from each car at oilchange intervals of about 3,000 miles of service and these drains combined.
  • a 30-cc. sample of each of the combined drains was mixed with 1% by weight of the dispersant additive to be tested and 2% by weight of water. This mixture then was homogenized, placed in a 100-cc. graduated cone-shaped centrifuge tube and centrifuged for two hours at 1500 rpm.
  • the various dispersants were evaluated by noting the volume of deposited sediment in terms of cubic centimeters and also the turbidity of the supernatant oil layer. It is apparent that the more effective dispersants will give test results which show a minimum of deposited sediment and a relatively hazy supernatant oil layer.
  • the clarity of the supernatant oil layer was determined by the amount of light transmitted through it from a 3-volt, 0.75 watt incandescent bulb.
  • the dispersant properties of the compositions of this invention may be illustrated also by the results of an oxidation-dispersancy test which is useful as a screening test for determining the effectiveness of the dispersant additive under light-duty service conditions.
  • a 350-cc. sample of a lubricating oil containing the dispersant additive is placed in a 2 x 15" borosilicate tube.
  • a 1%" x 5%" SAE 1020 steel panel is immersed in the oil.
  • the sample then is heated at 300 F. for 48 hours while air is bubbled through the oil at the rate of 10 liters per hour.
  • the oxidized sample is cooled to F., homogenized, allowed to stand at room temperature for 24 hours and then filtered through two layers of No.
  • Two modifications of the above procedure may be employed; both make the test more severe: one consists of extending the test from 48 hours to 96 hours, and the other involves adding 0.5 of water, based on the weight of the test sample, to the oxidized oil before homogenization.
  • the lubricating oil employed in this test was a Mid-Continent conventionally refined petroleum oil having a viscosity of about 200 SUS/ 100 F., and
  • the engine is dismantled and various parts of the engine are examined for engine deposits.
  • the lubricant dispersant addition agent is then rated according to 1) the extent of piston ring-filling, (2) the amount of sludge formed in the engine (on a scale of 80*0, 80 being indicative of no sludge and 0 being indicative of extremely heavy sludge), and (3) the total amount of engine deposits, i.e., sludge and varnish, formed in the engine (on a scale of 100-0, 100 being indicative of no deposits and 0 being indicative of extremely heavy deposits).
  • Table III The results are summarized in Table III.
  • a composition comprising a major proportion of a lubricating oil and a minor proportion sufficient to impart detergency thereto of an oil-soluble acylated nitrogen compound characterized by the presence within its structure of (A) a substantially saturated hydrocarbonsubstituted polar group selected from the class consisting of acyl, acylimidoyl, and acyloXy radicals wherein the substantially saturated hydrocarbon substituent contains at least about 50 aliphatic carbon atoms and (B) a nitrogen-containing group characterized by a nitrogen atom attached directly to said polar radical.
  • composition of claim 1 wherein the hydrocarbon substituent contains at least about 25 aliphatic carbon atoms per each polar radical.
  • composition of claim 1 wherein the hydrocarbon substituent is a polymer of butene.
  • composition of claim 1 wherein the hydrocarbon substituent is a polyisobutene having a molecular Weight within the range from about 700 to about 100,000.
  • composition of claim 1 wherein the nitrogencontaining group has the formula wherein R and R are selected from the group consisting of hydrogen, hydrocarbon, amino-substituted hydrocarbon, hydroxy-substituted hydrocarbon, alkoxy-substituted hydrocarbon, amino, carbamyl, thiocaribamyl, guanyl, and acylimidoyl radicals.
  • a composition comprising a major proportion of a lubricating oil and a minor proportion sufficient to impart detergency thereto of an oil-soluble acylated nitrogen compound characterized by the presence within its structure of (A) a substantially saturated hydrocarbonsubstituted succinic radical selected from the class consisting of succinoyl, succinoylimidoyl, and succinoyloxy radicals and having at least about 50 aliphatic carbon atoms in the substantially saturated hydrocarbon substituent and (B) an amino group characterized by a nitrogen atom attached directly to said succinic radical.
  • a composition comprising a major proportion of a lubricating oil and a minor proportion sufficient to impart detergency thereto of an oil-soluble acylated nitrogen compound characterized by the presence within its structure of (A) an olefin polymer-substituted succinic radical selected from the class consisting of succinoyl, succinimidoyl, and succinoyloxy radicals, said olefin polymer having a molecular weight within the range from about 700 to about 50,000 and being a polymer of a 1- mono-olefin having from 2, to about 8 aliphatic carbon atoms, and (B) a nitrogen-containing group characterized by at least one nitrogen atom attached directly to said succinic radical, said nitrogen-containing group being derived from an alkylene amine.
  • A an olefin polymer-substituted succinic radical selected from the class consisting of succinoyl, succinimidoyl, and succinoyloxy radicals, said olefin
  • a composition comprising a major proportion of a lubricating oil and a minor proportion sufficient to impart detergency thereto of an oil-soluble acylated nitrogen-containing composition prepared by the process comprising rcacting at a temperature of from about C. and up to the decomposition point a high molecular weight acid-producing compound characterized by the presence within its structure of a high molecular weight oil-solubiliz'ing substantially saturated group having at least about 50 aliphatic carbon atoms and at least one acid-producing group having the structural configuration 2 moles, per equivalent of said acid producing compound, of a nitrogen-containing compound characterized by the 31 presence within its structure of at least one radical having the structural configuration 1I]' H 9.
  • composition of claim 8 wherein the high molecular weight acid-producing compound is selected from the group consisting of substituted succinic acids having the structural formula RC
  • composition of claim 8 wherein the nitrogencontaining compound is characterized by the structural formula RNH Iii!
  • structural formula R and R" are selected from the group consisting of hydrogen, hydrocarbon, amino-su'bstituted hydrocarbon, alkoxy-substitut ed hydrocarbon, amino, carbamyl, thiocarbamyl, guanyl, and acyl-imidoyl radicals.
  • composition of claim 8 wherein the nitrogencontaining compound is a polyethylene polyamine.
  • a lubricating composition comprising a major proportion of a lubricating oil and a minor proportion, sufficient to impart detergency thereto, of an amide having the structural formula wherein x is at least 1, R is a substantially saturated hydrocarbon group having at least about 50 aliphatic carbon atoms and at least about 25 aliphatic carbon atoms for each unit of x, and NR' is selected from the class consisting of (A) radicals derived from an alkylene polyamine by the removal of a hydrogen atom from an amino group and (B) radicals derived from an alkylene polyamine by the removal of a hydrogen atom from an amino group and characterized by the presence, on the nitrogen atom of at least one additional amino group, of a complex substituent having the formula 13.
  • a lubricating composition comprising a major proportion of a lubricating oil and a minor proportion, sufficient to impart detergency thereto, of an amide having the structural formula wherein x is at least 1, R is a substantially saturated hydrocarbon group having at least about 50 aliphatic carbon atoms and at least about 25 aliphatic carbon atoms for each unit of x, and NR is selected from the class consisting of (A) radicals derived from an ethylene polyamine by the removal of a hydrogen atom from an amino group and (B) radicals derived from an ethylene polyamine by the removal of a hydrogen atom from an amino group and characterized by the presence, on the nitrogen atom of at least one additional amino group, of a complex substituent having the formula 14.
  • the lubricating composition of claim 12 wherein R of the structural formula is a polyisobutene group having a molecular weight of from about 750 to 5000, x is about 1, and NR' is derived from an ethylene polyamine having from 2 to 8 amino groups by the removal of a hydrogen atom from an amino group and characterized by the presence, on the nitrogen atom of at least one additional amino group, of a complex substitutent having the formula 15.
  • the composition of claim 8 wherein the oil-soluble acylated nitrogen-containing composition is prepared by a process which comprises reacting at a temperature within the range of from about C. to about 250 C.
  • a substantially saturated hydrocarbon substituted succinicacid-proclucing compound having at least about 50 aliphatic carbon atoms in the substantially saturated hydrocarbon substituent with from about one-half equivalent to about 2 moles, per equivalent of said succinic-acidproducing compound, of an alkylene polyamine.
  • composition of claim 8 wherein the oil-soluble acylated nitrogen-containing composition is prepared by a process which comprises reacting at a temperature within the range of from about 80 C. to about 250 C. a substantially saturated hydrocarbon substituted succinicacid-producing compound having at least about 50 aliphatic carbon atoms in the substantially saturated hydrocarbon substituent with from about one-half equivalent to about 2 moles per equivalent of said succinic-acidproducing compound, of a polyethylene polyamine.
  • composition of claim 8 wherein the oil-soluble acylated nitrogen-containing composition is prepared by a process which comprises reacting at a temperature within the range of from about 80 C. to about 250 C. a substantially saturated hydrocarbon substituted succinicacid-producing compound having at least about 50 aliphatic carbon atoms in the substantially saturated hydrocarbon substituent with from about one-half equivalent to about 2 moles, per equivalent of said succinic-acidproducing compound, of a hydroxyalkyl amine.
  • composition of claim 1 wherein it contains additionally an ash-containing detergent is additionally present.

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  • Chemical & Material Sciences (AREA)
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  • Lubricants (AREA)

Description

United States Patent Office Fatented Sept. 13, 1966 3,272,746 LUBIRECATING COMPUSHIUN CUNTAHNING AN ACYLATED NITROGEN COMPQUND William M. Le Suer, Cleveland, and George R. Norman,
Lyndhurst, Uhio, assignors to The Lnbrizol Corporation, Wickiiiie, ()hio, a corporation of Qhio No Drawing. Filed Nov. 22, 1965, Ser. No. 509,172 18 Claims. (Cl. 252-475) This is a continuation-in-part of copending application Serial No. 126,809 filed July 21, 1961, now U.S. 3,219,666 which was a continuation-in-part of application Serial No. 802,667 filed March 30, 1959, now U.S. 3,172,892. This application is also a continuation-in-part of copending application Serial No. 437,547 filed March 5, 1965, now abandoned and copending application Serial No. 468,948 filed July 1, 1965.
This invention relates to oil-soluble nitrogen-containing compositions and to the process of preparing the same. The compositions of this invention are useful as dispersing agents in lubricants, especially lubricants intended for use in the crankcase of internal combustion engines, gears, and power transmitting units.
One of the principal problems associated with present day crankcase lubricants is that posed by the inevitable presence in the lubricant of foreign particles such as dirt, soot, water and decomposition products resulting from breakdown of the lubricating oil. Even if there were none of this latter contaminant present the very nature of the design of the modern internal combustion engine is such that a significant amount of foreign matter will accumulate in the crankcase. Perhaps the most important of these contaminants is water because it seems to be responsible for the deposition of a mayonnaise-like sludge. It appears that if there were no water present the solid components of the mayonnaise-like sludge would circulate with the oil and be removed by the oil filter. It will be readily appreciated that the deposition of the sludge presents a serious problem with respect to the eflicient operation of the engine and that it is desirable to prevent such deposition of sludge-like material.
The presence of water and the precursors of sludge in a lubricating oil is dependent largely upon the operating temperature of the oil. If the oil is operated at a high temperature the water, of course, will be eliminated by evaporation about as fast as it accumulates. In the absence of water as stated above the other foreign particles will be removed by the filter. At low oil temperatures, on the other hand, water will accumulate and so consequently will sludge. It is apparent that the environment in which a crankcase lubricant is maintained will determine to a large extent the ultimate performance of that lubricant.
High operating temperatures are characteristic of a lubricant in an engine that is run at relatively constant high speed. Thus, in an engine that is run at 60 miles per hours for a long period of time it is very unlikely that there will be any accumulation of water and it is similarly unlikely that there will be any formation and deposition of sludge, but in ordinary stop-and-go driving such as is the case with taxicabs, delivery trucks, police cruisers, etc., the crankcase lubricant will be alternately hot and cold, an ideal environment for the accumulation of water. In such cases the formation of sludge is a serious problem. This problem has been with the automotive industry for many years and its solution has been approached by the use of known detergents such as metal phenates and sulfonates but without notable success. Although such known detergents are very effective in solving the detergency problems associated with motor oils at high temperatures they have not been particularly effective in solving the problems associated with low temperature operation or, to put it better, those problems which are associated with crankcase lubricants in engines which are operated at alternating high and low temperatures.
It is accordingly, a principal object of this invention to provide novel compositions of matter.
It is also an object of this invention to provide compositions which are adapted for use as additives in hydrocarbon oils.
It is also an object of this invention to provide compositions which are effective as detergents in lubricating compositions.
It is another object of this invention to provide a novel process for the preparation of products which are effective as dispersants in lubricant compositions.
It is another object of this invention to provide novel compositions which are effective dispersants in lubricant compositions intended for use in engines operated at alternating high and low temperatures.
It is another object of this invention to provide improvide hydrocarbon oil compositions.
It is another object of this invention to provide improved lubricating compositions.
It is another object of this invention to provide improved fuel compositions.
These and other objects are achieved in accordance with this invention by providing a detergent composition comprising an oil-soluble, acylated nitrogen composition characterized by the presence Within its structure of (A) a hydrocarbon-substituted polar group selected from the class consisting of acyl, acylimidoyl, and acyloxy radicals wherein the substantially hydrocarbon substituent contains at least about 50 aliphatic carbon atoms and (B) a nitrogen-containing group characterized by a nitrogen atom attached directly to said relatively polar group.
A critical aspect of this invention is the size of the hydrocarbon substituent in the acylated nitrogen compounds. Thus, only acylated nitrogen compositions having at least about 50 aliphatic carbon atoms in the hydrocarbon substituent are contemplated as being within the scope of this invention. Furthermore, in the case of acylated nitrogen compositions having two or more polar groups in a molecule, the hydrocarbon substituent must then contain at least about 25 aliphatic carbon atoms per each polar group. This lower limit is based not only upon the consideration of the oilsolubility of the acylated nitrogen compositions but also upon the effectiveness of such compounds as additives in hydrocarbon oils for the purposes of this invention. It has now been discovered that while acylated nitrogen compositions having less than the minimum number of such aliphatic carbon atoms may be sufi iciently oil-soluble, they nevertheless are not sufficiently effective to be useful as additives of this invention. Furthermore, it has been discovered that their effectiveness diminishes sharply with a corresponding decrease in the size of the hydrocarbon substituent so that acylated nitrogen compositions having less than about 35 aliphatic car-hon atoms in such substituent either are ineffective or produce detrimental results when added to a hydrocarbon oil.
Another important aspect of this invention is the structural constitution of the hydrocarbon substituent. Thus, the radical preferably should be substantially saturated, i.e., at least about of the total number of carbonto-carbon covalent linkages are saturated linkages. An excessive proportion of unsaturated linkages renders the molecule susceptible to oxidation, degradation, and polymerization and results in products unsuitable for use in hydrocarbon oils in many applications.
The hydrocarbon substituent of the acylated nitro gen compositions of this invention preferably should be substantially free from large oil-solubilizing pendant groups, i.e., groups having more than about 6 aliphatic carbon atoms. While some large oil-solubilizing pendant groups may be present, they preferably should be present in proportions less than about one such group for every 25 aliphatic carbon atoms in the main hydrocarbon chain. A higher proportion of large pendant groups impairs the effectiveness of the acylated nitrogen compositions of this invention as additives in hydrocarbon oils.
The hydrocarbon substituent may contain polar substituents provided, however, that the polar substituents are not present in proportions sufficiently large to alter significantly the hydrocarbon character of the radical. The polar substituents are exemplified by chloro, bromo, keto, ethereal, aldehydro, nitro, etc. The upper limit with respect to the proportion of such polar substituents in the radical is approximately based on the weight of the hydrocarbon portion of the radical.
The sources of the hydrocarbon substituent include principally the high molecular weight substantially saturated petroleum fractions and substantially saturated olefin polymers, particularly polymers of mono-olefins having from 2 to about 30 carbon atoms. The especially useful polymers are the polymers of l-monoolefins such as ethylene, propene, l-butene, isobutene, I-hexene, l-octene, 2-methyl-1-heptene, 3-cyclohexyl-1- butene, and 2-methyl-5-propyl-l-hexene. Polymers of medial olefins, i.e., olefins in which the olefinic linkage is not at the terminal position, likewise are useful. They are illustrated by Z-butene, 3-pentene, and 4-octene.
Also useful are the interpolymers of the olefins such as those illustrated above with other interpolymerizable olefinic substances such as aromatic olefins, cyclic olefins, and polyolefins. Such interpolymers include, for example, those prepared "by polymerizing isobutene with styrene; isobutene with butadiene; propene with isoprene; ethylene with piperylene; isobutene with chloroprene; isobutene with p-methyl styrene; l-hexene with 1,3-hexadiene; l-octene with l-hexene; I-heptene with l-pentene, 3-methyl-1-butene with l-octene; 3,3-dimethyl-l-pentene with l-hexene; isobutene with styrene and piperylene; etc.
The relative proportions of the mono-olefins to the other monomers in the interpolymers influence the stability and oil-solubility of the final acylated nitrogen compositions derived from such interpolymers. Thus, for reasons of oil-solubility and stability the interpolymers contemplated for use in this invention should be substantially aliphatic and substantially saturated, i.e., they should contain at least about 80%, preferably at least about 95%, on a weight basis of units derived from the aliphatic mono-olefins and no more than about 5% of olefinic linkages based on the total number of carbon-to-carbon covalent linkages. In most instances, the percentage of olefinic linkages should be less than about 2% of the total number of carbon-tocarbon covalent linkages.
Specific examples of such interpolymers include copolymer of 95% (by weight) of isobutene with 5% of styrene; terpolymer of 98% of isobutene with 1% of piperylene and 1% of chloroprene; terpolymer of 95% of isobutene with 2% of 1-butene and 3% of l-hexene; terpolymer of 60% of isobutene with of l-pentene and 20% of l-octene; copolymer of 80% of l-hexene and 20% of l-heptene; terpolymer of 90% of isobutene with 2% of cyclohexene and 8% of propene; and copolymer of 80% of ethylene and 20% of propene.
Another source of the substantially hydrocarbon radical comprises saturated aliphatic hydrocarbons such as highly refined high molecular weight white oils or synthetic alkanes such as are obtained by hydrogenation of high molecular weight olefin polymers illustrated above or high molectular weight olefinic substances.
The use of olefin polymers having molecular weights of about 7505000 is preferred. Higher molecular weight olefin polymers having molecular weights from about 10,000 to about 100,000 or higher have been found to impart also viscosity index improving properties to the acylated nitrogen compositions of this invention. In many instances the use of such higher molecular weight olefin polymers is desirable. On the other hand, olefin polymers having molecular weights less than about 700 are not useful.
The relatively polar group of the acylated nitrogen compositions is selected from the class consisting of acyl, acylimidoyl, and acyloxy radicals. These radicals have the following structural configurations, respectively:
NR2 R1("], R1(i7and Ri( JO- wherein R represents the substantially hydrocarbon substituent described hereinbefore and R represents a hydrogen radical or an organic radical such as a hydrocarbon radical or a polar-substituted hydrocarbon radical.
The nitrogen-containing group of the acylated nitrogen compositions of this invention is derived from compounds characterized by a radical having the structural configuration The two remaining valences of the nitrogen atom of the above radical preferably are satisfied by hydrogen, amino, or organic radicals bonded to said nitrogen atom through direct carbon-to-nitrogen linkages. Thus, the compounds from which the nitrogen-containing group may be derived include principally ammonia, aliphatic amines, aromatic amines, heterocyclic amines or carbocyclic amines. The amines may be primary or secondary amines and may also be polyamines such as alkylene amines, arylene amines, cyclic polyamines, and the hydroxy-substituted derivatives of such polyamines.
Specific amines of these types are methylamine, N- methylethylamine, N-methyl-octylamine, N-cyclohexylanaline, dibutylamine, cyclohexylamine, aniline, di(pmethylphenyl)amine, dodecylamine, octadecylamine, ophenylenediamine, N,N di-n-butyl-p-phenylenediamine, mor-pholine, piperazine, tetrahydropyr-azine, indole, hexahydro-1,3,5-triazine, 1-H-1,2,4-triazole, melamine, bis-(paminophenyl)methane, phenyl-methylenimine, menthanediamine, cyclohexamine, pyrrolidine, 3-amino-5,6-diphenyl-1,2,4 triazine, quinonediimine, 1,3 indandiimine, 2- octadecyl-imidazoline, 2 phenyl-4-methyl-imidazolidine, oxazolidine, ethanolamine, diethanolamine, and 2-heptyloxazolidine.
A preferred source of the nitrogen-containing group consists of polyamines, especially alkylene amines conforming for the most part to the formula HN alky1eue-N H l K i).
wherein n is an integer preferably less than about 10, A is a substantially hydrocarbon or hydrogen radical, and the alkylene radical is preferably a lower alkylene radical having less than about 8 carbon atoms. The alkylene amines include principally methylene amines, ethylene amines, butylene amines, propylene amines, pentylene amines, hexylene amines, heptylene amines, octylene amines, other polymethylene amines, and also the cyclic and the higher homologs of such amines such as piperazines and amino-alkyl-substituted piperazines. They are exemplified specifically by: ethylene diamine, triethylene.
tetramine, propylene diamine, decamethylene diamine, octamethylene diamine, di(heptamethylene)tria-mine, tripropylene tetramine, tetraethylene pentamine, trimethylene diamine, pen-taethylene hexamine, di(trimethylene triamine, 2-heptyl-3- Z-aminopropyl irnidazoline, 4-methylimidazoline, 1,3 -bis (Z-aminoethyl imidazo- Iline, pyrimidine, 1-(2-aminopropyl)piperazine, l,4-bis(2- aminoethyl)piperazine, and 2-methyl-1-(2-aminobutyl) piperazine. High homologs such as are obtained by condensing two or more of the above illustrated alkylene amines likewise are useful.
The ethylene amines are especially useful. They are described in some detail under the heading Ethylene Amines in Encycylopedia of Chemical Technology Kirk and Othmer, volume 5, pages 898905, Interscience Publishers, New York (1950). Such compounds are prepared most conveniently by the reaction of an alkylene chloride with ammonia. The reaction results in the production of somewhat complex mixtures of alkylene amines, including cyclic condensation products such as piperazines. These mixtures find use in the process of this invention. On the other hand, quite satisfactory products may be obtained also by the use of pure alkylene amines. An especially useful alkylene amine for reasons of economy as well as effectiveness of the products derived therefrom is a mixture of ethylene amines prepared by the reaction of ethylene chloride and ammonia and having a composition which corresponds to that of tetraethylene pentamine.
Hydroxyalkyl-substituted alkylene amines, i.e., alkylene amines having one or more hydroxyalkyl substituents on the nitrogen atoms, likewise are contemplated for use herein. The hydroxyalkyl-substituted alkylene amines are preferably those in which the alkyl group is a lower alkyl group, i.e., having less than about 6 carbon atoms. Examples of such amines include N-(2-hydroxyethyl) ethylene diamine, N,N' bis(2 hydroxyethyl)ethylene diamine, 1-(Z-hydroxyethyl)piperazine, mono-hydroxypropyl-substituted diethylene triamine, 1,4-bis(2-hydroxypropyl) piperazine, di-hydroxypropyl-substituted tetraethylene pentamine, N-(3-hydroxypropyl)tetramethylene diamine, and 2-heptadecyl-1-(2-hy droxyethyl) imidazoline.
Higher homologs such as are obtained by condensation of the above-illustrated alkylene amines or hydroxy alkyl-substituted alkylene amines through amino radicals or through hydroxy radicals are likewise useful. It will be appreciated that condensation through amino radicals results in a higher amine accompanied with removal of ammonia and that condensation through the hydroxy radicals results in products containing ether linkages accompanied with removal of water.
Other sources of the nitrogen-containing group include ureas, thioureas, hydrazines, guanidines, amidines, amides, thioamides, cyanamides, etc. Specific examples illustrating such compounds are: hydrazine, phenylhydrazine, N, N'-diphenylhydrazine, octadecylhydrazine, benzoylhydrazine, urea, thiourea, N-butylurea, stearylamide, oleylamide, guanidine, 1,3-diphenylguanidine, 1,2,3-tributylguanidine, benzamidine, octadecamidine, N,N-dimethylstearamidine, cyanamide, dicyandiamide, guanylurea, aminoguanidine, etc.
As indicated previously, the nitrogen-containing group in the acylated nitrogen compositions of this invention is characterized by a nitrogen atom attached directly to the relatively polar group. It will be appreciated, of course, that the linkage between a nitrogen atom and an acyl radical is representative of an amide or an imide structure, that the linkage between a nitrogen atom and an acylimidoyl radical is representative of an amidine structure, and that the linkage between a nitrogen atom and an acyloxy radical is representative of an ammonium-carboxylic acid salt structure. Thus, the acylated nitrogen compositions of this invention are characterized. by amide, imide, amidine, or salt linkages and in many instances a mixture of such linkages. Those containing two such linkages separated by a lower alkylene radical (i.e., one having less than about 6 carbon atoms), such as are derived from succinic, glutaric, or adipic radicals, are especially preferred in this invention.
A convenient method for preparing the acylated nitrogen compositions of this invention comprises reacting a high molecular weight acid-producing compoundv characterized by the presence within its structure of a high molecular weight oil-solubilizing group having at least about 50 aliphatic carbon atoms and at least one acid-producing group having the structural configuration o ax wherein X is selected from the class consisting of halogen, hydroxy, hydrocarbon-oxy, acyloxy, and amino radicals derived from ammonia or a lower primary amine such as a mono-alkylamine or mono-arylamine having no more than about 6 aliphatic carbon atoms with at least about one-half an equivalent amount of a nitrogen-containing compound characterized by the presence within its structure of at least one radical having the structural configuration The above process involves a reaction between the acidproducing group with the nitrogen-containing radical to result in the direct attachment of the nitrogen atoms to a polar radical, i.e., acyl, acylimidoyl, or acyloxy radical derived from the acid-producing group. The linkage formed between the nitrogen atom and the polar radical may thus be that representative of a salt, amide, imide, or amidine radical. In most instances, the product of the above process contains a mixture of linkages representative of such radicals. The precise relative proportions of such radicals in the product usually are not known as they depend to a large measure upon the type of the acidproducing group and the nitrogen-containing radical involved in the reaction and also upon the environment (e.g., temperature) in which the reaction is carried out. To illustrate, the reaction involving an acid or an'hydride group with an amino nitrogen-containing radical at relatively low temperatures such as below about 60 C. results predominantly in a salt linkage (i.e.,
but at relatively high temperatures such as above about C. results predominantly in an amide, imide, or amidine linkage (i.e.,
0 ll ll -C--N 0r -CN) The products obtained by the above process, irrespective of the nature or relative proportions of the linkages present therein, have been found to be effective as additives in hydrocarbon oils for the purposes of this invention.
The acid-producing compounds contemplated for use in the above process include mono-carboxylic and polycarboxylic acids, acid halides, esters, and anhydrides as well as imides and amides derived from ammonia or a lower primary amine, and also mixtures of such compounds. The imide or amide of ammonia or a lower primary amine is especially useful for preparing the acylated nitrogen compositions having more than one nitrogencontaining radicals. The nature of the oil-solubilizing group in such compounds should be the same as that which characterized the hydrocarbon substituent, described previously, in the acylated nitrogen compositions of this invention.
The substantially saturated, aliphatic hydrocarbon-substituted succinic acids and anhydrides are especially preferred for use as the acid-producing reactant in this process for reasons of the particular effectiveness of the products obtained from such compounds as additives in hydrocarbon oils. The succinic compounds are readily available from the reaction of maleic anhydride with a high molecular Weight olefin or a chlorinated hydrocarbon such as the olefin polymer described hereinabove. The reaction involves merely heating the two reactants at a temperature about 100-200 C. The product from such a reaction is an alkenyl succinic anhydride. The alkenyl group may be hydrogenated to an alkyl group. The anhydride may be hydrolyzed by treatment with Water or steam to the corresponding acid. Either the anhydride or the acid may be converted to the corresponding acid halide or ester by reaction with, e.g., phosphorus halide, phenols or alcohols or to the corresponding imide or amide by reaction with ammonia or a lower primary amine.
In lieu of the high molecular Weight olefins or chlorinated hydrocarbons, other high molecular weight hydrocarbons containing an activating polar substituent, i.e., a substituent which is capable of activating the hydrocarbon molecule in respect to reaction with maleic acid or anhydride may be used in the above-illustrated reaction for preparing the succinic compounds. Such polar substituents may be illustrated by sulfide, disulfide, nitro, mercaptan, bromine, ketone, and aldehyde radicals. Examples of such polar-substituted hydrocarbons include polypr-opene sulfide, di-polyisobutene disulfide, nitrated mineral oil, di-polyethylene sulfide, brominated polyethylene, etc. Another method useful for preparing the succinic acids and anhydrides involves the reaction of itaconic acid with a high molecular weight olefin or a polar-substituted hydrocarbon at a, temperature usually within the range from about 100 C. to about 200 C.
The polycarboxylic acids and derivatives thereof having more than two carboxylic radicals per molecule which are contemplated for use in this invention are those containing at least about 50 aliphatic carbon atoms per molecule and furthermore, at least about 25 aliphatic carbon atoms per each carboxylic radical. Such acids may be prepared by halogenating a high molecular weight hydrocarbon such as the olefin polymer described hereinabove to produce a poly-halogenated product, converting the polyhalogenated product to a poly-nitrile, and then hydrolyzing the poly-nitrile. They maybe prepared also by oxidation of a high molecular weight polyhydric alcohol with potassium permanganate, nitric acid, or a like oxidizing agent. Another method for preparing such polycarboxylic acids involves the reaction of an olefin or a polarsubstituted hydrocarbon such as a chloro-polyisobutene with an unsaturated poly-carboxylic acid such as 2- pentene-1,3,5-tricarboxylic acid obtained by dehydration of citric acid.
The mono-carboxylic acids and derivatives thereof may be obtained by oxidizing a mono-hydric alcohol with potassium permanganate or by reacting a halogenated high molecular olefin polymer with a ketene. Another convenient method for preparing the monocarboxylic acids involves the reaction of metallic sodium with an acetoacetic ester or a malonic ester of an alkanol to form a sodium derivative of the ester and the subsequent reaction of the sodium derivative with a halogenated high molecular weight hydrocarbon such as brominated wax or brominated polyisobutene. Other methods include the reaction of a high molecular weight olefin with ozone; the Haloform Reaction; the reaction of an organometallic complex (such as lithium-olefin complex) with carbon dioxide; the reaction of a chlorinated hydrocarbon with a lactone; the reaction of a chlorinated hydrocanbon with chloromaleic acid or mercapto-maleic anhydride.
The mono-carboxylic and poly-carboxylic acid anhydrides are obtained by dehydrating the corresponding acids. Dehydration is readily accomplished by heating the acid to a temperature above about 70 C. preferably in the presence of a dehydration agent, e.g., acetic anhy- 8 dride. Cyclic anhydrides are usually obtained from poly-cariboxylic acids having the acid radicals separated by no more than three carbon atoms such as substituted succinic or glutaric acids, whereas linear polymeric anhydrides are obtained from poly-carboxylic acids having the acid radicals separated by four or more carbon atoms.
The acid halides of the mono-carboxylic and polycarboxylic acids can be prepared by the reaction of the acids or their anhydrides with a halogenation agent such as phosphorus tribromide, phosphorus pentachloride, or thionyl chloride. The esters of such acids can be prepared simply by the reaction of the acids or their anhydrides With an alcohol or a phenolic compound such as methanol, ethanol, octadecanol, cyclohexanol, phenol, naphthol, octylphenol, etc. The esterification is usually promoted by the use of an alkaline catalyst such as sodium hydroxide or sodium alkoxide or an acidic catalyst such as sulfuric acid. The nature of the alcoholic or phenolic portion of the ester radical appears to have little infiuence on the utility of such ester as reactant in the process described herein-above.
The nitrogen-containing reactants useful in the above process are the compounds, described previously in this specification, from which the nitrogen-containing group the acylated nitrogen compositions of this invention can be derived.
The above process is usually carried out by heating a mixture of the acid-producing compound and the nitrogen-containing reactant at a temperature above about C., preferably within the range from about C. to about 250 C. However, when an acid or anhydride is employed in reactions with an amino nitrogen-containingreactant, the process may be carried out at a lower temperature such as room temperature to obtain products having predominantly salt linkages or mixed saltamide linkages. Such products may be converted, if desired, by heating to above 80 C. to products having predominantly amide, imide, or amidine linkages. The use of a solvent such as benzene, toluene, naphtha, mineral oil, xylene, n-hexane, or the like is often desirable in the above process to facilitate the control of the reaction temperature.
Another method for preparing the acylated nitrogen compositions of this invention involves first reacting the nitrogen-containing reactant with an olefinic acid-producing compound to form a nitrogen containing intermediate and then incorporating a large hydrocarbon substituent (i.e., having at least about 50 aliphatic carbon atoms) into the intermediate by reacting the intermediate with a high molecular weight hydrocarbon reactant, such as an olefin, a chlorinated hydrocarbon, or a polar substituted hydrocarbon illustrated previously.
The olefinic acid-producing compound useful in the process may be an acid, anhydride, acid halide, or ester and it likewise may be an imide or amide derived from ammonia or a lower primary amine such as is described previously. The acid-producing compound may be that of maleic acid, itaconic acid, acrylic acid, aconitic acid, methacrylic acid, chloromaleic acid, alpha-chloroacrylic acid, alpha-butylacrylic acid, crotonic acid, citraconic acid, mesaconic acid, or a like acid preferably having less than about 8 carbon atoms and an olefinic linkage adjacent to the acid-producing radical.
Specific examples of such olefinic acid-producing compound include maleic acid, maleic anhydride, chloromaleic anhydride, maleamic acid, acrylic acid, acrylyl chloride, acrylyl bromide, methacrylic acid, alphapropylacrylyl chloride, crotonic acid, methyl acrylate, ethyl methacrylate, dimethyl maleate, diethyl itaconate, dibutyl maleate, maleimide, maleamide, N-methyl maleamide, dimethyl maleamide, N-butyl maleamide acid, N- propyl maleimide, methyl chlo-roacrylate, dimethyl citraconate, etc. The ester groups, imide groups, and amide groups of such olefinic acid-producing compounds include those discussed previously in connection with the high molecular weight acid-producing compounds useful in preparing the acylated nitrogen compositions of the invention.
The reaction of the nitrogen-containing reactant with an olefinic acid-producing compound may be carried out at a temperature from about 25 C. to 300 C. or any temperature below the decomposition point of the reaction mixture. The reaction is sirnilar to that which characterizes the formation of acylated nitrogen compositions described previously and results in a nitrogen-containing inter-mediate. The intermediate produced by such reaction is thus characterized by the presence therein of an amide, imide or amidine linkage or a mixture of such linkages. A convenient method of incorporating a high molecular weight hydrocarbon substituent into the nitrogen-containing intermediate involves reacting the intermediate with a high molecular weight reactant olefin, chlorinated hydrocarbon such as a chlorinated olefin polymer, or a polar substituted high molecular Weight hydrocarbon at a temperature above about 100 C., preferably below about 200 C. Such high molecular Weight reactant is as described previously in connection with the preparation of the high molecular weight succinic acidproducin-g compounds of this invention.
The relative proportions of the acid-producing compounds and the nitrogen-containing reactants to be used in the above process are such that at least about one-half of a stoichiometrically equivalent amount of the nitrogencontaining reactant is used for each equivalent of the acidproducing compound used. In this regard it will be noted that the equivalent weight of the nitrogen-containing reactant is based upon the number of the nitrogen-containing radicals defined by the structural configuration Similarly the equivalent weight of the acid-producing compound is based upon the number of the acid-producing radicals defined by the structural configuration Thus, ethylene diamine has two equivalents per mole; amino guanidine has four equivalents per mole; a succinic acid or ester has two equivalents per mole, etc. The upper limit of the useful amount of the nitrogen-containing reactant appears to be about two moles for each equivalent of the acid-producing compound used. Such amount is required, for instance, in the formation of products having predominantly amidine linkages. Beyond this limit, the excess amount of the nitrogen-containing reactant appears not to take part in the reaction and thus simply remains in the product apparently Without any adverse effects. On the other hand, the lower limit of about one-half equivalent of the nitrogen-containing reactant used for each equivalent of the acid-producing compound is based upon the stoichiome'try for the formation of products having predominantly imide linkages. In most instances, the preferred amount of the nitrogencontaining reactant is approximately one equivalent for each equivalent of the acid-producing compound used.
It should be noted that the reaction of a high molecular weight substituted succinic acid-producing compound (such as acid or anhyd-ride) with an alkylene polyamine (such as ethylene diamine or polyethylene polyamine) produces an acylated nitrogen composition which contains an amide conforming to the structural formula 0 R- CH%NR2 JI-IiO-NR2 where x is at least 1, R is a hydrocarbon group having at least about 50 aliphatic carbon atoms and at least about 25 aliphatic carbon atoms for each unit of x, and NR' is selected from the class consist-ing of (A) radicals derived 10 from an alyklene polyamine by the removal of a hydrogen atom from an amino group and (B) radicals derived from an alkylene polyamine by the removal of a hydrogen atom from an amino group and characterized by the presence, on the nitrogen atom of at least one additional amino group, of a complex substituent having the formula The value of x is at least one for each mole of the hydrocarbon substituent present in the amide molecule and it may be greater than one provided that it does not exceed one per each 50 aliphatic carbon atoms present in the hydrocarbon substituent. The radical R is the residue derived from an alkylene polyamine by the removal of one amino group; it may further contain a complex substituent (illustrated above) on the nitrogen atom of at least one additional amino group, or on the nitrogen atom of each of the other amino groups of the alkylene polyamine residue. In the latter case, the amide is illustrated by one present in the acylated nitrogen composition obtained by the reaction of one mole of an alkylene polyamine with as many equivalents of the substituted succinic acid or anhydride as there are amino groups in the polyamine.
The following examples illustrate the processes useful for preparing the acylated nitrogen compounds of this invention:
Example 1 A polyisobutenyl succinic anhydride is prepared by the reaction of a chlorinated polyisobutylene with maleic anhydride at 200 C. The polyisobutenyl radical has an average molecular weight of 850 and the resulting alkenyl succinic anhydride is found to have an acid number of 113 (corresponding to an equivalent weight of 500). To a mixture of 500 grams (1 equivalent) of this polyisobutenyl succinic anhydride and 160 grams of toluene there is added at room temperature 35 grams (1 equivalent) of diethylene triamine. The addition is made portionwise throughout a period of 15 minutes, and an initial exothermic reaction caused the temperature to rise to 50 C. The mixture then is heated and a water-toluene azeotrope distilled from the mixture. When no more water would distill the mixture is heated to C. at reduced pressure to remove the toluene. The residue is diluted with 350 grams of mineral oil and this solution is found to have a nitrogen content of 1.6%. The product is an oil solution of an acylated nitrogen composition containing an amide conforming to the structural formula where R is a polyisobutene radical, x has a value of one for each mole of the polyisobutene group, and NR is a radical derived from diethylene triamine by the removal of a hydrogen atom from an amino group and characterized by the presence on the nitrogen atom of at least one remaining amino group of a radical selected from the class consisting of Example 2 The procedure of Example 1 is repeated using 31 grams (1 equivalent) of ethylene diamine as the amine reactant. The nitrogen content of the resulting product is 1.4%.
Example 3 The procedure of Example 1 is repeated using 55.5 grams (1.5 equivalents) of an ethylene amine mixture having a composition corresponding to that of triethylene tetramine. The resulting product has a nitrogen content of 1.9%. The product is an oil solution of an acylated nitrogen composition containing an amide conforming to the structural formula shown in Example 1 except that R is derived from the ethylene amine mixture.
Example 4 The procedure of Example 1 is repeated using 55.0 grams (1.5 equivalents) of triethylene tetramine as the amine reactant. The resulting product has a nitrogen content of 2.9%. The product is an oil solution of an acylated nitrogen composition containing an amide conforming to the structural formula shown in Example 1 except that R is derived from triethylene tetramine.
Example 5 To a mixture of 140 grams of toluene and 400 grams (0.78 equivalent) of a polyisobutenyl succinic anhydride (having an acid number of 109 and prepared from maleic anhydride and the chlorinated polyisobutylene of Example 1) there is added at room temperature 63.6 grams (1.55 equivalents) of an ethylene amine mixture having an average composition corresponding to that of tetraethylene pentamine and available from Carbide and Carbon under the trade name Polyamine H. The mixture is heated to distill the water-toluene azeotrope and then to 150 C. at reduced pressure to remove the remaining toluene. The residual polyamide has a nitrogen content of 4.7%. The product is an oil solution of an acylated nitrogen composition containing an amide conforming to the structural formula shown in Example 1 except that R is derived from the ethylene amine mixture.
Example 6 The procedure of Example 1 is repeated using 46 grams 1.5 equivalents) of ethylene diamine as the amine reactant. The product which resulted has a nitrogen content of 1.5%. The product is an oil solution of an acylated nitrogen composition containing an amide conforming to the structural formula shown in Example 1 except that R is derived from ethylene diamine.
Example 7 A polyisobutenyl succinic anhydride having an acid number of 105 and an equivalent weight of 540 is prepared by the reaction of a chlorinated polyisobutylene (having an average molecular weight of 1,050 and a chlorine content of 4.3%) and maleic anhydride. To a mixture of 300 parts by weight of the polyisobutenyl succinic anhydride and 160 parts by weight of mineral oil there is added at 65 95 C. an equivalent amount (25 parts by weight) of Polyamine H (identified in Example 5). This mixture then is heated to 150 C. to distill all of the water formed in the reaction. Nitrogen is bubbled through the mixture at this temperature to insure removal of the last traces of water. The residue is diluted by 79 parts by weight of mineral oil and this oil solution found to have a nitrogen content of 1.6%. The product is an oil solution of an acylated nitrogen composition containing an amide conforming to the structural formula shown in Example 1 except that R is derived from the ethylene amine mixture.
Example 8 A mixture of 2,112 grams (3.9 equivalents) of the polyisobutenyl succinic anhydride of Example 7, 136
grams (3.9 equivalents) of diethylene triamine, and 1060 grams of mineral oil is heated at l50 C. for one hour. Nitrogen is bubbled through the mixture at this temperature for four more hours to aid in the removal of water. The residue is diluted with 420 grams of mineral oil and this oil solution is found to have a nitrogen content of 1.3%. The product is an oil solution of an acylated nitrogen composition containing an amide conforming to the structural formula showin in Example 1.
Example 9 To a solution of 1,000 grams (1.87 equivalents) of the polyisobuentyl succinic anhydride of Example 7, in 500 grams of mineral oil there is added at 85-95 C. 70 grams (1.87 equivalents) of tetraethylene pentamine. The mixture then is heated at -165 C. for four hours, blowing with nitrogen to aid in the removal of Water. The residue is diluted with 200 grams of mineral oil and the oil solution found to have a nitrogen content of 1.4%. The product is an oil solution of an acylated nitrogen composition containing an amide conforming to the structural formula shown in Example 1 except that R is derived from tetraethylene pentamine.
Example 10 A polypropenyl succinic anhydride is prepared by the reaction of a chlorinated polypropylene (having a molecular weight of about 900 and a chlorine content of 4%) and maleic anhydride at 200 C.. The product has an acid number of 75. To a mixture of 390 grams (0.52 equivalent) of this polypropenyl succinic anhydride, 500 grams of toluene, and grams of mineral oil there is added portionwise 22 grams (0.52 equivalent) of Polyamine H. The reaction mixture is heated at reflux temperature for three hours and water removed from an azeotrope with toluene. The toluene then is removed by heating to 150 C./2O millimeters. The residue was found to contain 1.3% of nitrogen. The product is an oil solution of an acylated nitrogen composition containing an amide conforming to the structural formula shown in Example 1 except that R is derived from the ethylene amine mixture.
Example 11 A substituted succinic anhydride is prepared by reacting maleic anhydride with a chlorinated copolymer of isobutylene and styrene. The copolymer consists of 94 parts by weight of isobutylene units and 6 parts by weight of styrene units, has an average molecular weight of 1,200, and is chlorinated to a chlorine content of 2.8% by weight. The resulting substituted succinic anhydride has an acid number of 40. To 710 grams (0.51 equivalent) of this substituted succinic anhydride and 500 grams of toluene there is added portion wise 22 grams (0.51 equivalent) of Polyamine H. The mixture is heated at reflux temperature for three hours to remove by azeot-ropic distillation all of the water formed in the reaction, and then at 150 C./20 millimeters to remove the toluene. The residue contains 1.1% by weight of nitrogen. The product is an oil solution of an acylated nitrogen composition containing an amide conforming to the structural formula shown in Example 1.
Example 12 A substituted succinic anhydride is prepared by reacting maleic anhydride with a chlorinated copolymer of isobutylene and isoprene. The copolymer consists of 99 parts by weight of isobutylene units and 1% by weight of isoprene units. The molecular weight of the copolymer is 28,000 and the chlorine content of the chlorinated copolymer is 1.95%. The resulting alkenyl succinic anhydride had an acid number of 54. To a mixture of 228 grams (0.22 equivalent) of an oil solution of this alkenyl succinic anhydride, 58 grams of additional mineral oil, 500 grams of toluene and 9.3 grams (0.22 equivalent) of Example 13 A polyisobutenyl succinic anhydride is prepared by the reaction of a chlorinated polyisobutylene with maleic anhydride. The chlorinated polyisobutylene has a chlorine content of 2% and an average molecular weight of 11,000. The polyisobutenyl succinic anhydride has an acid number of 48. A mixture of 410 grams (0.35 equivalent) of this anhydride, 15 grams (0.35 equivalent) of Polyamine H and 500 grams of toluene is heated at reflux temperature for four hours to remove water from an azeotrope with toluene. The toluene then is removed by heating to 150 C./20 millimeters. The nitrogen content of the residue is 1.3%. The product is an oil solution of an acylated nitrogen composition containing an amine conforming to the structural formula shown in Example 1.
Example 14 The procedure of Example is repeated except that 0.94 equivalent of Polyamine H is used instead of 1.55 equivalents. The nitrogen content of the product is 3%. The product is an oil solution of an acylated nitrogen composition containing an amide conforming to the structural formula shown in Example 1.
Example 15 A polyisobutenylsubstituted succinic acid is prepared by hydrolysis of the corresponding anhydride (prepared in turn by the condensation of a chlorinated polyisobutylene and maleic anhydride). To 1152 grams (1.5 equivalents) of a 70% mineral oil solution of this polyisobutylenyl succinic acid having an acid number of 62 there is added at room temperature 59.5 grams (1.5 equivalents) of Polyamine H. This mixture is heated at 150- 167 C. for 7 hours during which time a total of 19.5 grams of Water is distilled from the mixture. The residue is diluted with 174 grams of mineral oil and then filtered at 150 C. The filtrate has a nitrogen content of 1.6%. The product is an oil solution of an acylated nitrogen composition containing an amide conforming to the structural formula shown in Example 1.
Example 16 A mixture of 1056 grams (2.0 equivalents) of the polyisobutenyl succinic anhydride of the preceding example (in which the polyisobutenyl group has a molecular weight of 850), 89 grams (2.0 equivalents) of di-(l,2-propylene) triamine (having a nitrogen content of 31.3%), 370 grams of mineral oil and 100 grams of toluene is heated at reflux temperature (180-190= C.) for 5 hours. A total of 18 grams of water is collected from the water-toluene azeotrope. The residue is heated to 150 C./20 mm. to remove any last traces of water which might have remained. The nitrogen analysis of this residue is 1.9%. The product is an oil solution of an acylated nitrogen composition containing an amide conforming to the structural formula shown in Example 1 except that R is derived from di-( 1,2-propylene triamine.
Example 17 A polyisobutylene having an average molecular weight of 50,000 is chlorinated to a chlorine content of by Weight. This chlorinated polyisobutylene is reacted with maleic anhydride to produce the corresponding polyisobutenyl succinic anhydride having an acid number of 24. To 6,000 grams (2.55 equivalents) of this anhydride there is added portionwise at 70-105 C. 108
grams (2.55 equivalents) of :Polyamine H over a period of 45 minutes. The resulting mixture is heated for four hours at 1'601'80 C. While nitrogen is bubbled throughout to remove water. When all of the Water has been removed the product is (filtered and the filtrate found to have a nitrogen content of 0.6%. The product is an oil solution of an acylated nitrogen composition containing an amide conforming to the structural formula shown in Example 1 except that R is derived from the ethylene amine mixture.
Example 18 A mixture of 1 equivalent of a polyisobutene-substituted succinic anhydride having an acid number of 98 (prepared according to the procedure described in Example 1) and 1 equivalent of an acrolein-ammonia (molar ratio of 1: 1) interpolymer having a nitrogen content of 23% by Weight is diluted with 40% by its Weight of a mineral oil. The resulting mixture is heated to 155 C. and nitrogen is bubbled through the mixture at this temperature for 5 hours. The residue is found to have a nitrogen content of 1.35%.
Example 19 A cyanoethyl-substituted ethylene amine is prepared by mixing 21-2 grams of acrylonitrile with 216 grams of an ethylene amine mixture consisting of 75% by weight of triethylene tetramine and 25% by weight of diethylene triamine at room temperature and heating the mixture at l'l-0130 C. for 5 hours and then to C./mm. To a mixture of 111110 grams of the polyisobutene-substituted succinic anhydride of Example 1 and 825 grams of mineral oil there is added at 60 C. 143 grams dropwise of the above cyanoethyl-substituted ethylene amine (having a nitrogen content of 31.8%), The mixture is heated at C. C. for 5 hours while being purged with nitrogen. A total of 6 cc. of water is removed by distillation. The residue has a nitrogen content of 1.6 6%.
Example 20 To a mixture of 430 grams of the polyisobutenesubstituted succinic anhydride of Example 1 and 355 grams of mineral oil there is added at 60-80 C. 108 grams of N-aminopropyl morpholine throughout a period of 1 hour. The mixture is heated at 150-155 C. for 5 'hours until no more Water distills. The residue is found to have a nitrogen content of 2.3%.
Example 21 To a mixture of 1000 grams of the polyisobutenesubstituted succinic anhydride of Example 1 and 500 grams of mineral oil there is introduced at 150 1 60 C. beneath its surface a sufficient quantity of ammonia for formation of an imide within a period of 1 hour. The mixture is diluted with 169 grams of mineral oil, heated to 150 C. and filtered. The filtrate is found to have a nitrogen content of 0.77%.
Example 23 A mixture of 286 grams of polyisobutene-substituted succinic anhydride of Example 1, 96 grams of N, N-di- 'butyl ethylene-diamine and 252 grams of mineral oil is prepared at 60 C. and heated at 150-165 C. for 5 hours while being purged with nitrogen. The residue is found to have a nitrogen content of 2.24%.
15 Example 24 -A mixture of 417 grams of polyisobutene-substituted succinic anhydride of Example 1, 30 grams of N-(2- aminoethyl) trimethylene diamine and 293 grams of mineral oil is prepared at 6080 C. and then heated at 150155 C. -for hours while being purged with nitrogen. The residue is found to have a nitrogen content of 1.51%.
Example 25 A mixture of 430 grams of the polyisobutene-substituted succinic anhydride of Example 1, 64 grams of 1,l-(dimethylaminoethyl)-4-methyl-piperazine and 324 grams of mineral oil is prepared at 60 C. and then heated at 150-155 C. while being blown with nitrogen. The residue is found to have a nitrogen content of 1.81%.
Example 26 A mixture of 416 grams of polyisobutene-substituted succinic anhydride of Example 1, 124 grams of N-phenyl piperazine and 356 grams of mineral oil is prepared at 60 C. and then heated at l50-155 C. for 5 hours while being purged with nitrogen. No water is removed by such heating. The residue is found to have a nitrogen content of 2.07%.
Example 27 A mixture of 1110 grams of polyisobutene-substituted succinic anhydride of Example 1, 105 grams of anthranilic acid and 844 grams of mineral oil is heated at 100 C. for 2 hours. The mixture is cooled and is mixed with 72 grams of a mixture consisting of 75% by weight of triethylene tetramine and 25% by weight of diethylenetriamine at 6080 C. The resulting mixture is heated at 150-155 C. for 5 hours while being purged with nitrogen. The residue is found to have a nitrogen content of 1.72%.
Example 28 A diisobutenyl-substituted ethylene amine is prepared by reacting 590 grams of diisobutenyl chloride and 264 grams of a mixture consisting of 75 by weight of triethylene tetramine and 20% by weight of diethylene triamine in the presence of 264 grams of potassium hydroxide (85% purity) and 2200 grams of isopropyl alcohol at 85-90 C. A mixture of 528 grams of polyisobutene-substituted succinic anhydride of Example 1, 101 grams of the above diisobutenyl-substituted ethylene amine and 411 grams of mineral oil is heated at 150- 160 C. while being purged with nitrogen until no more water distills. The residue has a nitrogen content of 1.98%.
Example 29 A mixture of 45 grams of di-(polypropoxy)cocoamine having a molecular weight of 2265, 22 grams of polyisobutene-substituted succinic anhydride of Example 1 and 44 grams of mineral oil is heated at 150155 C. for 7 hours. The residue is found to have a nitrogen content of 0.25%.
Example 30 A mixture of 1000 grams of the polyisobutene-substituted succinic anhydride of Example 1, 159 grams of menthane diamine and 500 grams of mineral oil is prepared at 70100 C.- and heated at 150-190 C. while being blown with nitrogen until no water distills. The residue is diluted with 258 grams of mineral oil and the solution is found to have a nitrogen content of 1.32%.
Example 31 A polypropylene-substituted succinic anhydride having an acid number of 84 is prepared by the reaction of a chlorinated polypropylene having a chlorine content of 3% and molecular weight of 1200 with maleic anhydride. A mixture of 813 grams of the polypropylene-substi- 16 tuted succinic anhydride, 50 grams of a commercial ethylene amine mixture having an average composition corresponding to that of tetraethylene pentamine and 566 grams of mineral oil is heated at 150 C. for 5 hours. The residue is found to have a nitrogen content of 1.18%.
Example 32 A mixture of 206 grams of N,N'-disecondary-butyl p-phenylene diamine, 1000 grams of the polyisobutenesubstituted succinic anhydride of Example 1 and 500 grams of mineral oil is prepared at C. and heated at 150200 C. for 9.5 hours. The mixture is diluted with 290 grams of mineral oil, heated to 160 C. and filtered. The filtrate is found to have a nitrogen content of 1.29%.
Example 33 To 1000 grams of the polyisobutene-substituted succinic anhydride of Example 1 and 500 grams of mineral oil there is added 17.6 grams of hydrazine at 70-80 C. The reaction is exothermic. The mixture is heated at 140150 C. for 1 hour whereupon 9 grams of water is collected as the distillate. To the residue there is then added 40 grams of an ethylene amine mixture having an average composition corresponding to that of tetraethylene pentamine at 70-80 C. The mixture i then heated at 150160 C. while being purged with nitrogen until no more water is removed by distillation. The residue is diluted with 200 grams of mineral oil, heated to 160 C. and filtered. The filtrate has a nitrogen content of 1.16%.
Example 34 T o a solution of 1000 grams of the polyisobutene-substituted snccinic anhydride of Example 1 in 500 grams of mineral oil there is added 28 grams of 1,1-dimethyl hydrazine at 5060 C. The mixture is heated at 60- C. for 3 hours and then mixed with 40 grams of an ethylene amine mixture having an average composition corresponding to that of tetraethylene pentamine at 85- 95C. The mixture is then heated at 150-185 C. for 6 hours whereupon 14 grams of water is collected as the distillate. The residue is diluted with 197 grams of mineral oil, heated to 160 C. and filtered. The filtrate has a nitrogen content of 1.53%.
Example 35 A mixture of 1000 grams of the polyisobutene-substituted succinic anhydride of Example 1, 333 grams of 1,2-di(3-aminopropoxy) ethane and 500 grams of mineral oil is heated at 170 C. for 5 hours whereupon 18 grams of Water is collected as the distillate. The residue is diluted with 380 grams of mineral oil, heated to 160 C. and filtered. The filtrate has a nitrogen content of 2.3%.
Example 36 A mixture of 1000 grams of the polyisobutene-substituted succinic anhydride of Example 1, 418 grams of di- (3-aminopropoxy ethyl) ether and 500 grams of mineral oil is heated at 170 C. for 4 hours. A total of 17 grams of water is collected as the distillate. The residue is diluted with 433 grams of mineral oil heated to 160 C. and filtered. The filtrate has the nitrogen content of 2.18%.
Example 37 A mixture of 1000 grams of the polyisobutene-substituted succinic anhydride of Example 1 and 361 grams of a technical tertiary-alkyl primary amine wherein the tertiary-alkyl radical contains 12-14 carbon atoms and 500 grams of mineral oil is heated at 250 C. for 13 hours while being purged with nitrogen. The residue is then heated to 150 C./1 mm., diluted with 337 grams of mineral oil, heated to C. and filtered. The filtrate has a nitrogen content of 0.87%.
1 7 Example 38 A mixture of 1000 grams of the polyisobutene-substituted succinic anhydride of Example 1, 254 grams of aminoguanidine bicarbonate and 500 grams of mineral oil is prepared at 80 C. and heated at 130-165 C. for hours. The residue is mixed with 223 grams of mineral oil, heated to 150 C., and filtered. The filtrate has the nitrogen content of 3.38%.
Example 39 A mixture of 1000 grams of the polyisobutene-substituted succinic anhydride of Example 1, 178 grams of Z-amino-pyridine and 500 grams of mineral oil is heated at 140175 C. for 10 hours while being purged with nitrogen. A total of 16 grams of water is collected as the distillate. The residue is diluted with 273 grams of mineral oil and filtered. The filtrate ha a nitrogen content of 2.55%.
Example 40 A mixture of 1000 grams of the polyisobutene-substituted succinic anhydride of Example 1, 103 grams of 2,6-diamino-pyridine and 500 grams of mineral oil is heated at 140-180 C. for 11 hours while being purged with nitrogen. A total of 16 grams of Water is collected as the distillate. The residue is diluted with 223 grams of mineral oil, heated to 150 C. and filtered. The filtrate has a nitrogen content of 2.15%.
Example 41 A mixture of 1000 grams of polyisobutene-substituted succinic anhydride of Example 1, 159 grams of cyanoguanidine and 233 grams of toluene is heated at the reflux temperature of 14 hours while 7.15 grams of water is removed by azeotropic distillation. The mixture is diluted With 740 grams of mineral oil and toluene is then removed by heating the mixture to 150 C. The residue is filtered and the filtrate has the nitrogen content of 4.74%.
Example 42 A mixture of 1632 grams of polyisobutene-substituted succinic anhydride of Example 1, 207 grams of a condensation product of acrolein with ammonia (molar ratio of 1:1) having a nitrogen content of 20%, 604 grams of mineral oil and 1750 grams of toluene is heated at the reflux temperature for 3 hours. A total of 31 grams of water is removed as the distillate. Toluene is then removed by heating the mixture to 150 C./ 20 mm. The residue is found to have a nitrogen content of 1.89%.
Example 43 I A nitrogen-containing compound is prepared by mixing 100 grams of cyanoguanidine with 500 grams of ethylene amine mixture having an average composition corresponding to that of tetraethylene pentamine and heating the mixture at 70-80 C. for 3 hours to obtain a homogeneous mass and filtering the mass. A mixture of 1000 grams of the polyisobutene-substituted succinic anhydride of Example 1, 96 grams of the above filtrate and 164 grams of toluene is heated at the reflux temperature for 10 hours. The toluene is then removed by heating the mixture to 150 C./2O mm. The residue is diluted with 400 grams of mineral oil and filtered. The filtrate has a nitrogen content of 3.43%.
Example 44 To a mixture of 544 .grams of the polyisobutene-substituted succinic anhydride of Example 1, 283 grams of mineral oil and 281 grams of toluene there is added 30 grams of urea at 45 C. The resulting mixture is heated at 130-135 C. for 11 hours whereupon 2.5 cc. of Water is removed as the distillate. The residue is then heated to 140 C./20 mm. and filtered. The filtrate has a nitrogen content of 1%.
18 Example 45 A mixture of 1088 grams of the polyisobutene-substituted succinic anhydride of Example 1, 106 grams of dipropylene triamine, 500 grams of toluene is heated at the reflux temperature for 4 hours until no more Water distills. The residue is then heated to C./20 mm. and diluted with 392 grams of mineral oil. The oil solution is found to have a nitrogen content of 1.74%.
Example 46 A mixture of 1000 grams of the polyisobutene-substituted succinic anhydride of Example 1, 174 grams of phenylbiguanide and 270 grams of toluene is heated at the reflux temperature for 6.5 hours whereupon 25 grams of water is removed by distillation. The residue is diluted With 500 grams of mineral oil and heated to C./2O mm. to distill ofi toluene. The residue is diluted further with 265 grams of mineral oil, heated to 150 C. and filtered. The filtrate has a nitrogen content of 3.4%.
Example 47 A mixture of 920 grams of the polyisobutene-substituted succinic anhydride of Example 1, and 249 grams of bis-(dimethylaminopropyl) amine is heated at reflux temperature until no more water distills. The residue has a nitrogen content of 4%.
Example 48 A mixture of 1000 grams of the polyisobutene-substituted succinic anhydride of Example 1, 363 grams of aminopropyl octadecylamine and 1314 grams of mineral oil is heated at 200 C. for 24 hours. The residue is filtered. The filtrate has a nitrogen content of 1.02%.
Example 49 A mixture of 1000 grams of the polyisobutene-substituted succinic anhydride of Example 1, and 258 grams of di-n-butylamine is heated at C. for 12 hours and then to 200 C./ 25 mm. The residue is diluted with 1157 grams of mineral oil and filtered. The filtrate has a nitrogen content of 0.8%.
Example 50 A mixture of 297 grams of the polyisobutene-substituted succinic anhydride of Example 1, 25 grams of melamine and 200 grams of mineral oil is heated at -260 C. for 9 hours and then at 290295 C. for 7 more hours. The residue is mixed with 50 grams of water, heated at reflux for 7 hours, dried and filtered. The filtrate has a nitrogen content of 2%.
Example 51 A mixture of 100 grams of the polyisobutene-substituted anhydride of Example 1 and 67 grams of mineral oil is heated to 50 C. To this mixture there is added 59 grams of an 85% aqueous solution of hydrazine hydrate. The mixture is heated at 100110 C. for 1.25 hours, diluted with toluene, and heated at 107 C. until no more water distills. Toluene is removed by distillation. The residue has a nitrogen content of 0.8%.
Example 52 A mixture of 1.0 equivalent of a mono-carboxylic acid (prepared by chlorinating a polyisobutene having a molecular weight of 750 to a product having a chlorine content of 3.6% by weight, converting the product to the corresponding nitrile by reaction with an equivalent amount of potassium cyanide in the presence of a catalytic amount of cuprous cyanide and hydrolyzing the resulting nitrile by treatment with 50% excess of a dilute aqueous sulfuric acid at the reflux temperautre) and 0.5 equivalent of ethylene diamine is mixed with twice its volume of xylene. The resulting mixture is heated at the reflux temperature until no more water is removed by distillation. The mixture is heated further and the xylene is 19 removed by distillation under reduced pressure. residue is the acylated nitrogen compound.
Example 53 A methyl ester of a high molecular weight mono-carboxylic acid is prepared by heating an equi-molar mixture of a chlorinated polyisobutene having a molecular weight of 1000 and a chlorine content of 4.7% by weight and methyl methacrylate at l40220 C. The resulting ester is then heated with a stoichiometrically equivalent amount of triethylene tetramine at 100200 C. to produce an acylated nitrogen compound of this invention.
Example 54 A dimethyl wax-substituted malonate is prepared by reacting dimethyl malonate with sodium ethoxide to form a sodium derivative of the ester, heating the sodium derivative with a brominated wax having 75 carbon atoms and 1 bromine atom per molecule. A mixture of 1.0 equivalent of the ester of 1.0 equivalent of N,N-dibuty1 thiourea is dissolved in five times its volume of xylene. The resulting mixture is heated at the reflux temperature until no more water is removed by azeotropic distillation. The mixture is heated further and the xylene is removed by distillation. The residue is the acylated nitrogen compound.
The
Example 55 A high molecular weight mono-carboxylic acid is prepared by telomerizing ethylene with carbon tetrachloride to a telomer having an average of 35 ethylene radicals per molecule and hydrolyzing the telomer to the corresponding acid in accordance with the procedure described in British Patent No. 581,899. A mixture of 1.5 equivalent of the acid and 0.75 equivalent of amino-propy-l octylamine is mixed with twice its volume of a mineral oil and twice its volume of xylene. The resulting mixture is heated at the reflux temperature until no more water is removed by azeotropic distillation. Xylene is then removed by distillation under reduced pressure and the residue is filtered.
Example 56 A mixture of 2000 grams of mineral oil, 3 equivalents of trimethylene diamine and 3 equivalents of a high molecular weight tricarboxylic acid prepared by the reaction of a brominated poly (l-hexene) having a molecular weight of 2000 and a bromine content of 4% by weight of 2-pentene-1,3,5-tricarboxylic acid (prepared by dehydration of citric acid) is heated at 150 C. for 20 hours. The residue is filtered to give a homogeneous mineral oil solution of the acylated nitrogen product.
Example 57 An equi-molar mixture of 2-aminoethyl morpholine and a mono-carboxylic acid (prepared by the reaction of ketene with a brominated poly(1-octene) having a molecular weight of 1500 and one atom of bromine per molecule) is diluted with three times its volume of xylene. The resulting mixture is heated at the reflux temperature until no more water is removed by distillation. The residue is an xylene solution of the :acylated nitrogen compound.
Example 58 A mixture of 1 equivalent of methane diamine and 1 equivalent of a high molecular glutaric acid-ester (prepared by the reaction of silver with an equi-molar mixture of beta-iodopropanoic acid and alpha-iodo derivative of the methyl ester of the mono-carboxylic acid of the preceding example) is diluted with an equal weight of a mineral oil and the resulting solution is heated at 180 C. until no more water distills. The residue is then filtered.
Example 59 An equi-molar mixture of a technical ethylene amine mixture having an average composition corresponding to A high molecular weight dicarboxylic acid is prepared by reacting two moles of the Omega-brorno derivative of the hexapentacontanoic acid of the preceding example with one mole of zinc. The dicarboxylic acid is then treated with 2 equivalents of ethylene diamine to produce a diamide.
Example 61 A mixture of 1 equivalent of 1-aminoethyl-2-octadecylimidazoline with 1 equivalent of the high molecular weight monocarboxylic acid of Example is mixed with twice its volume of diphenyl oxide. The resulting mixture is heated at the reflux temperature until no more water distills. The residue is then filtered.
Example 62 A product is obtained by the procedure described in the preceding example except that N,N'-di-n-butyl-p-phenylenediamine (1 equivalent) is used in lieu of the imidazoline used.
Example 63 To a solution of 1 equivalent of di-methyl ester of a polyethylene (molecular weight of 1500)-substituted malonic acid in 5000 grams of xylene, there is added 1 mole of melamine at C. The resulting mixture is heated at the reflux temperature for 25 hours. The residue is mixed with 2000 grams of mineral oil and xylene is removed by heating the oil solution to 180 C./2 mm.
Example 64 A product is obtained by the procedure of Example 1, except that pyrrolidine (1 equivalent) is used in lieu of the diethylene triamine used.
Example 65 A product is obtained by the procedure of Example 1, except that hexahydro-1,3,5-triazine (1 equivalent) is used in lieu of the diethylene triamine used.
Example 66 A product is obtained by the procedure of Example 1, except that 1,3,4-dithiazolidine (1 equivalent) is used in lieu of the ethylene diamine used.
Example 67 A product is obtained by the procedure of Example 1, except that hexamethylene tetramine (2 equivalents) is used in lieu of the ethylene diamine used.
Example 68 A product is obtained by the procedure of Example 1, except that tripentylene tetramine (3 equivalents) is used in lieu of the ethylene diamine used.
Example 69 An equi-molar mixture of the polyisobutene-substituted succinic anhydride of Example 1 and N-octyl thiourea is diluted with an equal volume of xylene. The resulting mixture is heated at the reflux temperature for 30 hours. The residue is a xylene solution of the product.
Example 70 A product is obtained by the procedure of Example 69 except that oleylamide is used in lieu of the thiourea used.
21 Example 71 A product is obtained by the procedure of Example 69 except that 1,3-diphenyl guanidine is used in lieu of the thiourea used.
Example 72 A product is obtained by the procedure of Example 69 except that octadecamidine is used in lieu of the thiourea used.
Example 73 A product is obtained by the procedure of Example 69 except that guanylurea is used in lieu of the thiourea used.
Example 74 To a mixture of 396 grams of the polyisobutene-substituted succinic anhydride of Example 1 and 282 grams of mineral oil there was added 34 grams of N-methyltrimethylene diamine at 60 C. Within a period of one hour. The mixture was blown with nitrogen at 150- 155 C. for hours. The residue was found to have a nitrogen content of 1.41%.
Example 75 A mixture of 308 grams of mineral oil, 400 grams of the polyisobutene-substituted succinic anhydride of Example 1, and 70 grams of N-(2-ethylhexyl)-trimethylene diamine was prepared at 60 C. The mixture was heated to 250 C. and was then blown with nitrogen at 150- 155 C. for 5 hours. The residue had a nitrogen content of 1.4%.
Example 76 A mixture of 386 grams of mineral oil, 528 grams of the polyisobutene-suostituted succinic anhydride of Example 1, and 59 grams of N-(2-hydroxyethyl)-trimethylenediamine was prepared at 60 C. The mixture was blown with nitrogen at 150-155 C. for 5 hours. The residue had a nitrogen content of 1.56%.
Example 77 A mixture of 185 grams of mineral oil, 330 grams of the polyisobutene-substituted succinic anhydride of Example 1, and 88.5 grams of 1,4-bis(2-hydroxypropyl)-2- methyl piperazine was prepared at 60 C. The mixture was heated at 180-276 C./40 mm. for 14.5 hours. The residue had a nitrogen content of 1.12%.
Example 78 To a mixture of 314 grams of mineral oil and 430 grams of of the polyisobutene-substituted succinic anhydride of Example 1 there was added at 60 C., 49 grams of 1-(2-hydroxyethyl)piperazine. The mixture was heated to 150 C. and blown with nitrogen at this temperature for 5 hours. The residue had a nitrogen content of 1.38%.
Example 79 A mixture of 382 grams of mineral oil, 528 grams of polyisobutene-substituted succinic anhydride of Example 1, and 53 grams of 1-methyl-4-(3-aminopropyl)piperazine was prepared at 60 C., heated to 150 C., and blown with nitrogen at 150155 C. for 5 hours. The residue had a nitrogen content of 1.57%.
Example 80 To a mixture of 800 grams of the polyisobutene-substituted succinic anhydride of Example 1 and 175 grams of toluene there was added 77 grams of a commercial mixture of alkylene amines and hydroxy alkyl-substituted alkylene amines consisting of approximately 2% (by weight) of diethylene triamine, 36% of 1-(2-aminoethyl)piperazine, 11% of 1-(Z-hydroxyethyl)piperazine, 11% of NlZ-hydroxyethyl)ethylenediamine, and 40% of higher homologues obtained as a result of condensation of the above-indicated amine components. The result- 22 ing mixture Was heated at the reflux temperature for 16.5 hours whereupon 12 cc. of water was collected as the distillate. The residue was then heated to 160 C./25 mm. and diluted with 570 grams of mineral oil. The final product was found to have a nitrogen content of 1.57%.
Example 81 A product is obtained by the procedure of Example 69 except that an equimolar mixture of ammonia and bis(2-hydroxyethyl)amine is used in lieu of the thiourea used.
Example 82 A product is obtained by the procedure of Example 69 except that an equimolar mixture of benzidine is is used in lieu of the thiourea used.
Example 83 An alkenyl succinic anhydride in which the alkenyl group has less than 50 carbon atoms is prepared from a polyisobutylene having an average molecular weight of 375. This polymer is chlorinated to a chlorine content of 9.7% and then reacted with maleic anhydride. The resulting polyisobutenyl succinic anhydride has an acid number of 190 and an equivalent weight of 300. The procedure of Example 1 is followed using 1.0 equivalent of this polyisobutenyl succinic anhydride and 1.0 equivalent of Polyamine H. The resulting product then is diluted with mineral oil to a 58% solution therein; the nitrogen content is 3.2%
Example 84 Another alkenyl succinic anhydride in which the alkenyl group has less than 50 carbons is prepared by alkylation of maleic anhydride with tetra-propylene. Equivalent amounts of this tetrapropenyl succinic anhydride and triethylene tetramine in toluene are heated at reflux temperature until substantially all of the water is removed. The toluene then is removed by heating at 155 C. under reduced pressure and the residue is dissolved in mineral oil to a 60% solution. This oil solution is found to have a nitrogen content of 4.8%.
Example 85 A polyisobutene having an average molecular weight of 520 corresponding to 37 carbon atoms) is chlorinated to a chlorine content of 6.25% and then is made to react with an equivalent amount of maleic anhydride to yield a polyisobutene-substituted succinic anhydride having a saponification of 152. To 552 grams (1.5 equivalents) of this anhydride dissolved in 276 grams of mineral oil there is added at 60 C. 63 grams (1.5 equivalents) of Polyamine H portionwise over a period of 1 hour. The resulting mixture is heated for 6 hours at 150 C. and then blown with nitrogen at this temperature for 1 hour. The residue is diluted with grams of mineral oil and the final oil solution is found to have a nitrogen content of 2.1%.
Example 86 A mixture of 1 equivalent of maleimide (i.e.,
and 1 equivalent of a chlorinated polyisobutene having a chlorine content of 4.34% and a molecular weight of 350 is heated to C. in 2 hours and then blown with nitrogen at 150-204 C., cooled, diluted with benzene, mixed with a filter aid and filtered. The filtrate is heated to C./30 mm. to remove volatile materials. The residue is a polyisobutene-substituted succinimide having a nitrogen content of 1.44%. A mixture of this substituted succinimide (58.3 grams, 0.06 equivalent of nitrogen), tetraethylene pentamine (9.9 grams, 0.24 equivalent of nitrogen), and mineral oil (44.8 grams) is heated at 150-455 C. for 2.75 hours, cooled to room tem- 23 perature, diluted with benzene (500 grams), mixed with a filter aid and filtered. The filtrate is heated at 135 C./40 mm. to remove volatile materials. The residue is an oil solution of the desired acylated tetraethylene pentamine and has a nitrogen content of 2.94%.
Example 87 A mixture of 1 equivalent of N-butyl maleimide and 1 equivalent of a chlorinated polyisobutene having a chlorine content of 4.33% and a molecular wieght of 850 is heated at 100 C".210 C. in nitrogen atmosphere and then heated at l03114 C./12l mm. The reaction mixture is then filtered and the filtrate is an N-butyl polyisobutene substituted succinimide having a nitrogen content of 1.23%. A mixture of this substituted N-butyl succinimide (177 grams, 0.156 equivalent of nitrogen) and tetraethylene pentamine (12.8 grams, 0.311 equivalent of nitrogen) is diluted with mineral oil (86 grams) and heated at 150158 C. in nitrogen atmosphere. The reaction mixture is diluted with mineral oil (41 grams) and filtered. The filtrate is blown with nitrogen at 190204 C. for 5 hours, heated at 140/1 mm. and again blown with nitrogen at 24025S C. for 5.9 hours. The mixture is filtered. The filtrate is an oil solution of an acylated polyamine and has a nitrogen content of 1.13
Example 88 A mixture of 1 equivalent of maleic anhydride and 2 equivalents of tetraethylene pentamine is heated at a temperature of 100-180 C. to form an intermediate product. The intermediate product is then mixed with 1 equivalent of a chlorinated polyisobutene having a chlorine content of 4% and a molecular weight of 1500 at 150-2l0 C. The product is diluted with equal Weight of mineral oil and filtered. The filtrate is an oil solution of the acylated polyamine.
Example 89 The procedure of Example 88 is repeated except the chlorinated polyisobutene is replaced on a weight basis with a polyisobutene having a molecular weight of 2000.
Example 90 A polyisobutene having a molecular weight of 1000 (1000 grams) and maleic anhydride (100 grams), is heated at 150220 C. to form a polyisobutene-substituted maleic anhydride. The anhydride is then mixed with tetraethylene pentamine (1.5 equivalents per equivalent of anhydride) and the mixture is heated at 18020'0 C. to form an acylated polyamine.
Example 91 An acid producing compound is prepared by heating chloromaleic anhydride (1 equivalent) and 1 equivalent of a chlorinated polyisobutene having a chlorine content of 4% and a molecular weight of 2500 at 150200 C. The product of the reaction is then mixed with tetraethylene pentamine (2.5 equivalents) at 50 C. and the mixture is heated at 180-210 C. to form an acylated polyamine.
Example 92 A substituted monocarboxylic acid producing compound is obtained by reacting acrylic acid (1 equivalent) with a chlorinated polyisobutene (1 equivalent) having a chlorine content of 4.5% and a. molecular weight of 850 at 150200 C. The product of the reaction is then mixed with 1.25 equivalents of pentaethylene hexamine at 5075 C. and the resulting mixture is heated at 180-200 C. to form an acylated polyamine.
Example 93 The procedure of Example 92 is repeated except that the acrylic acid is replaced on a chemically equivalent basis with alpha-chloroacrylic acid and the pentaethylene hexamine is replaced on a nitrogen basis with ethylene diamine.
Example 94 The procedure of Example 91 is repeated except that the acid-producing compound used is one which is obtained by the reaction (Haloform reaction) of methyl heptapentacontanyl ketone with iodine, sodium hydroxide, and acidification of the haloform product.
Example 95 The procedure of Example 91 is repeated except that the acid-producing compound used is one which is obtained by the reaction of equivalent amounts of the chlorinated polyisobutene with methyl ester of N-butyl maleamic acid.
Example 96 The polyisobutene-substituted succinimide is obtained by reacting the polyisobutene-substituted succinic anhydride of Example 1 with ammonia (0.5 equivalent per equivalent of the anhydride). A mixture of the succinimide (1 equivalent of nitrogen) and tetraethylene penta mine (1 equivalent of nitrogen) is diluted with an equal weight of mineral oil and heated at 180 -250 C. to effect trans-amidation. The product is an acylated tetraethylene pentamine.
Example 97 The procedure of Example 96 is repeated except that the succinimide is N-methyl polyisobutene-substituted succinimide obtained by reacting the corresponding polyisobutene-substituted succinic anhydride with methylamine (0.5 equivalent per equivalent of the anhydride).
Example 98 The procedure of Example 96 is repeated except that the succinimide is N phenyl polyisobutene-substituted succinimide obtained by reacting the corresponding polyisobutene-substituted succinic anhydride with aniline (0.5 equivalent per equivalent of the anhydride).
Example 99 A polyisobutene-substituted succinamide is obtained by reacting 1 equivalent of the polyisobutene-substituted succinic anhydride of Example 1 with 1 equivalent of dimethylamine. The succinamide so obtained is then reacted with 2 equivalents of pentaethylene hexamine at 160-210 C. to effect trans-amidation and form an acylated polyamine.
Example 100 The procedure of Example 88 is repeated except that maleic anhydride used is replaced with itaconic acid on a stoichiometrically equivalent basis.
As indicated previously the acylated nitrogen-containing composition is usually present in lubricating oils in amounts ranging from about 0.1% to about 10% by weight. The optimum amounts for a particular application depend to a large measure upon the type of surface to which the lubricating composition is to be subjected. Thus, for example, lubricating compositions for use in gasoline internal combustion engines may contain from about 0.5 to about 5% of an acylated nitrogen-containing composition, whereas lubricating compositions for use in gears and diesel engines may contain as much as 10% or even more of the additive.
This invention contemplates also the presence of other additives in the lubricating compositions. Such additives include, for example, detergents of the ash-containing type, viscosity index improving agents, pour point depressing agents, anti-foam agents, extreme pressure agents, rust-inhibiting agents, and oxidation and corrosion inhibiting agents.
The ash-containing detergents are exemplified by oilsoluble neutral and basic salts of alkali or alkaline earth metals with sulf-onic acids, carboxylic acids, or organic phosphorus acids characterized by at least one direct carbon-to-phosphorus linkage such as those prepared by the treatment of an olefin polymer (e.g., polyisobutene having a molecular weight of 1000) with a phosphorizing agent such as phosphorus trichloride, phosphorus heptasulfide, phosphorus pentasulfide, phosphorus trichloride and sulfur, white phosphorus and a sulfur halide, or phosphorothioic chloride. The most commonly used salts of such acids are those of sodium, potassium, lithium, calcium, magnesium, strontium, and barium.
The term basic salt is used to designate the metal salts wherein the metal is present in stoichiometrically larger amounts than the organic acid radical. The commonly employed methods for preparing the basic salts involves heating a mineral oil solution of an acid with a stoichiometric excess of a metal neutralizing agent such as the metal oxide, hydroxide, carbonate, bicarbonate, or sulfide at a temperature above 50 C. and filtering the resulting mass. The use of a promoter in the neutralization step to aid the incorporation of a large excess of metal likewise is known. Examples of compounds useful as the promoter include phenolic substances such as phenol, naphthol, alkylphenol, thiophenol, sulfurized alkylphenol, and condensation products of formaldehyde with a phenolic substance; alcohols such as methanol, 2-propanol, octyl alcohol, cellosolve, carbitol, ethylene glycol, stearyl alcohol, and cyclohexyl alcohol; amines such as aniline, phenylenediamine, phenothiazine, phenylbeta-naphthylamine, and dodecylamine. A particularly effective method for preparing the basic salts comprises mixing an acid with an excess of a basic alkaline earth metal neutralizing agent, a phenolic promoter compound, and a small amount of water and carbonating the mixture at an elevated temperature such as 60-200 C.
Extreme pressure agents and corrosion-inhibiting and oxidation-inhibiting agents are exemplified by chlorinated aliphatic hydrocarbons such as chlorinated wax; organic sulfides and polysulfides such as benzyl disulfide, bis- (chlorobenzyDdisulfide, dibutyl tetrasulfide, sulfurized sperm oil, sulfurized methyl ester of oleic acid, sulfurized alkyphenol, sulfurized dipentene, and sulfurized terpene; phosphosulfurized hydrocarbons such as the reaction product of a phosphorus sulfide with turpentine or methyl oleate; phosphorus esters including principally dihydrocarbon and trihydrocarbon phosphites such as dibutyl phosphite, diheptyl phosphite, dicyclohexyl phosphite, pentyl phenyl phosphite, dipentyl phenyl phoshite, tridecyl phosphite, distearyl phosphite, dimethyl naphthyl phosphite, oleyl 4-pentylphenyl phosphite, polypropylene (molecular weight 500)-substituted phenyl phosphite, diisobutylsubstituted phenyl phosphite; metal thiocarbamates, such as Zinc dioctyl-dithiocarbamate, and barium heptylphenyl dithiocarbamate: Group 11 metal phosphorodithioates such as zinc dicyclohexylphosphorodithioate, zinc dioctylphosphorodithioate, barium di(heptylphenyl) phosphorodithioate, cadmium dinonylphosphorodithioate, and zinc salt of a phosphorodithioic acid produced by the reaction of phosphorus pentasulfide with an equimolar mixture of isopropyl alcohol and n-hexyl alcohol.
The lubricating compositions may also contain metal detergent additives in amounts usually within the range of about 0.1% to about 20% by weight. In some applications such as in lubricating marine diesel engines the lubricating compositions may contain as much as of a metal detergent additive. They may also contain extreme pressure addition agents, viscosity index improving agents, and pour point depressing agents, each in amounts within the range of from about 0.1% to about 10%.
The following examples are illustrative of the lubricating compositions of this invention: (all percentages are by weight) 26% Example A SAE 20 mineral lubricating oil containing 0.5% of the product of Example 1.
Example B SAE 30 mineral lubricating oil containing 0.75% of the product of Example 2 and 0.1% of phosphorus as the barium salt of di-n-nonylphosphorodithioic acid.
Example C SAE 10W-30 mineral lubricating oil containing 0.4% of the product of Example 7.
Example D SAE mineral lubricating oil containing 0.1% of the product of Example 7 and 0.15% of the zinc salt of an equimolar mixture of di-cylohexylphosphorodithioic acid and di-isobutyl phosphorodithioc acid.
Example E SAE 30 mineral lubricating oil containing 2% of the product of Example 3.
Example F SAE 20W-30 mineral lubricating oil containing 5% of the product of Example 14.
Example G SAE 10W-30 mineral lubricating oil containing 1.5% of the product of Example 25 and 0.05% of phosphorous as the zinc salt of a phosphorodithioic acid prepared by the reaction of phosphorus pentasulfide with a mixture of 60% (mole) of p-butylphenol and 40% (mole) of npentyl alcohol.
Example H SAE 50 mineral lubricating oil containing 3% of the product of Example 36 and 0.1% of phosphorus as the calcium salt of di-hexylphosphorodithioate.
Example I SAE 10W-30 mineral lubricating oil containing 2% of the product of Example 48, 0.06% of phosphorus as zinc di-n-octyl-phosphorodithioate, and 1% of sulfate ash as barium mahogany sulfonate.
Example I SAE 10W-30 mineral lubricating oil containing 6% of the product of Example 60, 0.075% of phosphorus as zinc di-n-octylphosphorodithioate, and 5% of the barium salt of an acidic composition prepared by the reaction of 1000 parts of a polyisobutene having a molecular weight of 60,000 with parts of phosphorus pentasulfide at 200 C. and hydrolyzing the product with steam at C.
Example L SAE 10 mineral lubricating oil containing 2% of the product of Example 74, 0.075% of phosphorus as the adduct of zinc di-cyclohexylphosp-horodithioate treated with 0.3 mole of ethylene oxide, 2% of sulfurized sperm oil having a sulfur content of 10%, 3.5% of a poly-(alkyl methacrylate) viscosity index improver, 0.02% of a poly- (alkyl methacrylate) pour point depressant, 0.003% of a poly-(alkyl siloxane) anti-foam agent.
27 Example M SAE 10 mineral lubricating oil containing 1.5% of the product of Example 51, 0.075 of phosphorus as the ad duct obtained by heating zinc di-nonylphosphordithioate with 0.25 mole of 1,2-hexene oxide at 120 C., a sulfurized methyl ester of tall oil acid having .a sulfur content of 15%, 6% of a polybutene vicosity index improver, 0.005% of a poly-(alkyl methacrylate) anti-foam agent, and 0.5% of lard oil.
Example N SAE 20 mineral lubricating oil containing 1.5% of the product of Example 13, 0.5% of di-dodecyl phosphite, 2% of the sulfurized sperm oil having a sulfur content of 9%, a basic calcium detergent prepared by carbonating a mixture comprising mineral oil, calcium mahogany sulfonate and 6 moles of calcium hydroxide in the presence of an equi-molar mixture 10% of the mixture) of methyl alcohol and n-butyl alcohol as the promoter at the reflux temperature.
Example SAE 10 mineral lubricating oil containing 2% of the product of Example 7, 0.07% of phosphorus as zinc diocytlphosphorodithioate, 2% of a barium detergent prepared by neutralizing with barium hydroxide the hydrolyzed reaction product of a polypropylene (molecular weight 2000) with 1 mole of phosphorus pentasulfide and 1 mole of sulfur, 3% of a barium sulfonate detergent prepared by carbonating a mineral oil solution of mahogany acid, and a 500% stoichiometrically excess amount of barium hydroxide in the presence of phenol as the promoter at 180 C., 3% of a supplemental ashless detergent prepared by copolymerizing a mixture of 95% (weight) of decyl-methacrylate and (weight) of diethylamino-ethylacrylate.
Example P SAE 80 mineral lubricating oil containing 2% of the product of Example 7, 0.1% of phosphorus as zinc di-nhexylphosphorodithioate, of a chlorinated parafiin wax having a chlorine content of 40%, 2% of di-butyl tetrasulfide, 2% of sulfurized dipentene, 0.2% of oleyl amide, 0.03% of an anti-foam agent, 0.02% of a pour point depressant, and 3% of a viscosity index improver.
Example Q SAE 10 mineral lubricating oil containing 3% of the product of Example 16, 0.075% of phosphorus as the zinc salt of a phosphorodithioic acid prepared by the reaction of phosphorus pentasulfide with an equimolar mixture of n-butyl alcohol and dodecyl alcohol, 3% of a barium detergent prepared by carbonating a mineral oil solution containing 1 mole of sperm oil, 0.6 mole of octylphenol, 2 moles of barium oxide, and a small amount of water at 150 C.
Example R SAE 20 mineral lubricating oil containing 2% of the product of Example 17 and 0.07% of phosphorus as zinc di-n-octyl-phosphorodithioate.
Example S SAE 30 mineral lubricating oil containing 3% of the product of Example 48 and 0.1% of phosphorus as zinc di-(isobutyl-phenyl)-phosphorodithioate.
Example T SAE 50 mineral lubricating oil containing 2% of the product of Example 39.
Example U SAE 90 mineral lubricating oil containing 3% of the product of Example 20 and 0.2% of phosphorus as the reaction product of 4 moles of turpentine with 1 mole of phosphorus pentasulfide.
The above lubricants are merely illustrative and the scope of invention includes the use of all of the additives previously illustrated as well as others within the broad concept of this invention described herein.
The utility of the dispersant additives of this invention is shown by the results of an evaluation of the crankcase lubricants used in taxicabs which had been operated for over 50,000 miles each. In this test ten 6-cylinder 1958 Chevrolet cars (with no oil filters) were operated as a fleet of taxicabs. In each case the crankcase lubricant was a solvent refined Mid-Continent petroleum oil having a viscosity of 185 SUS/ F. and a viscosity index of 112, and containing 5.9% by volume of a poly-alkylrnethacrylate viscosity index improver and 0.59% by volume of a zinc dialky'l phosphorodithioate (the alkyl groups being isobutyl and a mixture of primary amyl). Crankcase oil drains were taken from each car at oilchange intervals of about 3,000 miles of service and these drains combined. A 30-cc. sample of each of the combined drains was mixed with 1% by weight of the dispersant additive to be tested and 2% by weight of water. This mixture then was homogenized, placed in a 100-cc. graduated cone-shaped centrifuge tube and centrifuged for two hours at 1500 rpm. The various dispersants were evaluated by noting the volume of deposited sediment in terms of cubic centimeters and also the turbidity of the supernatant oil layer. It is apparent that the more effective dispersants will give test results which show a minimum of deposited sediment and a relatively hazy supernatant oil layer.
The clarity of the supernatant oil layer was determined by the amount of light transmitted through it from a 3-volt, 0.75 watt incandescent bulb.
The results of these tests are shown in Table I.
TAB LE I Centimeters of Sediment Turbidity of Oil Layer None Prior art Product of Example 83- Product of Example 5- Product of Example 3. Product of Example 1- Product of Example 2 Product of Example 6 Clear-translucent.
o. Opaque.
s q pppp CHI-c0030,
Do. Heavy haze. Do.
The dispersant properties of the compositions of this invention may be illustrated also by the results of an oxidation-dispersancy test which is useful as a screening test for determining the effectiveness of the dispersant additive under light-duty service conditions. In this test a 350-cc. sample of a lubricating oil containing the dispersant additive is placed in a 2 x 15" borosilicate tube. A 1%" x 5%" SAE 1020 steel panel is immersed in the oil. The sample then is heated at 300 F. for 48 hours while air is bubbled through the oil at the rate of 10 liters per hour. The oxidized sample is cooled to F., homogenized, allowed to stand at room temperature for 24 hours and then filtered through two layers of No. 1 Whatman filter paper at 20 mm. Hg pressure. The weight of the precipitate, washed with naphtha and dried, is taken as a measure of the effectiveness of the dispersant additive, i.e., the greater this weight of precipitate the less effective the dispersant.
Two modifications of the above procedure may be employed; both make the test more severe: one consists of extending the test from 48 hours to 96 hours, and the other involves adding 0.5 of water, based on the weight of the test sample, to the oxidized oil before homogenization.
The lubricating oil employed in this test (Table II) was a Mid-Continent conventionally refined petroleum oil having a viscosity of about 200 SUS/ 100 F., and
29 containing 0.001% by weight of iron naphthenate (to promote oxidation).
TAB LE II Oxidation-Dispersance Test Result, mg. of deposit 100 ml. of oil tested Additive Tested (1.5% by weight of diluentlree chemical) None .s 144 o- 275 (b) Dos l, 000 (a, b) Prior art product of Example 83- 738 Prior art product of Example 84- 1,060 (b) Prior art product of Example 85- Product of Example 1-. Product of Example 2.. Product of Example 3.- Product of Example 4..
Product of Example 10 Product of Example 11- Product of Example 12. Product of Example 13. Product of Example 14. Product of Example 14- Product of Example l4 Product of Example l5 Product of Example 16 Product of Example 38 Product of Example 38 Product of Example 4L Product of Example 4L Product of Example 40 Product of Example 40. Product of Example 35 Product of Example 47-.. Product of Example 44 Product of Example 49 Modification (a): 96 hours testing. Modification (b): 0.5% of water used in the test.
Further illustration of the usefulness of the products of this invention as dispersants in motor oils was gained from a modified version of the CRC-EX-3 Engine Test. This test is recognized in the field as an important test by which lubricants can be evaluated for use under light duty service conditions. In this particular test the lubricant is used in the crankcase of a 1954 6-cylinder Chevrolet Powerglide engine for 144 hours under recurring cycling conditions, each cycle consisting of:
2 hours at an engine speed of 500 :25 r.p.m. under zero load at an oil sump temperature of 100125 F.; air-fuel ratio of 10:1;
2 hours at an engine speed of 2500 :25 r.p.m. under a load of 40 brake-horsepower at an oil sump temperature of 160-l70 F.; air-fuel ratio of 16:1;
2 hours at an engine speed of 2500 :25 rpm. under a load of 40 brake-horsepower at an oil sump temperature of 240-250 F.; air-fuel ratio of 16:1.
After completion of the test, the engine is dismantled and various parts of the engine are examined for engine deposits. The lubricant dispersant addition agent is then rated according to 1) the extent of piston ring-filling, (2) the amount of sludge formed in the engine (on a scale of 80*0, 80 being indicative of no sludge and 0 being indicative of extremely heavy sludge), and (3) the total amount of engine deposits, i.e., sludge and varnish, formed in the engine (on a scale of 100-0, 100 being indicative of no deposits and 0 being indicative of extremely heavy deposits). The results are summarized in Table III.
TAB LE III 1 Ordinarily this test lasts for 96 hours.
What is claimed is:
1. A composition comprising a major proportion of a lubricating oil and a minor proportion sufficient to impart detergency thereto of an oil-soluble acylated nitrogen compound characterized by the presence within its structure of (A) a substantially saturated hydrocarbonsubstituted polar group selected from the class consisting of acyl, acylimidoyl, and acyloXy radicals wherein the substantially saturated hydrocarbon substituent contains at least about 50 aliphatic carbon atoms and (B) a nitrogen-containing group characterized by a nitrogen atom attached directly to said polar radical.
2. The composition of claim 1 wherein the hydrocarbon substituent contains at least about 25 aliphatic carbon atoms per each polar radical.
3. The composition of claim 1 wherein the hydrocarbon substituent is a polymer of butene.
4. The composition of claim 1 wherein the hydrocarbon substituent is a polyisobutene having a molecular Weight within the range from about 700 to about 100,000.
5. The composition of claim 1 wherein the nitrogencontaining group has the formula wherein R and R are selected from the group consisting of hydrogen, hydrocarbon, amino-substituted hydrocarbon, hydroxy-substituted hydrocarbon, alkoxy-substituted hydrocarbon, amino, carbamyl, thiocaribamyl, guanyl, and acylimidoyl radicals.
6. A composition comprising a major proportion of a lubricating oil and a minor proportion sufficient to impart detergency thereto of an oil-soluble acylated nitrogen compound characterized by the presence within its structure of (A) a substantially saturated hydrocarbonsubstituted succinic radical selected from the class consisting of succinoyl, succinoylimidoyl, and succinoyloxy radicals and having at least about 50 aliphatic carbon atoms in the substantially saturated hydrocarbon substituent and (B) an amino group characterized by a nitrogen atom attached directly to said succinic radical.
7. A composition comprising a major proportion of a lubricating oil and a minor proportion sufficient to impart detergency thereto of an oil-soluble acylated nitrogen compound characterized by the presence within its structure of (A) an olefin polymer-substituted succinic radical selected from the class consisting of succinoyl, succinimidoyl, and succinoyloxy radicals, said olefin polymer having a molecular weight within the range from about 700 to about 50,000 and being a polymer of a 1- mono-olefin having from 2, to about 8 aliphatic carbon atoms, and (B) a nitrogen-containing group characterized by at least one nitrogen atom attached directly to said succinic radical, said nitrogen-containing group being derived from an alkylene amine.
8. A composition comprising a major proportion of a lubricating oil and a minor proportion sufficient to impart detergency thereto of an oil-soluble acylated nitrogen-containing composition prepared by the process comprising rcacting at a temperature of from about C. and up to the decomposition point a high molecular weight acid-producing compound characterized by the presence within its structure of a high molecular weight oil-solubiliz'ing substantially saturated group having at least about 50 aliphatic carbon atoms and at least one acid-producing group having the structural configuration 2 moles, per equivalent of said acid producing compound, of a nitrogen-containing compound characterized by the 31 presence within its structure of at least one radical having the structural configuration 1I]' H 9. The composition of claim 8 wherein the high molecular weight acid-producing compound is selected from the group consisting of substituted succinic acids having the structural formula RC|1HCOOH CH2-COOH and substituted succinic anhydrides having the structural formula RCHCO o CHz-GO in which structural formulas R is a substantially saturated radical having at least about 50 aliphatic carbon atoms and a butene polymer group.
10. The composition of claim 8 wherein the nitrogencontaining compound is characterized by the structural formula RNH Iii!
in which structural formula R and R" are selected from the group consisting of hydrogen, hydrocarbon, amino-su'bstituted hydrocarbon, alkoxy-substitut ed hydrocarbon, amino, carbamyl, thiocarbamyl, guanyl, and acyl-imidoyl radicals.
11. The composition of claim 8 wherein the nitrogencontaining compound is a polyethylene polyamine.
12. A lubricating composition comprising a major proportion of a lubricating oil and a minor proportion, sufficient to impart detergency thereto, of an amide having the structural formula wherein x is at least 1, R is a substantially saturated hydrocarbon group having at least about 50 aliphatic carbon atoms and at least about 25 aliphatic carbon atoms for each unit of x, and NR' is selected from the class consisting of (A) radicals derived from an alkylene polyamine by the removal of a hydrogen atom from an amino group and (B) radicals derived from an alkylene polyamine by the removal of a hydrogen atom from an amino group and characterized by the presence, on the nitrogen atom of at least one additional amino group, of a complex substituent having the formula 13. A lubricating composition comprising a major proportion of a lubricating oil and a minor proportion, sufficient to impart detergency thereto, of an amide having the structural formula wherein x is at least 1, R is a substantially saturated hydrocarbon group having at least about 50 aliphatic carbon atoms and at least about 25 aliphatic carbon atoms for each unit of x, and NR is selected from the class consisting of (A) radicals derived from an ethylene polyamine by the removal of a hydrogen atom from an amino group and (B) radicals derived from an ethylene polyamine by the removal of a hydrogen atom from an amino group and characterized by the presence, on the nitrogen atom of at least one additional amino group, of a complex substituent having the formula 14. The lubricating composition of claim 12 wherein R of the structural formula is a polyisobutene group having a molecular weight of from about 750 to 5000, x is about 1, and NR' is derived from an ethylene polyamine having from 2 to 8 amino groups by the removal of a hydrogen atom from an amino group and characterized by the presence, on the nitrogen atom of at least one additional amino group, of a complex substitutent having the formula 15. The composition of claim 8 wherein the oil-soluble acylated nitrogen-containing composition is prepared by a process which comprises reacting at a temperature within the range of from about C. to about 250 C. a substantially saturated hydrocarbon substituted succinicacid-proclucing compound having at least about 50 aliphatic carbon atoms in the substantially saturated hydrocarbon substituent with from about one-half equivalent to about 2 moles, per equivalent of said succinic-acidproducing compound, of an alkylene polyamine.
16. The composition of claim 8 wherein the oil-soluble acylated nitrogen-containing composition is prepared by a process which comprises reacting at a temperature within the range of from about 80 C. to about 250 C. a substantially saturated hydrocarbon substituted succinicacid-producing compound having at least about 50 aliphatic carbon atoms in the substantially saturated hydrocarbon substituent with from about one-half equivalent to about 2 moles per equivalent of said succinic-acidproducing compound, of a polyethylene polyamine.
17. The composition of claim 8 wherein the oil-soluble acylated nitrogen-containing composition is prepared by a process which comprises reacting at a temperature within the range of from about 80 C. to about 250 C. a substantially saturated hydrocarbon substituted succinicacid-producing compound having at least about 50 aliphatic carbon atoms in the substantially saturated hydrocarbon substituent with from about one-half equivalent to about 2 moles, per equivalent of said succinic-acidproducing compound, of a hydroxyalkyl amine.
18. The composition of claim 1 wherein it contains additionally an ash-containing detergent.
References Cited by the Examiner UNITED STATES PATENTS 3,018,250 1/1962 Anderson et al 25251 3,024,195 3/ 1962 Drummond et al. 252-51.5 3,131,150 4/1964 Stuart et al. 252-51.5 X 3,154,560 10/1964 Osuch 252-51.5 X 3,172,892 3/1965 Le Suer et al 25251.5 X 3,219,666 11/1965 Norman et al 2525l.5 X
DANIEL E. WYMAN, Primary Examiner.
P. P. GARVIN, Assistant Examiner.
UNITED STATES PATENT OFFICE CERTIFICATE OF CORRECTION Patent No 3 ,272 746 September 13 1966 William M. Le Suer et al.
It is hereby certified'that error appears in the above numbered patent requiring correction and that the said Letters Patent should read as corrected below.
Column 1, line 57, for "hours" read hour column 2, line 20, for "provide" read proved column 3, line 16, for "aldehydrp g read aldehydo column 4, lines 17 and I 2 18 for "R C read R C- column 5, line 9, for "High" read Higher line 14, for "Encycylopedia" read Encyclopedia column 10, lines 8 to 10, the right-hand formula should appear as shown below instead of as in the patent column 12 line 9 for "showin" read shown in line 13 for "polyisobuentyl" read polyisobutenyl column 13,
line 24, for "amine" read amide line 40, for "butylenyl" read butenyl column 14, line 31, for "125 C./mm."
read 125 C./30 mm. column 18, line 71, for "temperautre" read temperature column 22, line 45, for "corresponding" read (corresponding column 26, line 18, for "phosphorodithioc" read phosphorodithioic line 49, for "diosopropyl-" read di-isopropyl column 27, line 4, for "dinonylphosphordithioate" read dinonylphosphorodithioate line 24, for "octlphosphorodithioate" read octylphosphorodithioate line 43, for "0.03%" read 0.003%
Signed and sealed this 3rd day of September 1968.
(SEAL) Attest:
EDWARD M.FLETCHER,JR. EDWARD J. BRENNER Attesting Officer Commissioner of Patents

Claims (2)

1. A COMPOSITION COMPRISING A MAJOR PROPORTION OF A LUBRICATING OIL AND A MINOR PROPORTION SUFFICIENT TO IMPART DETERGENCY THERETO OF AN OIL-SOLUBLE ACYLATED NITROGEN COMPOUND CHARACTERIZED BY THE PRESENCE WITHIN ITS STRUCTURE OF (A) A SUBSTANTIALLY STURATED HYDROCARBONSUBSTITUTED POLAR GROUP SELECTED FROM THE CLASS CONSISTING OF ACYL, ACYLIMIDOYL, AND ACYLOXY RADICALS WHEREIN THE SUBSTANTIALLY STURATED HYDROCARBON STBSTITUENT CONTAINS AT LEAST ABOUT 50 ALIPHATIC CARBON ATOMS AND (B) A NITRO-CONTTAINING GROUP CAHRACTERIZED BY A NITROGEN ATOM ATTACHED DIRECTLY TO SAID POLAR RADICAL.
5. THE COMPOSITION OF CLAIM 1 WHEREIN THE NITROGENCONTAINING GROUP HAS THE FORMULA
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Cited By (571)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3340281A (en) * 1965-06-14 1967-09-05 Standard Oil Co Method for producing lubricating oil additives
US3359204A (en) * 1966-12-19 1967-12-19 Ethyl Corp Lubricating oil dispersant
US3415750A (en) * 1963-10-04 1968-12-10 Monsanto Co Imidazolines having polyalkenylsuccinimido-containing substituents
US3438899A (en) * 1968-02-23 1969-04-15 Chevron Res Alkenyl succinimide of tris (aminoalkyl) amine
US3442808A (en) * 1966-11-01 1969-05-06 Standard Oil Co Lubricating oil additives
US3445386A (en) * 1967-01-13 1969-05-20 Mobil Oil Corp Detergent compositions
US3448048A (en) * 1967-01-23 1969-06-03 Lubrizol Corp Lubricant containing a high molecular weight acylated amine
US3452002A (en) * 1966-12-22 1969-06-24 Exxon Research Engineering Co Adducts of alkylene imines and carboxylic acids
US3519565A (en) * 1967-09-19 1970-07-07 Lubrizol Corp Oil-soluble interpolymers of n-vinylthiopyrrolidones
US3522179A (en) * 1963-04-23 1970-07-28 Lubrizol Corp Lubricating composition containing esters of hydrocarbon-substituted succinic acid
US3793201A (en) * 1970-12-28 1974-02-19 Lubrizol Corp Stabilized basic magnesium sulfonate compositions
US3879306A (en) * 1973-11-05 1975-04-22 Texaco Inc Automatic transmission fluid
US3883320A (en) * 1972-12-07 1975-05-13 Standard Oil Co Reducing deposits and smoke from jet fuels with additives incorporating an ammonium salt
US3960889A (en) * 1973-07-09 1976-06-01 Texaco Inc. Dehydrohalogenated polyalkene-maleic anhydride reaction product
US4005021A (en) * 1974-06-10 1977-01-25 Standard Oil Company (Indiana) Oil-soluble reaction products of (a) a high molecular weight olefin polymer, acrylonitrile, chlorine, an amine and maleic anhydride, with (g) an aliphatic amines; and lubricant compositions containing the same
US4029148A (en) * 1976-09-13 1977-06-14 Atlantic Richfield Company Well fracturing method
US4081388A (en) * 1975-04-18 1978-03-28 Orogil Compositions based on alkenylsuccinimides as additives for lubricating oils
US4089794A (en) * 1975-06-25 1978-05-16 Exxon Research & Engineering Co. Polymeric additives for fuels and lubricants
US4138370A (en) * 1976-04-26 1979-02-06 Exxon Research & Engineering Co. Multipurpose lubricating oil additive based on electrophilically terminated anion of oxidized ethylene copolymer
US4151173A (en) * 1971-05-17 1979-04-24 The Lubrizol Corporation Acylated polyoxyalkylene polyamines
FR2404668A1 (en) * 1977-10-03 1979-04-27 Exxon Research Engineering Co COMPOSITION OF LUBRICATING OIL ADDITIONED TO A POLYOL ESTER AND AN IMIDE
US4153567A (en) * 1977-11-10 1979-05-08 Milliken Research Corporation Additives for lubricants and fuels
US4159956A (en) * 1978-06-30 1979-07-03 Chevron Research Company Succinimide dispersant combination
US4163644A (en) * 1978-04-25 1979-08-07 The Rolfite Company Suspension of coal in fuel oils
US4171273A (en) * 1977-03-14 1979-10-16 Texaco Inc. Fatty alkyl succinate ester and succinimide modified copolymers of ethylene and an alpha olefin
US4194985A (en) * 1974-01-14 1980-03-25 The Lubrizol Corporation Polymeric compositions, method for their preparation, and lubricants containing them
US4237022A (en) * 1979-10-01 1980-12-02 The Lubrizol Corporation Tartarimides and lubricants and fuels containing the same
US4239633A (en) * 1979-06-04 1980-12-16 Exxon Research & Engineering Co. Molybdenum complexes of ashless polyol ester dispersants as friction-reducing antiwear additives for lubricating oils
US4240803A (en) * 1978-09-11 1980-12-23 Mobil Oil Corporation Fuel containing novel detergent
US4248719A (en) * 1979-08-24 1981-02-03 Texaco Inc. Quaternary ammonium salts and lubricating oil containing said salts as dispersants
US4256595A (en) * 1978-09-28 1981-03-17 Texaco Inc. Diesel lubricant composition containing 5-amino-triazole-succinic anhydride reaction product
US4257779A (en) * 1976-12-23 1981-03-24 Texaco Inc. Hydrocarbylsuccinic anhydride and aminotriazole reaction product additive for fuel and mineral oils
US4263015A (en) * 1976-12-23 1981-04-21 Texaco Inc. Rust inhibitor and oil composition containing same
EP0031236A2 (en) * 1979-12-20 1981-07-01 The British Petroleum Company p.l.c. Lubricant additives, their method of preparation and lubricants containing them
US4326973A (en) * 1981-01-13 1982-04-27 Texaco Inc. Quaternary ammonium succinimide salt composition and lubricating oil containing same
US4326972A (en) * 1978-06-14 1982-04-27 The Lubrizol Corporation Concentrates, lubricant compositions and methods for improving fuel economy of internal combustion engine
US4400282A (en) * 1980-12-05 1983-08-23 Gulf Research & Development Company Lubricating oils containing quaternary ammonium thiomolybdates
US4440658A (en) * 1981-01-16 1984-04-03 Mobil Oil Corporation Anti-rust compositions
US4440659A (en) * 1982-02-19 1984-04-03 Ethyl Corporation Lubricating oil ashless dispersant and lubricating oils containing same
US4491527A (en) * 1982-04-26 1985-01-01 The Lubrizol Corporation Ester-heterocycle compositions useful as "lead paint" inhibitors in lubricants
US4491455A (en) * 1982-02-10 1985-01-01 Nippon Oil And Fats Co., Ltd. Method for improving cold flow of fuel oils
US4505718A (en) * 1981-01-22 1985-03-19 The Lubrizol Corporation Organo transition metal salt/ashless detergent-dispersant combinations
US4559155A (en) * 1982-08-09 1985-12-17 The Lubrizol Corporation Hydrocarbyl substituted carboxylic acylating agent derivative containing combinations, and fuels containing same
US4560490A (en) * 1983-02-04 1985-12-24 Institut Francais Du Petrole Dispersing additive compositions for lubricating oils and their manufacture
US4564460A (en) * 1982-08-09 1986-01-14 The Lubrizol Corporation Hydrocarbyl-substituted carboxylic acylating agent derivative containing combinations, and fuels containing same
US4575526A (en) * 1982-08-09 1986-03-11 The Lubrizol Corporation Hydrocarbyl substituted carboxylic acylaging agent derivative containing combinations, and fuels containing same
US4579674A (en) * 1981-12-28 1986-04-01 Texaco Inc. Hydrocarbylsuccinimide of a secondary hydroxyl-substituted polyamine and lubricating oil containing same
US4596663A (en) * 1982-08-09 1986-06-24 The Lubrizol Corporation Carboxylic acylating agents substituted with olefin polymers of high molecular weight mono-olefins, derivatives thereof, and fuels and lubricants containing same
US4613342A (en) * 1982-08-09 1986-09-23 The Lubrizol Corporation Hydrocarbyl substituted carboxylic acylating agent derivative containing combinations, and fuels containing same
US4617137A (en) * 1984-11-21 1986-10-14 Chevron Research Company Glycidol modified succinimides
US4623684A (en) 1982-08-09 1986-11-18 The Lubrizol Corporation Hydrocarbyl substituted carboxylic acylating agent derivative containing combinations, and fuels containing same
US4631070A (en) * 1984-11-21 1986-12-23 Chevron Research Company Glycidol modified succinimides and fuel compositions containing the same
US4637886A (en) * 1982-12-27 1987-01-20 Exxon Research & Engineering Co. Macrocyclic polyamine and polycyclic polyamine multifunctional lubricating oil additives
US4652273A (en) * 1981-07-30 1987-03-24 Institut Francais Du Petrole Hydrocarbon middle distillates composition containing nitrogen-containing additives for decreasing its cloud point
US4659338A (en) * 1985-08-16 1987-04-21 The Lubrizol Corporation Fuel compositions for lessening valve seat recession
WO1987003003A1 (en) 1985-11-08 1987-05-21 The Lubrizol Corporation Fuel compositions
US4695390A (en) * 1985-01-04 1987-09-22 The Lubrizol Corporation Reaction product of polyalrylene-substituted polycarboxylic acid acylating agent, polyamine and sulfolene as a dispersant
WO1988001272A2 (en) 1986-08-14 1988-02-25 The Lubrizol Corporation Borated amine salts of monothiophosphoric acids
US4744798A (en) * 1982-09-30 1988-05-17 Mobil Oil Corporation Benzophenone derivatives as fuel additives
US4804389A (en) * 1985-08-16 1989-02-14 The Lubrizol Corporation Fuel products
EP0310367A1 (en) * 1987-09-30 1989-04-05 Amoco Corporation Medium speed diesel engine lubricating oils
EP0310365A1 (en) * 1987-09-30 1989-04-05 Amoco Corporation Engine seal compatible dispersant for lubricating oils
US4820432A (en) * 1987-07-24 1989-04-11 Exxon Chemical Patents Inc. Lactone-modified, Mannich base dispersant additives useful in oleaginous compositions
US4855074A (en) * 1988-03-14 1989-08-08 Ethyl Petroleum Additives, Inc. Homogeneous additive concentrates and their formation
US4863624A (en) * 1987-09-09 1989-09-05 Exxon Chemical Patents Inc. Dispersant additives mixtures for oleaginous compositions
US4866139A (en) * 1986-10-07 1989-09-12 Exxon Chemical Patents Inc. Lactone modified, esterified dispersant additives useful in oleaginous compositions
US4866141A (en) * 1986-10-07 1989-09-12 Exxon Chemical Patents Inc. Lactone modified, esterfied or aminated additives useful in oleaginous compositions and compositions containing same
US4866140A (en) * 1986-10-07 1989-09-12 Exxon Chemical Patents Inc. Lactone modified adducts or reactants and oleaginous compositions containing same
US4870197A (en) * 1986-12-12 1989-09-26 Exxon Chemical Patents Inc. Method for preparing salts of polyolefinic substituted dicarboxylic acids
EP0351964A1 (en) 1988-06-24 1990-01-24 Exxon Chemical Patents Inc. Synergistic combination of additives useful in power transmitting compositions
US4904401A (en) * 1988-06-13 1990-02-27 The Lubrizol Corporation Lubricating oil compositions
US4906394A (en) * 1986-10-07 1990-03-06 Exxon Chemical Patents Inc. Lactone modified mono-or dicarboxylic acid based adduct dispersant compositions
US4938881A (en) * 1988-08-01 1990-07-03 The Lubrizol Corporation Lubricating oil compositions and concentrates
US4943382A (en) * 1988-04-06 1990-07-24 Exxon Chemical Patents Inc. Lactone modified dispersant additives useful in oleaginous compositions
US4952328A (en) * 1988-05-27 1990-08-28 The Lubrizol Corporation Lubricating oil compositions
US4954276A (en) * 1986-10-07 1990-09-04 Exxon Chemical Patents Inc. Lactone modified adducts or reactants and oleaginous compositions containing same
US4954572A (en) * 1988-11-07 1990-09-04 Exxon Chemical Patents Inc. Dispersant additives prepared from monoepoxy alcohols
US4954277A (en) * 1986-10-07 1990-09-04 Exxon Chemical Patents Inc. Lactone modified, esterified or aminated additives useful in oleaginous compositions and compositions containing same
US4957649A (en) * 1988-08-01 1990-09-18 The Lubrizol Corporation Lubricating oil compositions and concentrates
US4957645A (en) * 1988-02-29 1990-09-18 Exxon Chemical Patents Inc. Oil soluble dispersant additives useful in oleaginous compositions
US4963275A (en) * 1986-10-07 1990-10-16 Exxon Chemical Patents Inc. Dispersant additives derived from lactone modified amido-amine adducts
US4971711A (en) * 1987-07-24 1990-11-20 Exxon Chemical Patents, Inc. Lactone-modified, mannich base dispersant additives useful in oleaginous compositions
EP0399764A1 (en) 1989-05-22 1990-11-28 Ethyl Petroleum Additives Limited Lubricant compositions
US4981602A (en) * 1988-06-13 1991-01-01 The Lubrizol Corporation Lubricating oil compositions and concentrates
US5024677A (en) * 1990-06-11 1991-06-18 Nalco Chemical Company Corrosion inhibitor for alcohol and gasohol fuels
US5026495A (en) * 1987-11-19 1991-06-25 Exxon Chemical Patents Inc. Oil soluble dispersant additives useful in oleaginous compositions
US5030369A (en) * 1988-02-29 1991-07-09 Exxon Chemical Patents Inc. Oil soluble dispersant additives useful in oleaginous compositions
US5032320A (en) * 1986-10-07 1991-07-16 Exxon Chemical Patents Inc. Lactone modified mono- or dicarboxylic acid based adduct dispersant compositions
US5041622A (en) * 1988-04-22 1991-08-20 The Lubrizol Corporation Three-step process for making substituted carboxylic acids and derivatives thereof
US5053152A (en) * 1985-03-14 1991-10-01 The Lubrizol Corporation High molecular weight nitrogen-containing condensates and fuels and lubricants containing same
US5053150A (en) * 1988-02-29 1991-10-01 Exxon Chemical Patents Inc. Polyepoxide modified adducts or reactants and oleaginous compositions containing same
US5057617A (en) * 1988-11-07 1991-10-15 Exxon Chemical Patents Inc. Dispersant additives prepared from monoepoxy thiols
US5080815A (en) * 1987-09-30 1992-01-14 Amoco Corporation Method for preparing engine seal compatible dispersant for lubricating oils comprising reacting hydrocarbyl substituted discarboxylic compound with aminoguanirise or basic salt thereof
US5085788A (en) * 1987-11-19 1992-02-04 Exxon Chemical Patents Inc. Oil soluble dispersant additives useful in oleaginous compositions
US5102566A (en) * 1987-10-02 1992-04-07 Exxon Chemical Patents Inc. Low ash lubricant compositions for internal combustion engines (pt-727)
US5141658A (en) * 1986-11-07 1992-08-25 Dibiase Stephen A Lubricant composition comprising a sulfur additive and a borated dispersant
US5141657A (en) * 1987-10-02 1992-08-25 Exxon Chemical Patents Inc. Lubricant compositions for internal combustion engines
US5147414A (en) * 1989-08-03 1992-09-15 Texaco Inc. Process for producing ori control additives
US5160350A (en) * 1988-01-27 1992-11-03 The Lubrizol Corporation Fuel compositions
US5164103A (en) * 1988-03-14 1992-11-17 Ethyl Petroleum Additives, Inc. Preconditioned atf fluids and their preparation
US5174915A (en) * 1987-09-30 1992-12-29 Ethyl Petroleum Additives, Inc. Medium speed diesel engine lubricating oils
US5182041A (en) * 1989-05-01 1993-01-26 Texaco Inc. Dispersant - anti-oxidant additive and lubricating oil composition containing same
US5198133A (en) * 1988-03-14 1993-03-30 Ethyl Petroleum Additives, Inc. Modified succinimide or sucinamide dispersants and their production
US5205947A (en) * 1988-11-07 1993-04-27 Exxon Chemical Patents Inc. Dispersant additives comprising amine adducts of dicarboxylic acid monoepoxy thiol reaction products
US5217634A (en) * 1988-02-29 1993-06-08 Exxon Chemical Patents Inc. Polyepoxide modified adducts or reactants and oleaginous compositions containing same
US5221491A (en) * 1991-08-09 1993-06-22 Exxon Chemical Patents Inc. Two-cycle oil additive
US5232616A (en) * 1990-08-21 1993-08-03 Chevron Research And Technology Company Lubricating compositions
EP0558835A1 (en) 1992-01-30 1993-09-08 Albemarle Corporation Biodegradable lubricants and functional fluids
US5256325A (en) * 1988-02-29 1993-10-26 Exxon Chemical Patents Inc. Polyanhydride modified adducts or reactants and oleaginous compositions containing same
US5275748A (en) * 1988-02-29 1994-01-04 Exxon Chemical Patents Inc. Polyanhydride modified adducts or reactants and oleaginous compositions containing same
US5292813A (en) * 1992-10-02 1994-03-08 Exxon Research & Engineering Co. Fullerene-grafted polymers and processes of making
US5292444A (en) * 1992-10-02 1994-03-08 Exxon Research And Engineering Company Lube oil compositions containing fullerene-grafted polymers
US5302304A (en) * 1990-12-21 1994-04-12 Ethyl Corporation Silver protective lubricant composition
US5304315A (en) * 1992-04-15 1994-04-19 Exxon Chemical Patents Inc. Prevention of gel formation in two-cycle oils
US5312554A (en) * 1987-05-26 1994-05-17 Exxon Chemical Patents Inc. Process for preparing stable oleaginous compositions
US5312555A (en) * 1990-02-16 1994-05-17 Ethyl Petroleum Additives, Inc. Succinimides
US5320765A (en) * 1987-10-02 1994-06-14 Exxon Chemical Patents Inc. Low ash lubricant compositions for internal combustion engines
US5330667A (en) * 1992-04-15 1994-07-19 Exxon Chemical Patents Inc. Two-cycle oil additive
US5334329A (en) * 1988-10-07 1994-08-02 The Lubrizol Corporation Lubricant and functional fluid compositions exhibiting improved demulsibility
EP0611818A1 (en) 1990-07-31 1994-08-24 Exxon Chemical Patents Inc. Low pressure derived mixed phosphorous- and sulfur-containing reaction products useful in power transmitting compositions and process for preparing the same
US5354484A (en) * 1986-06-13 1994-10-11 The Lubrizol Corporation Phosphorus-containing lubricant and functional fluid compositions
US5356552A (en) * 1993-03-09 1994-10-18 Chevron Research And Technology Company, A Division Of Chevron U.S.A. Inc. Chlorine-free lubricating oils having modified high molecular weight succinimides
EP0629614A1 (en) * 1993-05-27 1994-12-21 Hoechst Aktiengesellschaft Substituted succinimides
WO1994029413A1 (en) * 1993-06-16 1994-12-22 Ethyl Corporation Ashless dispersants, their preparation, and their use
WO1995000607A1 (en) * 1993-06-25 1995-01-05 Ethyl Corporation Fluoroelastomer-friendly crankcase and drivetrain lubricants and their use
US5389273A (en) * 1988-03-14 1995-02-14 Ethyl Petroleum Additives, Inc. Modified succinimide or succinamide dispersants and their production
US5430105A (en) * 1992-12-17 1995-07-04 Exxon Chemical Patents Inc. Low sediment process for forming borated dispersant
US5439606A (en) * 1988-03-14 1995-08-08 Ethyl Petroleum Additives, Inc. Modified succinimide or succinamide dispersants and their production
US5439607A (en) * 1993-12-30 1995-08-08 Exxon Chemical Patents Inc. Multifunctional viscosity index improver-dispersant antioxidant
EP0683220A2 (en) 1994-05-18 1995-11-22 Ethyl Corporation Lubricant additive compositions
US5490945A (en) * 1991-04-19 1996-02-13 The Lubrizol Corporation Lubricating compositions and concentrates
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
EP0713907A2 (en) 1994-09-26 1996-05-29 Ethyl Petroleum Additives Limited Zinc additives of enhanced performance capabilities
EP0713908A1 (en) 1994-11-22 1996-05-29 Ethyl Corporation Power transmission fluids
US5554310A (en) * 1992-12-17 1996-09-10 Exxon Chemical Patents Inc. Trisubstituted unsaturated polymers
US5562864A (en) * 1991-04-19 1996-10-08 The Lubrizol Corporation Lubricating compositions and concentrates
US5614480A (en) * 1991-04-19 1997-03-25 The Lubrizol Corporation Lubricating compositions and concentrates
EP0776963A1 (en) 1995-12-01 1997-06-04 Chevron Chemical Company Polyalkylene succinimides and post-treated derivatives thereof
EP0778333A2 (en) 1995-11-09 1997-06-11 The Lubrizol Corporation Carboxylic compositions, derivatives, lubricants, fuels and concentrates
EP0831104A2 (en) 1996-08-20 1998-03-25 Chevron Chemical Company Novel dispersant terpolymers
US5756428A (en) * 1986-10-16 1998-05-26 Exxon Chemical Patents Inc. High functionality low molecular weight oil soluble dispersant additives useful in oleaginous composition
US5814111A (en) * 1995-03-14 1998-09-29 Shell Oil Company Gasoline compositions
JP2864146B2 (en) 1989-04-21 1999-03-03 アジップ・ペトローリ・エセ・ピ・ア Manufacturing method of fuel or lubricating oil
EP0921136A1 (en) * 1997-12-03 1999-06-09 The Lubrizol Corporation Nitrogen containing dispersant-viscosity improvers
US5955404A (en) * 1991-04-17 1999-09-21 Mobil Oil Corporation Lubricant and fuel compositions containing an organo-substituted diphenyl sulfide
US6051537A (en) * 1985-07-11 2000-04-18 Exxon Chemical Patents Inc Dispersant additive mixtures for oleaginous compositions
US6127321A (en) * 1985-07-11 2000-10-03 Exxon Chemical Patents Inc Oil soluble dispersant additives useful in oleaginous compositions
CN1064271C (en) * 1995-12-28 2001-04-11 华南理工大学 Surfactant for emulsified-liquid film and preparation method thereof
US6294506B1 (en) 1993-03-09 2001-09-25 Chevron Chemical Company Lubricating oils having carbonated sulfurized metal alkyl phenates and carbonated metal alkyl aryl sulfonates
US6306802B1 (en) 1994-09-30 2001-10-23 Exxon Chemical Patents Inc. Mixed antioxidant composition
EP1188813A1 (en) * 2000-09-19 2002-03-20 Ethyl Corporation Lubricants comprising friction modifiers
US6376434B1 (en) * 1996-10-29 2002-04-23 Idemitsu Kosan Co., Ltd. Lube oil compositions for diesel engines
US6440905B1 (en) * 2001-04-24 2002-08-27 The Lubrizol Corporation Surfactants and dispersants by in-line reaction
US20020193650A1 (en) * 2001-05-17 2002-12-19 Goze Maria Caridad B. Low noack volatility poly alpha-olefins
US6617287B2 (en) 2001-10-22 2003-09-09 The Lubrizol Corporation Manual transmission lubricants with improved synchromesh performance
US20030173251A1 (en) * 2000-12-22 2003-09-18 Antonio Gutierrez Hydroxy aromatic mannich base condensation products and the use thereof as soot dispersants in lubricating oil compositions
US20030172584A1 (en) * 2002-03-13 2003-09-18 Henly Timothy J. Fuel lubricity additives derived from hydrocarbyl succinic anhydrides and hydroxy amines, and middle distillate fuels containing same
US6624123B2 (en) * 1997-04-11 2003-09-23 Chevron Chemical S.A. Use of surfactants with high molecular weight for improving the filterability in hydraulic lubricants
US6627584B2 (en) 2002-01-28 2003-09-30 Ethyl Corporation Automatic transmission fluid additive comprising reaction product of hydrocarbyl acrylates and dihydrocarbyldithiophosphoric acids
US6642191B2 (en) 2001-11-29 2003-11-04 Chevron Oronite Company Llc Lubricating oil additive system particularly useful for natural gas fueled engines
US20040033908A1 (en) * 2002-08-16 2004-02-19 Deckman Douglas E. Functional fluid lubricant using low Noack volatility base stock fluids
US6756348B2 (en) 2001-11-29 2004-06-29 Chevron Oronite Company Llc Lubricating oil having enhanced resistance to oxidation, nitration and viscosity increase
US20040147410A1 (en) * 2003-01-15 2004-07-29 Milner Jeffrey L Extended drain, thermally stable, gear oil formulations
US20040235682A1 (en) * 2003-05-22 2004-11-25 Chevron Oronite Company Llc Low emission diesel lubricant with improved corrosion protection
US6827750B2 (en) 2001-08-24 2004-12-07 Dober Chemical Corp Controlled release additives in fuel systems
US6835218B1 (en) 2001-08-24 2004-12-28 Dober Chemical Corp. Fuel additive compositions
EP1503316A1 (en) 2003-07-30 2005-02-02 Ethyl Petroleum Additives, Inc. Fuel consumption economy credits method
US6860241B2 (en) 1999-06-16 2005-03-01 Dober Chemical Corp. Fuel filter including slow release additive
EP1512736A1 (en) * 2003-09-05 2005-03-09 Infineum International Limited Stabilised diesel fuel additive compositions
US20050065043A1 (en) * 2003-09-23 2005-03-24 Henly Timothy J. Power transmission fluids having extended durability
US20050070445A1 (en) * 2003-09-30 2005-03-31 Nelson Kenneth D. Stable colloidal suspensions and lubricating oil compositions containing same
US20050101497A1 (en) * 2003-11-12 2005-05-12 Saathoff Lee D. Compositions and methods for improved friction durability in power transmission fluids
US20050101494A1 (en) * 2003-11-10 2005-05-12 Iyer Ramnath N. Lubricant compositions for power transmitting fluids
US20050181959A1 (en) * 2004-02-17 2005-08-18 Esche Carl K.Jr. Lubricant and fuel additives derived from treated amines
EP1568759A2 (en) 2004-02-27 2005-08-31 Afton Chemical Corporation Power transmission fluids
US20050202980A1 (en) * 2004-03-10 2005-09-15 Loper John T. Novel additives for lubricants and fuels
US20060025313A1 (en) * 2004-07-29 2006-02-02 Chevron Oronite Company Llc Lubricating oil composition for internal combustion engines
US7001531B2 (en) 2001-08-24 2006-02-21 Dober Chemical Corp. Sustained release coolant additive composition
US20060059770A1 (en) * 2004-09-17 2006-03-23 Sutkowski Andrew C Fuel oils
EP1640438A1 (en) 2004-09-17 2006-03-29 Infineum International Limited Improvements in Fuel Oils
US20060135375A1 (en) * 2004-12-21 2006-06-22 Chevron Oronite Company Llc Anti-shudder additive composition and lubricating oil composition containing the same
US20060264339A1 (en) * 2005-05-19 2006-11-23 Devlin Mark T Power transmission fluids with enhanced lifetime characteristics
US20070000745A1 (en) * 2005-06-30 2007-01-04 Cameron Timothy M Methods for improved power transmission performance
US20070004603A1 (en) * 2005-06-30 2007-01-04 Iyer Ramnath N Methods for improved power transmission performance and compositions therefor
US20070027267A1 (en) * 2005-04-29 2007-02-01 Chevron Oronite Company Llc Lubricating oil additive composition and method of making the same
US20070042916A1 (en) * 2005-06-30 2007-02-22 Iyer Ramnath N Methods for improved power transmission performance and compositions therefor
US20070042917A1 (en) * 2005-07-12 2007-02-22 Ramanathan Ravichandran Amine Tungstates and Lubricant Compositions
EP1757673A1 (en) 2005-08-23 2007-02-28 Chevron Oronite Company LLC Lubricating oil composition for internal combustion engines
US20070049503A1 (en) * 2005-08-31 2007-03-01 Chevron Oronite Company Llc Lubricating oil additive composition and method of making the same
US20070054813A1 (en) * 2003-09-25 2007-03-08 Chip Hewette Boron free automotive gear oil
US20070078066A1 (en) * 2005-10-03 2007-04-05 Milner Jeffrey L Lubricant formulations containing extreme pressure agents
US20070105728A1 (en) * 2005-11-09 2007-05-10 Phillips Ronald L Lubricant composition
US20070111906A1 (en) * 2005-11-12 2007-05-17 Milner Jeffrey L Relatively low viscosity transmission fluids
US20070123437A1 (en) * 2005-11-30 2007-05-31 Chevron Oronite Company Llc Lubricating oil composition with improved emission compatibility
US20070142237A1 (en) * 2005-11-09 2007-06-21 Degonia David J Lubricant composition
US20070142660A1 (en) * 2005-11-09 2007-06-21 Degonia David J Salt of a sulfur-containing, phosphorus-containing compound, and methods thereof
US20070142659A1 (en) * 2005-11-09 2007-06-21 Degonia David J Sulfur-containing, phosphorus-containing compound, its salt, and methods thereof
US20070149689A1 (en) * 2005-12-28 2007-06-28 Xiaorong Wang Rubber composition having good wet-traction properties and a low aromatic-oil content
US20070270317A1 (en) * 2006-05-19 2007-11-22 Milner Jeffrey L Power Transmission Fluids
US20080015124A1 (en) * 2006-07-14 2008-01-17 Devlin Mark T Lubricant composition
WO2008013698A1 (en) 2006-07-21 2008-01-31 Exxonmobil Research And Engineering Company Method for lubricating heavy duty geared apparatus
EP1916293A1 (en) 2006-10-27 2008-04-30 Chevron Oronite Company LLC A lubricating oil additive composition and method of making the same
EP1916292A1 (en) 2006-10-27 2008-04-30 Chevron Oronite Company LLC A lubricating oil additive composition and method of making the same
US20080103236A1 (en) * 2006-10-27 2008-05-01 Chevron Oronite Company Llc Lubricating oil additive composition and method of making the same
US20080103074A1 (en) * 2006-10-27 2008-05-01 Chevron Oronite Company Llc Lubricating oil additive composition and method of making the same
US20080103076A1 (en) * 2006-10-27 2008-05-01 Chevron Oronite Company Llc Lubricating oil additive composition and method of making the same
US20080113889A1 (en) * 2006-10-27 2008-05-15 Chevron Oronite Company Llc lubricating oil additive composition and method of making the same
US20080153972A1 (en) * 2006-12-22 2008-06-26 Xiaorong Wang Reduced Oil Rubber Compositions Including N-Substituted Polyalkylene Succinimide Derivates and Methods For Preparing Such Compositions
EP1942177A2 (en) 2006-12-19 2008-07-09 Chevron Oronite Company LLC Lubricating oil providing enhanced piston cleanliness
EP1947164A1 (en) 2006-12-21 2008-07-23 Chevron Oronite Technology B.V. Engine lubricant with enhanced thermal stability
EP1947161A1 (en) 2006-12-13 2008-07-23 Infineum International Limited Fuel oil compositions
US20080182768A1 (en) * 2007-01-31 2008-07-31 Devlin Cathy C Lubricant composition for bio-diesel fuel engine applications
EP1959003A2 (en) 2007-02-08 2008-08-20 Infineum International Limited Soot dispersants and lubricating oil compositions containing same
EP1970430A2 (en) 2007-03-09 2008-09-17 Afton Chemical Corporation Fuel composition containing a hydrocarbyl-substituted succinimide
US20080241095A1 (en) * 2007-03-26 2008-10-02 Syrinek Allen R Antifoulant for hydrocarbon processing equipment
US20080274921A1 (en) * 2007-05-04 2008-11-06 Ian Macpherson Environmentally-Friendly Lubricant Compositions
US20080289249A1 (en) * 2007-05-22 2008-11-27 Peter Wangqi Hou Fuel additive to control deposit formation
EP2000523A1 (en) 2007-05-30 2008-12-10 Chevron Oronite S.A. Lubricating oil with enhanced protection against wear and corrosion
WO2008154334A1 (en) 2007-06-08 2008-12-18 Infineum International Limited Additives and lubricating oil compositions containing same
EP2009082A2 (en) 2007-06-20 2008-12-31 Chevron Oronite Company LLC Synergistic lubricating oil composition containing a mixture of a nitro-substituted diarylamine and a diarylamine
US20090029888A1 (en) * 2005-07-12 2009-01-29 Ramanathan Ravichandran Amine tungstates and lubricant compositions
US20090031614A1 (en) * 2007-08-01 2009-02-05 Ian Macpherson Environmentally-Friendly Fuel Compositions
EP2025737A1 (en) 2007-08-01 2009-02-18 Afton Chemical Corporation Environmentally-friendly fuel compositions
US20090071067A1 (en) * 2007-09-17 2009-03-19 Ian Macpherson Environmentally-Friendly Additives And Additive Compositions For Solid Fuels
EP2042582A2 (en) 2007-09-24 2009-04-01 Afton Chemical Corporation Surface passivation and to methods for the reduction of fuel thermal degradation deposits
US20090093384A1 (en) * 2007-10-03 2009-04-09 The Lubrizol Corporation Lubricants That Decrease Micropitting for Industrial Gears
US20090156445A1 (en) * 2007-12-13 2009-06-18 Lam William Y Lubricant composition suitable for engines fueled by alternate fuels
EP2075264A1 (en) 2007-12-26 2009-07-01 Infineum International Limited Method of forming polyalkene substituted carboxylic acid compositions
EP2077315A1 (en) 2007-12-20 2009-07-08 Chevron Oronite Company LLC Lubricating oil compositions containing a tetraalkyl-napthalene-1,8 diamine antioxidant
EP2078745A1 (en) 2007-12-20 2009-07-15 Chevron Oronite Company LLC Lubricating oil compositions comprising a molybdenum compound and a zinc dialkyldithiophosphate
EP2083024A1 (en) 2008-01-24 2009-07-29 Afton Chemical Corporation Olefin copolymer dispersant VI improver and lubricant compositions and uses thereof
EP2083063A1 (en) 2008-01-22 2009-07-29 Infineum International Limited Lubricating oil composition
EP2090642A1 (en) 2008-02-08 2009-08-19 Infineum International Limited Engine lubrication
US7581558B2 (en) 2001-08-24 2009-09-01 Cummins Filtration Ip Inc. Controlled release of additives in fluid systems
US20090233822A1 (en) * 2008-03-11 2009-09-17 Afton Chemical Corporation Ultra-low sulfur clutch-only transmission fluids
DE102009001301A1 (en) 2008-03-11 2009-09-24 Volkswagen Ag Method for lubricating a component only for the clutch of an automatic transmission, which requires lubrication
WO2009119831A1 (en) 2008-03-28 2009-10-01 富士フイルム株式会社 Composition and method for forming coating film
DE102009012567A1 (en) 2008-03-11 2009-10-01 Afton Chemical Corp. Clutch-only transmission fluid useful for lubrication comprises oil formulated with additive components having metal detergent, phosphorus-based wear preventative, phosphorylated and boronated dispersant, sulfurized extreme pressure agent
EP2107102A2 (en) 2008-04-04 2009-10-07 Afton Chemical Corporation A succinimide lubricity additive for diesel fuel
US20090270531A1 (en) * 2008-04-25 2009-10-29 Chevron Oronite Company Llc Lubricating oil additive composition and method of making the same
EP2116590A1 (en) 2005-02-18 2009-11-11 Infineum International Limited Soot dispersants and lubricating oil compositions containing same
EP2133406A1 (en) * 2008-06-09 2009-12-16 Idemitsu Kosan Co., Ltd. Lubricating oil composition for internal combustion engine
WO2010005947A2 (en) 2008-07-11 2010-01-14 Innospec Fuel Specialties, LLC Fuel composition with enhanced low temperature properties
DE202009013309U1 (en) 2009-10-05 2010-03-04 Afton Chemical Corp. Fuel and fuel compositions
JP2010047747A (en) * 2008-07-22 2010-03-04 Sanyo Chem Ind Ltd Lubricant additive and lubricant composition
US20100075876A1 (en) * 2008-09-24 2010-03-25 David John Claydon Fuel compositions
EP2169034A2 (en) 2009-10-05 2010-03-31 Afton Chemical Corporation Fuel compositions
US20100081588A1 (en) * 2008-09-30 2010-04-01 Chevron Oronite Company Llc Lubricating oil compositions
US20100081594A1 (en) * 2008-09-30 2010-04-01 Chevron Oronite Company Llc Lubricating oil additive composition and method of making the same
EP2199377A1 (en) 2008-12-22 2010-06-23 Infineum International Limited Additives for fuel oils
US20100160193A1 (en) * 2008-12-22 2010-06-24 Chevron Oronite LLC Additive composition and method of making the same
US20100160194A1 (en) * 2008-12-22 2010-06-24 Chevron Oronite LLC Post-treated additive composition and method of making the same
US20100160192A1 (en) * 2008-12-22 2010-06-24 Chevron Oronite LLC lubricating oil additive composition and method of making the same
US20100206260A1 (en) * 2009-02-18 2010-08-19 Chevron Oronite Company Llc Method for preventing exhaust valve seat recession
WO2010104738A1 (en) 2009-03-12 2010-09-16 Nalco Company An improved process for reacting an a, b-unsaturated dicarboxylic acid compound with an ethylenically unsaturated hydrocarbon
EP2236590A1 (en) 2009-04-01 2010-10-06 Infineum International Limited Lubricating oil composition
US20100258070A1 (en) * 2007-09-27 2010-10-14 Innospec Limited Fuel compositions
WO2010115594A1 (en) 2009-04-07 2010-10-14 Infineum International Limited Marine engine lubrication
US7833953B2 (en) 2006-08-28 2010-11-16 Afton Chemical Corporation Lubricant composition
US20100293844A1 (en) * 2007-09-27 2010-11-25 Macmillan John Alexander Additives for Diesel Engines
US20100299992A1 (en) * 2007-09-27 2010-12-02 Jacqueline Reid Fuel compositions
WO2010136822A2 (en) 2009-05-29 2010-12-02 Innospec Limited Method and use
WO2010139994A1 (en) 2009-06-01 2010-12-09 Innospec Limited Improvements in efficiency
WO2010147993A1 (en) 2009-06-16 2010-12-23 Chevron Phillips Chemical Company Lp Oligomerization of alpha olefins using metallocene-ssa catalyst systems and use of the resultant polyalphaolefins to prepare lubricant blends
EP2272940A1 (en) 2001-09-14 2011-01-12 Afton Chemical Intangibles LLC Fuels compositions for direct injection gasoline engines
US7879775B2 (en) 2006-07-14 2011-02-01 Afton Chemical Corporation Lubricant compositions
US7883638B2 (en) 2008-05-27 2011-02-08 Dober Chemical Corporation Controlled release cooling additive compositions
US20110039994A1 (en) * 2009-07-01 2011-02-17 Xiaorong Wang Multiple-Acid-Derived Metal Soaps Incorporated In Rubber Compositions And Method For Incorporating Such Soaps In Rubber Compositions
EP2290041A2 (en) 2009-08-24 2011-03-02 Infineum International Limited A lubricating oil composition
EP2290040A1 (en) 2009-07-31 2011-03-02 Chevron Japan Ltd. Friction modifier and transmission oil
US20110060062A1 (en) * 2009-09-10 2011-03-10 Bridgestone Corporation Compositions and method for making hollow nanoparticles from metal soaps
EP2302020A1 (en) 2007-07-28 2011-03-30 Innospec Limited Use of additives for improving oxidation stability of a fuel oil composition
US20110098378A1 (en) * 2008-06-26 2011-04-28 Xiaorong Wang Rubber compositions including metal-functionalized polyisobutylene derivatives and methods for preparing such compositions
US20110105371A1 (en) * 2009-11-05 2011-05-05 Afton Chemical Corporation Olefin copolymer vi improvers and lubricant compositions and uses thereof
US7938277B2 (en) 2001-08-24 2011-05-10 Dober Chemical Corporation Controlled release of microbiocides
US20110118160A1 (en) * 2009-11-18 2011-05-19 Chevron Oronite Company Llc Alkylated hydroxyaromatic compound substantially free of endocrine disruptive chemicals
WO2011059626A1 (en) 2009-11-10 2011-05-19 The Lubrizol Corporation Lubricant system clean-up compositions and methods thereof
US20110143979A1 (en) * 2009-12-15 2011-06-16 Chevron Oronite Company Llc Lubricating oil compositions
US20110143980A1 (en) * 2009-12-15 2011-06-16 Chevron Oronite Company Llc Lubricating oil compositions containing titanium complexes
EP2363444A1 (en) 2006-06-15 2011-09-07 Dow Global Technologies LLC Functionalized olefin interpolymers, compositions and articles prepared therefrom, and methods for making the same
WO2011110860A1 (en) 2010-03-10 2011-09-15 Innospec Limited Fuel composition comprising detergent and quaternary ammonium salt additive
EP2371933A1 (en) 2006-02-06 2011-10-05 The Lubrizol Corporation Tartaric acid derivatives as fuel economy improvers and antiwear agents in crankcase oils and preparation thereof
WO2011126641A2 (en) 2010-03-31 2011-10-13 Chevron Oronite Company Llc Method for improving copper corrosion performance
WO2011126642A2 (en) 2010-03-31 2011-10-13 Chevron Oronite Company Llc Method for improving copper corrosion performance
WO2011141731A1 (en) 2010-05-10 2011-11-17 Innospec Limited Composition, method and use
WO2011143051A1 (en) 2010-05-12 2011-11-17 The Lubrizol Corporation Tartaric acid derivatives in hths fluids
WO2011146289A1 (en) 2010-05-18 2011-11-24 The Lubrizol Corporation Methods and compositions that provide detergency
WO2011149799A1 (en) 2010-05-25 2011-12-01 The Lubrizol Corporation Method to provide power gain in an engine
WO2011159742A1 (en) 2010-06-15 2011-12-22 The Lubrizol Corporation Methods of removing deposits in oil and gas applications
EP2402421A2 (en) 2010-06-29 2012-01-04 Chevron Oronite Technology B.V. Trunk Piston Engine Lubricating Oil Compositions
WO2012033668A1 (en) 2010-09-07 2012-03-15 The Lubrizol Corporation Hydroxychroman derivatives as engine oil antioxidants
WO2012051075A2 (en) 2010-10-12 2012-04-19 Chevron Oronite Company Llc Lubricating composition containing multifunctional borated hydroxylated amine salt of a hindered phenolic acid
WO2012051064A2 (en) 2010-10-12 2012-04-19 Chevron Oronite Company Llc Lubricating composition containing multifunctional hydroxylated amine salt of a hindered phenolic acid
WO2012076896A1 (en) 2010-12-09 2012-06-14 Innospec Limited Improvements in or relating to additives for fuels and lubricants
WO2012084906A1 (en) 2010-12-22 2012-06-28 Rhodia Operations Fuel additive composition containing a dispersion of iron particles and a detergent
EP2479245A1 (en) 2011-01-19 2012-07-25 Afton Chemical Corporation Fuel additives and gasoline containing the additives
WO2012099736A2 (en) 2011-01-21 2012-07-26 Chevron Oronite Company Llc Improved process for preparation of high molecular weight molybdenum succinimide complexes
WO2012099734A2 (en) 2011-01-21 2012-07-26 Chevron Oronite Company Llc Improved process for preparation of low molecular weight molybdenum succinimide complexes
US8299003B2 (en) 2005-11-09 2012-10-30 Afton Chemical Corporation Composition comprising a sulfur-containing, phosphorus-containing compound, and/or its salt, and uses thereof
WO2012162282A1 (en) 2011-05-26 2012-11-29 The Lubrizol Corporation Stabilized blends containing friction modifiers
WO2012162027A1 (en) 2011-05-26 2012-11-29 The Lubrizol Corporation Stabilized blends containing friction modifiers
WO2012162020A1 (en) 2011-05-26 2012-11-29 The Lubrizol Corporation Stabilized blends containing antioxidants
WO2012162219A1 (en) 2011-05-26 2012-11-29 The Lubrizol Corporation Stabilized blends containing friction modifiers
WO2012177529A1 (en) 2011-06-21 2012-12-27 The Lubrizol Corporation Lubricating compositions containing salts of hydrocarbyl substituted acylating agents
WO2013003394A1 (en) 2011-06-30 2013-01-03 Exxonmobil Research And Engineering Company Lubricating compositions containing polyetheramines
WO2013003405A1 (en) 2011-06-30 2013-01-03 Exxonmobil Research And Engineering Company Lubricating compositions containing polyalkylene glycol mono ethers
WO2013003392A1 (en) 2011-06-30 2013-01-03 Exxonmobil Research And Engineering Company Method of improving pour point of lubricating compositions containing polyalkylene glycol mono ethers
WO2013003406A1 (en) 2011-06-29 2013-01-03 Exxonmobil Research And Engineering Company Low viscosity engine oil with superior engine wear protection
WO2013043332A1 (en) 2011-09-23 2013-03-28 The Lubrizol Corporation Quaternary ammonium salts in heating oils
WO2013055480A1 (en) 2011-10-10 2013-04-18 Exxonmobil Research And Engineering Company Low viscosity engine oil compositions
US8425772B2 (en) 2006-12-12 2013-04-23 Cummins Filtration Ip, Inc. Filtration device with releasable additive
WO2013066915A1 (en) 2011-11-01 2013-05-10 Exxonmobil Research And Engineering Company Lubricants with improved low-temperature fuel economy
WO2013074498A1 (en) 2011-11-14 2013-05-23 Exxonmobil Research And Engineering Company Method for improving engine fuel efficiency
EP2604676A1 (en) 2011-12-16 2013-06-19 Chevron Oronite Technology B.V. Trunk piston engine lubricating oil compositions
WO2013096532A1 (en) 2011-12-22 2013-06-27 Exxonmobil Research And Engineering Company Method for improving engine fuel efficiency
WO2013123160A1 (en) 2012-02-17 2013-08-22 The Lubrizol Corporation Mixtures of olefin-ester copolymer with polyolefin as viscosity modifier
WO2013123102A2 (en) 2012-02-17 2013-08-22 The Lubrizol Corporation Lubricating composition including esterified copolymer and low dispersant levels suitable for driveline applications
EP2644684A1 (en) 2009-02-25 2013-10-02 Innospec Limited Methods and uses relating to fuel compositions
US8557752B2 (en) 2005-03-23 2013-10-15 Afton Chemical Corporation Lubricating compositions
US8586520B2 (en) 2011-06-30 2013-11-19 Exxonmobil Research And Engineering Company Method of improving pour point of lubricating compositions containing polyalkylene glycol mono ethers
US8591747B2 (en) 2008-05-27 2013-11-26 Dober Chemical Corp. Devices and methods for controlled release of additive compositions
WO2013181318A1 (en) 2012-06-01 2013-12-05 Exxonmobil Research And Engineering Company Lubricant compostions and processes for preparing same
WO2014008121A1 (en) 2012-07-02 2014-01-09 Exxonmobil Research And Engineering Company Enhanced durability performance of lubricants using functionalized metal phosphate nanoplatelets
WO2014047017A1 (en) 2012-09-24 2014-03-27 The Lubrizol Corporation Lubricant comprising a mixture of an olefin-ester copolymer with an ethylene alpha-olefin copolymer
US8702995B2 (en) 2008-05-27 2014-04-22 Dober Chemical Corp. Controlled release of microbiocides
US8703680B2 (en) 2010-11-24 2014-04-22 Chevron Oronite Company Llc Lubricating composition containing friction modifier blend
US8702968B2 (en) 2011-04-05 2014-04-22 Chevron Oronite Technology B.V. Low viscosity marine cylinder lubricating oil compositions
WO2014066344A1 (en) 2012-10-23 2014-05-01 The Lubrizol Corporation Diesel detergent without a low molecular weight penalty
WO2014066444A1 (en) 2012-10-24 2014-05-01 Exxonmobil Research And Engineering Comapny Functionalized polymers and oligomers as corrosion inhibitors and antiwear additives
US8716202B2 (en) 2010-12-14 2014-05-06 Chevron Oronite Company Llc Method for improving fluorocarbon elastomer seal compatibility
EP2727984A1 (en) 2012-11-02 2014-05-07 Infineum International Limited Marine engine lubrication
EP2735603A1 (en) 2012-11-21 2014-05-28 Infineum International Limited Marine engine lubrication
WO2014107315A1 (en) 2013-01-04 2014-07-10 Exxonmobil Research And Engineering Company Method for improving engine fuel efficiency
US8796192B2 (en) 2010-10-29 2014-08-05 Chevron Oronite Company Llc Natural gas engine lubricating oil compositions
US8802755B2 (en) 2011-01-18 2014-08-12 Bridgestone Corporation Rubber compositions including metal phosphate esters
EP2765179A1 (en) 2013-02-07 2014-08-13 Infineum International Limited Marine engine lubrication
WO2014137800A1 (en) 2013-03-07 2014-09-12 The Lubrizol Corporation Ion tolerant corrosion inhibitors and inhibitor combinations for fuels
US8841243B2 (en) 2010-03-31 2014-09-23 Chevron Oronite Company Llc Natural gas engine lubricating oil compositions
WO2014158533A1 (en) 2013-03-14 2014-10-02 Exxonmobil Research And Engineering Company Lubricating composition providing high wear resistance
WO2014193692A1 (en) 2013-05-28 2014-12-04 The Lubrizol Corporation Asphaltene inhibition
US8933002B2 (en) 2011-11-10 2015-01-13 Chevron Oronite Company Llc Lubricating oil compositions
US8933001B2 (en) 2010-03-31 2015-01-13 Chevron Oronite Company Llc Method for improving fluorocarbon elastomer seal compatibility
US8969273B2 (en) 2009-02-18 2015-03-03 Chevron Oronite Company Llc Lubricating oil compositions
EP2851413A1 (en) 2013-09-23 2015-03-25 Chevron Japan Ltd. Fuel economy engine oil composition
EP2851412A1 (en) 2013-09-24 2015-03-25 Infineum International Limited Marine engine lubrication
US8993496B2 (en) 2010-03-31 2015-03-31 Chevron Oronite Company Llc Method for improving fluorocarbon elastomer seal compatibility
WO2015050690A1 (en) 2013-10-03 2015-04-09 Exxonmobil Research And Engineering Company Compositions with improved varnish control properties
WO2015073296A2 (en) 2013-11-18 2015-05-21 Russo Joseph M Mixed detergent composition for intake valve deposit control
US9062271B2 (en) 2013-10-30 2015-06-23 Chevron Oronite Technology B.V. Process for preparing an overbased salt of a sulfurized alkyl-substituted hydroxyaromatic composition
WO2015095336A1 (en) 2013-12-18 2015-06-25 Chevron Phillips Chemical Company Lp Method for making polyolefins using aluminum halide catalyzed oligomerization of olefins
WO2015099907A1 (en) 2013-12-23 2015-07-02 Exxonmobil Research And Engineering Company Low viscosity ester lubricant and method for using
WO2015099820A1 (en) 2013-12-23 2015-07-02 Exxonmobil Research And Engineering Company Method for improving engine fuel efficiency
WO2015099819A1 (en) 2013-12-23 2015-07-02 Exxonmobil Research And Engineering Company Method for improving engine fuel efficiency
WO2015099821A1 (en) 2013-12-23 2015-07-02 Exxonmobil Research And Engineering Company Method for improving engine fuel efficiency
US9090127B2 (en) 2007-12-31 2015-07-28 Bridgestone Corporation Metal soaps incorporated in rubber compositions and method for incorporating such soaps in rubber compositions
EP2913387A1 (en) 2009-09-02 2015-09-02 Chevron Oronite Company LLC Natural gas engine lubricating oil compositions
WO2015134129A2 (en) 2014-03-05 2015-09-11 The Lubrizol Corporation Emulsifier components and methods of using the same
US9149814B2 (en) 2013-03-13 2015-10-06 Ecolab Usa Inc. Composition and method for improvement in froth flotation
EP2940110A1 (en) 2014-04-29 2015-11-04 Infineum International Limited Lubricating oil compositions
WO2015171978A1 (en) 2014-05-09 2015-11-12 Exxonmobil Research And Engineering Company Method for preventing or reducing low speed pre-ignition
WO2015171980A1 (en) 2014-05-09 2015-11-12 Exxonmobil Research And Engineering Company Method for preventing or reducing low speed pre-ignition
WO2015171981A1 (en) 2014-05-09 2015-11-12 Exxonmobil Research And Engineering Company Method for preventing or reducing low speed pre-ignition
WO2015171292A1 (en) 2014-05-08 2015-11-12 Exxonmobil Research And Engineering Company Method for preventing or reducing engine knock and pre-ignition
WO2015184301A2 (en) 2014-05-30 2015-12-03 The Lubrizol Corporation Coupled quaternary ammonium salts
WO2015183455A1 (en) 2014-05-29 2015-12-03 Exxonmobil Research And Engineering Company Lubricating oil compositions with engine wear protection
WO2015184247A1 (en) 2014-05-30 2015-12-03 The Lubrizol Corporation High molecular weight imide containing quaternary ammonium salts
WO2015184276A1 (en) 2014-05-30 2015-12-03 The Lubrizol Corporation Epoxide quaternized quaternary ammonium salts
WO2015183916A1 (en) 2014-05-30 2015-12-03 The Lubrizol Corporation Low molecular weight amide/ester containing quaternary ammonium salts
WO2015184251A1 (en) 2014-05-30 2015-12-03 The Lubrizol Corporation Branched amine containing quaternary ammonium salts
WO2015183908A1 (en) 2014-05-30 2015-12-03 The Lubrizol Corporation Low molecular weight imide containing quaternary ammonium salts
WO2015184280A1 (en) 2014-05-30 2015-12-03 The Lubrizol Corporation Imidazole containing quaternary ammonium salts
WO2015184254A1 (en) 2014-05-30 2015-12-03 The Lubrizol Corporation High molecular weight amide/ester containing quaternary ammonium salts
US9243199B2 (en) 2007-09-27 2016-01-26 Innospec Limited Fuel compositions
US9249091B2 (en) 2011-12-27 2016-02-02 Chevron Oronite Company Llc Post-treated sulfurized salt of an alkyl-substituted hydroxyaromatic composition
WO2016018462A1 (en) 2014-07-31 2016-02-04 Chevron U.S.A. Inc. Sae 15w-30 lubricating oil composition having improved oxidative stability
EP2998384A1 (en) 2005-06-16 2016-03-23 The Lubrizol Corporation Diesel fuel composition comprising a quaternary ammonium salt detergent
WO2016043944A1 (en) 2014-09-17 2016-03-24 Exxonmobil Research And Engineering Company Composition and method for preventing or reducing engine knock and pre-ignition in high compression spark ignition engines
US9315752B2 (en) 2007-09-27 2016-04-19 Innospec Limited Fuel compositions
WO2016073149A1 (en) 2014-11-03 2016-05-12 Exxonmobil Research And Engineering Company Low transition temperature mixtures or deep eutectic solvents and processes for preparation thereof
EP3020790A1 (en) 2014-11-14 2016-05-18 Chevron Oronite Technology B.V. Trunk piston engine oil composition for low sulfur marine distillate fueled engines
EP3029133A1 (en) 2014-12-04 2016-06-08 Infineum International Limited Marine engine lubrication
WO2016106214A1 (en) 2014-12-24 2016-06-30 Exxonmobil Research And Engineering Company Methods for determining condition and quality of petroleum products
WO2016106211A1 (en) 2014-12-24 2016-06-30 Exxonmobil Research And Engineering Company Methods for authentication and identification of petroleum products
WO2016109322A1 (en) 2014-12-30 2016-07-07 Exxonmobil Research And Engineering Company Lubricating oil compositions containing encapsulated microscale particles
WO2016109382A1 (en) 2014-12-30 2016-07-07 Exxonmobil Research And Engineering Company Lubricating oil compositions with engine wear protection
WO2016109376A1 (en) 2014-12-30 2016-07-07 Exxonmobil Research And Engineering Company Lubricating oil compositions with engine wear protection
US9434906B2 (en) 2013-03-25 2016-09-06 Chevron Oronite Company, Llc Marine diesel engine lubricating oil compositions
WO2016140998A1 (en) 2015-03-04 2016-09-09 Huntsman Petrochemical Llc Novel organic friction modifiers
EP3072948A1 (en) 2015-03-23 2016-09-28 Chevron Japan Ltd. Lubricating oil compositions for construction machines
EP3072949A1 (en) 2015-03-23 2016-09-28 Chevron Japan Ltd. Lubricating oil composition for construction machines
US9481841B2 (en) 2004-12-09 2016-11-01 The Lubrizol Corporation Process of preparation of an additive and its use
US9506008B2 (en) 2013-12-23 2016-11-29 Exxonmobil Research And Engineering Company Method for improving engine fuel efficiency
WO2016191409A1 (en) 2015-05-28 2016-12-01 Exxonmobil Research And Engineering Company Composition and method for preventing or reducing engine knock and pre-ignition in high compression spark ignition engines
WO2016200606A1 (en) 2015-06-09 2016-12-15 Exxonmobil Research And Engineering Company Inverse micellar compositions containing lubricant additives
US9523057B2 (en) 2011-02-22 2016-12-20 Afton Chemical Corporation Fuel additives to maintain optimum injector performance
US9528071B2 (en) 2015-02-13 2016-12-27 Chevron Oronite Technology B.V. Lubricating oil compositions with enhanced piston cleanliness
US9528074B2 (en) 2015-02-13 2016-12-27 Chevron Oronite Technology B.V. Lubricating oil compositions with enhanced piston cleanliness
WO2017007670A1 (en) 2015-07-07 2017-01-12 Exxonmobil Research And Engineering Company Composition and method for preventing or reducing engine knock and pre-ignition in high compression spark ignition engines
WO2017013257A1 (en) 2015-07-22 2017-01-26 Chevron Oronite Technology B.V. Marine diesel cylinder lubricant oil compositions
EP3127992A1 (en) 2008-10-10 2017-02-08 The Lubrizol Corporation Additives to reduce metal pick-up in fuels
EP3135750A1 (en) 2015-08-26 2017-03-01 Infineum International Limited Lubricating oil compositions
WO2017079123A1 (en) 2015-11-02 2017-05-11 Lubrizol Oilfield Solutions, Inc. Lubricant for water based drilling fluid
WO2017083042A1 (en) 2015-11-09 2017-05-18 The Lubrizol Corporation Using quaternary amine additives to improve water separation
US9670341B2 (en) 2012-11-02 2017-06-06 Bridgestone Corporation Rubber compositions comprising metal carboxylates and processes for making the same
WO2017096175A1 (en) 2015-12-02 2017-06-08 The Lubrizol Corporation Ultra-low molecular weight imide containing quaternary ammonium salts having short hydrocarbon tails
WO2017096159A1 (en) 2015-12-02 2017-06-08 The Lubrizol Corporation Ultra-low molecular weight amide/ester containing quaternary ammonium salts having short hydrocarbon tails
WO2017117178A1 (en) 2015-12-28 2017-07-06 Exxonmobil Research And Engineering Company Bright stock production from deasphalted oil
US9732300B2 (en) 2015-07-23 2017-08-15 Chevron Phillipa Chemical Company LP Liquid propylene oligomers and methods of making same
WO2017146897A1 (en) 2016-02-26 2017-08-31 Exxonmobil Research And Engineering Company Lubricant compositions containing controlled release additives
WO2017146896A1 (en) 2016-02-26 2017-08-31 Exxonmobil Research And Engineering Company Lubricant compositions containing controlled release additives
WO2017172254A1 (en) 2016-03-31 2017-10-05 Exxonmobil Research And Engineering Company Lubricant compositions
WO2017223306A1 (en) 2016-06-22 2017-12-28 Lubrizol Oilfield Solutions, Inc. Gas hydrate inhibitors
WO2018013249A1 (en) 2016-07-12 2018-01-18 Chevron Phillips Chemical Company Lp Decene oligomers
WO2018013181A1 (en) 2016-07-13 2018-01-18 Chevron Oronite Company Llc Synergistic lubricating oil composition containing mixture of antioxidants
US9879202B2 (en) 2014-12-04 2018-01-30 Infineum International Limited Marine engine lubrication
US9885004B2 (en) 2013-12-23 2018-02-06 Exxonmobil Research And Engineering Company Method for improving engine fuel efficiency
WO2018027227A1 (en) 2016-08-05 2018-02-08 Rutgers, The State University Of New Jersey Thermocleavable friction modifiers and methods thereof
WO2018026982A1 (en) 2016-08-03 2018-02-08 Exxonmobil Research And Engineering Company Lubricating engine oil for improved wear protection and fuel efficiency
WO2018039571A1 (en) 2016-08-25 2018-03-01 Evonik Degussa Gmbh Amine alkenyl substituted succinimide reaction product fuel additives, compositions, and methods
US9909079B2 (en) 2013-10-18 2018-03-06 Chevron Oronite Company Llc Lubricating oil composition for protection of silver bearings in medium speed diesel engines
WO2018041732A1 (en) 2016-08-29 2018-03-08 Chevron Oronite Technology B.V. Marine diesel cylinder lubricant oil compositions
WO2018048781A1 (en) 2016-09-12 2018-03-15 The Lubrizol Corporation Total base number boosters for marine diesel engine lubricating compositions
US9926509B2 (en) 2015-01-19 2018-03-27 Exxonmobil Research And Engineering Company Lubricating oil compositions with engine wear protection and solubility
WO2018057377A1 (en) 2016-09-20 2018-03-29 Exxonmobil Research And Engineering Company Non-newtonian engine oil with superior engine wear protection and fuel economy
WO2018067905A1 (en) 2016-10-07 2018-04-12 Exxonmobil Research And Engineering Company Method for preventing or minimizing electrostatic discharge and dielectric breakdown in electric vehicle powertrains
WO2018067903A1 (en) 2016-10-07 2018-04-12 Exxonmobil Research And Engineering Company Method for controlling electrical conductivity of lubricating oils in electric vehicle powertrains
WO2018067902A1 (en) 2016-10-07 2018-04-12 Exxonmobil Research And Engineering Company Lubricating oil compositions for electric vehicle powertrains
WO2018069460A1 (en) 2016-10-12 2018-04-19 Chevron Oronite Technology B.V. Marine diesel lubricant oil compositions
WO2018073268A1 (en) 2016-10-18 2018-04-26 Chevron Oronite Technology B.V. Marine diesel lubricant oil compositions
WO2018075147A1 (en) 2016-10-17 2018-04-26 The Lubrizol Corporation Acid emulsifier technology for continuous mixed emulsified acid systems
WO2018077621A1 (en) 2016-10-25 2018-05-03 Chevron Oronite Technology B.V. Lubricating oil compositions comprising a biodiesel fuel and a dispersant
WO2018101282A1 (en) 2016-11-30 2018-06-07 Chevron Japan Ltd. Lubricating oil compositions for motorcycles
EP3339404A1 (en) 2006-07-18 2018-06-27 Infineum International Limited Lubricating oil compositions
WO2018118477A1 (en) 2016-12-19 2018-06-28 Exxonmobil Research And Engineering Company Composition and method for preventing or reducing engine knock and pre-ignition compression spark ignition engines
WO2018125956A1 (en) 2016-12-30 2018-07-05 Exxonmobil Research And Engineering Company Low viscosity lubricating oil compositions for turbomachines
WO2018144167A1 (en) 2017-02-01 2018-08-09 Exxonmobil Research And Engineering Company Lubricating engine oil and method for improving engine fuel efficiency
WO2018156304A1 (en) 2017-02-21 2018-08-30 Exxonmobil Research And Engineering Company Lubricating oil compositions and methods of use thereof
EP3369802A1 (en) 2017-03-01 2018-09-05 Infineum International Limited Improvements in and relating to lubricating compositions
EP3375848A1 (en) 2017-03-13 2018-09-19 Afton Chemical Corporation Polyol carrier fluids and fuel compositions including polyol carrier fluids
WO2018170110A1 (en) 2017-03-16 2018-09-20 Chevron Phillips Chemical Company Lp Lubricant compositions containing hexene-based oligomers
WO2018175830A1 (en) 2017-03-24 2018-09-27 Exxonmobil Research And Engineering Company Method for improving engine fuel efficiency and energy efficiency
EP3381998A1 (en) 2009-05-15 2018-10-03 The Lubrizol Corporation Quaternary ammonium ester salts
WO2018197312A1 (en) 2017-04-27 2018-11-01 Shell Internationale Research Maatschappij B.V. Lubricating composition
WO2018211466A1 (en) 2017-05-19 2018-11-22 Chevron Oronite Company Llc Dispersants, method of making, and using same
US10138438B2 (en) 2015-02-18 2018-11-27 Chevron Oronite Technology B.V. Low sulfur marine distillate fuel trunk piston engine oil composition
EP3421576A1 (en) 2017-06-30 2019-01-02 Infineum International Limited Refinery antifoulant process
WO2019003176A1 (en) 2017-06-30 2019-01-03 Chevron Oronite Company Llc Lubricating oil magnesium detergents and method of making and using same
WO2019003177A1 (en) 2017-06-30 2019-01-03 Chevron Oronite Company Llc Lubricating engine oil compositions containing detergent compounds
WO2019012447A1 (en) 2017-07-14 2019-01-17 Chevron Oronite Company Llc Lubricating oil compositions containing zirconium and method for preventing or reducing low speed pre-ignition in direct injected spark-ignited engines
WO2019014092A1 (en) 2017-07-13 2019-01-17 Exxonmobil Research And Engineering Company Continuous process for the manufacture of grease
WO2019012450A1 (en) 2017-07-14 2019-01-17 Chevron Oronite Company Llc Lubricating oil compositions containing non-sulfur-phosphorus containing zinc compounds and method for preventing or reducing low speed pre-ignition in direct injected spark-ignited engines
WO2019018145A1 (en) 2017-07-21 2019-01-24 Exxonmobil Research And Engineering Company Method for improving deposit control and cleanliness performance in an engine lubricated with a lubricating oil
US10190072B2 (en) 2013-12-23 2019-01-29 Exxonmobil Research And Engineering Company Method for improving engine fuel efficiency
WO2019028310A1 (en) 2017-08-04 2019-02-07 Exxonmobil Research And Engineering Company Novel formulation for lubrication of hyper compressors providing improved pumpability under high-pressure conditions
WO2019055291A1 (en) 2017-09-18 2019-03-21 Exxonmobil Research And Engineering Company Hydraulic oil compositions with improved hydrolytic and thermo-oxidative stability
WO2019053635A1 (en) 2017-09-13 2019-03-21 Chevron U.S.A. Inc. Method for preventing or reducing low speed pre-ignition in direct injected spark-ignited engines with cobalt-containing lubricant
WO2019060144A1 (en) 2017-09-22 2019-03-28 Exxonmobil Research And Engineering Company Lubricating oil compositions with viscosity and deposit control
EP3461877A1 (en) 2017-09-27 2019-04-03 Infineum International Limited Improvements in and relating to lubricating compositions
WO2019069197A1 (en) 2017-10-06 2019-04-11 Chevron Japan Ltd. Passenger car lubricating oil compositions for fuel economy
WO2019077462A1 (en) 2017-10-20 2019-04-25 Chevron Japan Ltd. Low viscosity lubricating oil composition
WO2019089177A1 (en) 2017-10-30 2019-05-09 Exxonmobil Research And Engineering Company Lubricating oil compositions with engine wear protection
WO2019090038A1 (en) 2017-11-03 2019-05-09 Exxonmobil Research And Engineering Company Lubricant compositions with improved performance and methods of preparing and using the same
WO2019094019A1 (en) 2017-11-09 2019-05-16 Exxonmobil Research And Engineering Company Method for preventing or reducing low speed pre-ignition while maintaining or improving cleanliness
WO2019103808A1 (en) 2017-11-22 2019-05-31 Exxonmobil Research And Engineering Company Lubricating oil compositions with oxidative stability in diesel engines
US10308593B2 (en) 2009-03-18 2019-06-04 Infineum International Limited Additives for fuel oils
WO2019108723A1 (en) 2017-11-30 2019-06-06 The Lubrizol Corporation Hindered amine terminated succinimide dispersants and lubricating compositions containing same
US10316712B2 (en) 2015-12-18 2019-06-11 Exxonmobil Research And Engineering Company Lubricant compositions for surface finishing of materials
EP3495462A1 (en) 2017-12-11 2019-06-12 Infineum International Limited Low ash and ash-free acid neutralizing compositions and lubricating oil compositions containing same
WO2019112711A1 (en) 2017-12-04 2019-06-13 Exxonmobil Research And Enginerring Company Method for preventing or reducing low speed pre-ignition
WO2019118115A1 (en) 2017-12-15 2019-06-20 Exxonmobil Research And Engineering Company Lubricating oil compositions containing microencapsulated additives
WO2019133409A1 (en) 2017-12-28 2019-07-04 Exxonmobil Research And Engineering Company Friction and wear reduction using liquid crystal base stocks
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WO2019133218A1 (en) 2017-12-29 2019-07-04 Exxonmobil Research And Engineering Company Lubricating oil compositions with wear and sludge control
WO2019133191A1 (en) 2017-12-29 2019-07-04 Exxonmobil Research And Engineering Company Lubrication of oxygenated diamond-like carbon surfaces
WO2019142059A1 (en) 2018-01-19 2019-07-25 Chevron Oronite Company Llc Ultra low ash lubricating oil compositions
US10364403B2 (en) 2013-11-06 2019-07-30 Chevron Oronite Technology B.V. Marine diesel cylinder lubricant oil compositions
US10364404B2 (en) 2014-12-04 2019-07-30 Infineum International Limited Marine engine lubrication
WO2019162744A1 (en) 2018-02-22 2019-08-29 Chevron Japan Ltd. Lubricating oils for automatic transmissions
WO2019166977A1 (en) 2018-03-02 2019-09-06 Chevron Oronite Technology B.V. Lubricating oil composition providing wear protection at low viscosity
US10435491B2 (en) 2015-08-19 2019-10-08 Chevron Phillips Chemical Company Lp Method for making polyalphaolefins using ionic liquid catalyzed oligomerization of olefins
US10450525B2 (en) 2014-08-27 2019-10-22 Chevron Oronite Company Llc Process for alaknolamide synthesis
US10457887B2 (en) 2015-05-19 2019-10-29 Chevron Oronite Technology B.V. Trunk piston engine oil composition
WO2019217058A1 (en) 2018-05-11 2019-11-14 Exxonmobil Research And Engineering Company Method for improving engine fuel efficiency
WO2019224647A1 (en) 2018-05-25 2019-11-28 Chevron U.S.A. Inc. Method for preventing or reducing low speed pre-ignition in direct injected spark-ignited engines with manganese-containing lubricant
US10494579B2 (en) 2016-04-26 2019-12-03 Exxonmobil Research And Engineering Company Naphthene-containing distillate stream compositions and uses thereof
WO2019240965A1 (en) 2018-06-11 2019-12-19 Exxonmobil Research And Engineering Company Non-zinc-based antiwear compositions, hydraulic oil compositions, and methods of using the same
WO2019244020A1 (en) 2018-06-22 2019-12-26 Chevron Oronite Company Llc Lubricating oil compositions
US10519394B2 (en) 2014-05-09 2019-12-31 Exxonmobil Research And Engineering Company Method for preventing or reducing low speed pre-ignition while maintaining or improving cleanliness
EP1871861B1 (en) 2005-04-08 2020-01-15 The Lubrizol Corporation Additive system for lubricants
WO2020023437A1 (en) 2018-07-24 2020-01-30 Exxonmobil Research And Engineering Company Lubricating oil compositions with engine corrosion protection
WO2020023430A1 (en) 2018-07-23 2020-01-30 Exxonmobil Research And Engineering Company Lubricating oil compositions with oxidative stability in diesel engines using biodiesel fuel
US10550341B2 (en) 2015-12-28 2020-02-04 Exxonmobil Research And Engineering Company Sequential deasphalting for base stock production
US10550335B2 (en) 2015-12-28 2020-02-04 Exxonmobil Research And Engineering Company Fluxed deasphalter rock fuel oil blend component oils
EP3604484A1 (en) 2018-08-03 2020-02-05 Afton Chemical Corporation Lubricity additives for fuels
WO2020068439A1 (en) 2018-09-27 2020-04-02 Exxonmobil Research And Engineering Company Low viscosity lubricating oils with improved oxidative stability and traction performance
US10647936B2 (en) 2016-12-30 2020-05-12 Exxonmobil Research And Engineering Company Method for improving lubricant antifoaming performance and filterability
WO2020096804A1 (en) 2018-11-05 2020-05-14 Exxonmobil Research And Engineering Company Lubricating oil compositions having improved cleanliness and wear performance
WO2020100045A1 (en) 2018-11-16 2020-05-22 Chevron Japan Ltd. Low viscosity lubricating oil compositions
US10669506B2 (en) 2013-11-06 2020-06-02 Chevron Oronite Technology B.V. Marine diesel cylinder lubricant oil compositions
WO2020112338A1 (en) 2018-11-28 2020-06-04 Exxonmobil Research And Engineering Company Lubricating oil compositions with improved deposit resistance and methods thereof
WO2020123440A1 (en) 2018-12-10 2020-06-18 Exxonmobil Research And Engineering Company Method for improving oxidation and deposit resistance of lubricating oils
US10689593B2 (en) 2014-08-15 2020-06-23 Exxonmobil Research And Engineering Company Low viscosity lubricating oil compositions for turbomachines
WO2020131439A1 (en) 2018-12-19 2020-06-25 Exxonmobil Research And Engineering Company Grease compositions having polyurea thickeners made with isocyanate terminated prepolymers
WO2020131515A2 (en) 2018-12-19 2020-06-25 Exxonmobil Research And Engineering Company Lubricant compositions with improved wear control
WO2020131441A1 (en) 2018-12-19 2020-06-25 Exxonmobil Research And Engineering Company Grease compositions having improved performance
WO2020132164A1 (en) 2018-12-19 2020-06-25 Exxonmobil Research And Engineering Company Lubricating oil compositions with viscosity control
WO2020131310A1 (en) 2018-12-19 2020-06-25 Exxonmobil Research And Engineering Company Method for improving high temperature antifoaming performance of a lubricating oil
WO2020132166A1 (en) 2018-12-19 2020-06-25 Exxonmobil Research And Engineering Company Lubricating oil compositions with antioxidant formation and dissipation control
WO2020131440A1 (en) 2018-12-19 2020-06-25 Exxonmobil Research And Engineering Company Grease compositions having calcium sulfonate and polyurea thickeners
WO2020139333A1 (en) 2018-12-26 2020-07-02 Exxonmobil Research And Engineering Company Formulation approach to extend the high temperature performance of lithium complex greases
US10712105B1 (en) 2019-06-19 2020-07-14 Exxonmobil Research And Engineering Company Heat transfer fluids and methods of use
EP3680312A1 (en) 2019-01-11 2020-07-15 Afton Chemical Corporation Oxazoline modified dispersants
WO2020150123A1 (en) 2019-01-17 2020-07-23 The Lubrizol Corporation Traction fluids
WO2020176171A1 (en) 2019-02-28 2020-09-03 Exxonmobil Research And Engineering Company Low viscosity gear oil compositions for electric and hybrid vehicles
US10781394B2 (en) 2016-10-25 2020-09-22 Chevron Oronite Technology B.V. Lubricating oil compositions comprising a biodiesel fuel and a Mannich condensation product
US10781397B2 (en) 2014-12-30 2020-09-22 Exxonmobil Research And Engineering Company Lubricating oil compositions with engine wear protection
US10793801B2 (en) 2017-02-06 2020-10-06 Exxonmobil Chemical Patents Inc. Low transition temperature mixtures and lubricating oils containing the same
US10808196B2 (en) 2017-03-28 2020-10-20 Exxonmobil Chemical Patents Inc. Cold cranking simulator viscosity reducing base stocks and lubricating oil formulations containing the same
US10858610B2 (en) 2017-03-24 2020-12-08 Exxonmobil Chemical Patents Inc. Cold cranking simulator viscosity boosting base stocks and lubricating oil formulations containing the same
WO2020257377A1 (en) 2019-06-19 2020-12-24 Exxonmobil Research And Engineering Company Heat transfer fluids and methods of use
WO2020257371A1 (en) 2019-06-19 2020-12-24 Exxonmobil Research And Engineering Company Heat transfer fluids and methods of use
WO2020257375A1 (en) 2019-06-19 2020-12-24 Exxonmobil Research And Engineering Company Heat transfer fluids and methods of use
WO2020257373A1 (en) 2019-06-19 2020-12-24 Exxonmobil Research And Engineering Company Heat transfer fluids and methods of use
WO2020257376A1 (en) 2019-06-19 2020-12-24 Exxonmobil Research And Engineering Company Heat transfer fluids and methods of use
WO2020257379A1 (en) 2019-06-19 2020-12-24 Exxonmobil Research And Engineering Company Heat transfer fluids and methods of use
WO2020257374A1 (en) 2019-06-19 2020-12-24 Exxonmobil Research And Engineering Company Heat transfer fluids and methods of use
WO2020257370A1 (en) 2019-06-19 2020-12-24 Exxonmobil Research And Engineering Company Heat transfer fluids and methods of use
WO2020257378A1 (en) 2019-06-19 2020-12-24 Exxonmobil Research And Engineering Company Heat transfer fluids and methods of use
US10876062B2 (en) 2017-03-24 2020-12-29 Exxonmobil Chemical Patents Inc. Cold cranking simulator viscosity boosting base stocks and lubricating oil formulations containing the same
WO2020264534A2 (en) 2019-06-27 2020-12-30 Exxonmobil Research And Engineering Company Method for reducing solubilized copper levels in wind turbine gear oils
EP3760696A1 (en) 2018-12-20 2021-01-06 Infineum International Limited Oil anti-foulant and/or asphaltene agglomeration process
EP3778841A1 (en) 2019-08-15 2021-02-17 Infineum International Limited Method for reducing piston deposits in a marine diesel engine
US11015137B2 (en) 2017-03-30 2021-05-25 Innospec Limited Composition, method and use
EP3835392A1 (en) 2018-12-20 2021-06-16 Infineum International Limited Hydrocarbon marine fuel oil
WO2021154497A1 (en) 2020-01-30 2021-08-05 Exxonmobil Research And Engineering Company Sulfur-free, ashless, low phosphorus lubricant compositions with improved oxidation stability
WO2021181286A1 (en) 2020-03-11 2021-09-16 Chevron Oronite Company Llc Lubricating oil compositions with improved oxidative performance comprising alkylated diphenylamine antioxidant and sulfonate detergents
WO2021181285A1 (en) 2020-03-11 2021-09-16 Chevron Oronite Company Llc Lubricating oil compositions with improved oxidative performance comprising alkylated diphenylamine antioxidant and carboxylate detergents
WO2021194813A1 (en) 2020-03-27 2021-09-30 Exxonmobil Research And Engineering Company Monitoring health of heat transfer fluids for electric systems
US11174442B2 (en) 2017-03-30 2021-11-16 Innospec Limited Fuel compositions, methods and uses relating to quaternary ammonium salt additives for fuel used in spark ignition engines
WO2021229517A1 (en) 2020-05-14 2021-11-18 Chevron Japan Ltd. Lubricating oil composition including comb polymethacrylate and ethylene-based olefin copolymer viscosity modifiers
US11186791B2 (en) 2017-03-30 2021-11-30 Innospec Limited Composition, method and use
WO2022010606A1 (en) 2020-07-09 2022-01-13 Exxonmobil Research And Engineering Company Engine oil lubricant compositions and methods for making same with superior engine wear protection and corrosion protection
WO2022018682A1 (en) 2020-07-23 2022-01-27 Chevron Oronite Company Llc Succinimide dispersants post-treated with heteroaromatic glycidyl ethers that exhibit good soot handling performance
WO2022018681A1 (en) 2020-07-23 2022-01-27 Chevron Oronite Company Llc Succinimide dispersants post-treated with aromatic glycidyl ethers that exhibit good soot handling performance
WO2022054023A1 (en) 2020-09-14 2022-03-17 Chevron Japan Ltd. Lubricating oil containing alkyl phosphonic acid
WO2022072962A1 (en) 2020-09-30 2022-04-07 Exxonmobil Research And Engineering Company Low friction and low traction lubricant compositions useful in dry clutch motorcycles
WO2022074547A1 (en) 2020-10-05 2022-04-14 Chevron Japan Ltd. Friction modifier system
WO2022099291A1 (en) 2020-11-06 2022-05-12 Exxonmobil Research And Engineering Company Engine oil lubricant compositions and methods for making same with steel corrosion protection
WO2022112899A1 (en) 2020-11-25 2022-06-02 Chevron Japan Ltd. Lubricating oil compositions
EP4079828A1 (en) 2018-03-29 2022-10-26 Innospec Limited Composition, method and use
WO2022243947A1 (en) 2021-05-20 2022-11-24 Chevron Japan Ltd. Low ash lubricating oil composition
EP4180505A1 (en) 2021-11-15 2023-05-17 Infineum International Limited Improvements in marine fuels
WO2023111550A1 (en) 2021-12-14 2023-06-22 Innospec Limited Methods and uses relating to fuel compositions
WO2023122405A1 (en) 2021-12-21 2023-06-29 ExxonMobil Technology and Engineering Company Engine oil lubricant compostions and methods for making same with superior oil consumption
WO2023144721A1 (en) 2022-01-25 2023-08-03 Chevron Japan Ltd. Lubricating oil composition
WO2023156989A1 (en) 2022-02-21 2023-08-24 Chevron Oronite Company Llc Lubricating oil composition
US11760952B2 (en) 2021-01-12 2023-09-19 Ingevity South Carolina, Llc Lubricant thickener systems from modified tall oil fatty acids, lubricating compositions, and associated methods
US11795412B1 (en) 2023-03-03 2023-10-24 Afton Chemical Corporation Lubricating composition for industrial gear fluids
US11873461B1 (en) 2022-09-22 2024-01-16 Afton Chemical Corporation Extreme pressure additives with improved copper corrosion
US11884890B1 (en) 2023-02-07 2024-01-30 Afton Chemical Corporation Gasoline additive composition for improved engine performance
WO2024030899A1 (en) 2022-08-01 2024-02-08 Chevron Oronite Company Llc Lubricating oil composition for corrosion control
EP4353804A1 (en) 2022-10-11 2024-04-17 Infineum International Limited Functionalized c4 to c5 olefin polymers and lubricant compositions containing such
EP4353805A1 (en) 2022-10-11 2024-04-17 Infineum International Limited Lubricant composition containing metal alkanoate
EP4357443A1 (en) 2022-10-18 2024-04-24 Infineum International Limited Lubricating oil compositions
WO2024126998A1 (en) 2022-12-12 2024-06-20 Innospec Limited Composition, method and use
US12024686B2 (en) 2022-09-30 2024-07-02 Afton Chemical Corporation Gasoline additive composition for improved engine performance
EP4397738A1 (en) 2023-01-03 2024-07-10 Infineum International Limited Method for reduction of abnormal combustion events
EP4428212A1 (en) 2023-03-10 2024-09-11 Infineum International Limited Asphaltene deposition control
WO2024220396A1 (en) 2023-04-17 2024-10-24 Chevron Oronite Company Llc Friction modifier for wet clutch
WO2024220394A1 (en) 2023-04-17 2024-10-24 Chevron Oronite Company Llc Friction modifier for automatic transmission fluid
US12134742B2 (en) 2022-09-30 2024-11-05 Afton Chemical Corporation Fuel composition

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3018250A (en) * 1959-08-24 1962-01-23 California Research Corp Lubricating oil compositions containing nu-dialkylaminoalkyl alkenyl succinimides
US3024195A (en) * 1959-08-24 1962-03-06 California Research Corp Lubricating oil compositions of alkylpiperazine alkenyl succinimides
US3131150A (en) * 1961-04-12 1964-04-28 California Research Corp Lubricating oil compositions containing n-substituted alkenyl succinimides in combination with polyamines
US3154560A (en) * 1961-12-04 1964-10-27 Monsanto Co Nu, nu'-azaalkylene-bis
US3172892A (en) * 1959-03-30 1965-03-09 Reaction product of high molecular weight succinic acids and succinic anhydrides with an ethylene poly- amine

Patent Citations (6)

* 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
US3219666A (en) * 1959-03-30 1965-11-23 Derivatives of succinic acids and nitrogen compounds
US3018250A (en) * 1959-08-24 1962-01-23 California Research Corp Lubricating oil compositions containing nu-dialkylaminoalkyl alkenyl succinimides
US3024195A (en) * 1959-08-24 1962-03-06 California Research Corp Lubricating oil compositions of alkylpiperazine alkenyl succinimides
US3131150A (en) * 1961-04-12 1964-04-28 California Research Corp Lubricating oil compositions containing n-substituted alkenyl succinimides in combination with polyamines
US3154560A (en) * 1961-12-04 1964-10-27 Monsanto Co Nu, nu'-azaalkylene-bis

Cited By (771)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3522179A (en) * 1963-04-23 1970-07-28 Lubrizol Corp Lubricating composition containing esters of hydrocarbon-substituted succinic acid
US3415750A (en) * 1963-10-04 1968-12-10 Monsanto Co Imidazolines having polyalkenylsuccinimido-containing substituents
US3340281A (en) * 1965-06-14 1967-09-05 Standard Oil Co Method for producing lubricating oil additives
US3442808A (en) * 1966-11-01 1969-05-06 Standard Oil Co Lubricating oil additives
US3359204A (en) * 1966-12-19 1967-12-19 Ethyl Corp Lubricating oil dispersant
US3452002A (en) * 1966-12-22 1969-06-24 Exxon Research Engineering Co Adducts of alkylene imines and carboxylic acids
US3445386A (en) * 1967-01-13 1969-05-20 Mobil Oil Corp Detergent compositions
US3448048A (en) * 1967-01-23 1969-06-03 Lubrizol Corp Lubricant containing a high molecular weight acylated amine
US3519565A (en) * 1967-09-19 1970-07-07 Lubrizol Corp Oil-soluble interpolymers of n-vinylthiopyrrolidones
US3438899A (en) * 1968-02-23 1969-04-15 Chevron Res Alkenyl succinimide of tris (aminoalkyl) amine
US3793201A (en) * 1970-12-28 1974-02-19 Lubrizol Corp Stabilized basic magnesium sulfonate compositions
US4151173A (en) * 1971-05-17 1979-04-24 The Lubrizol Corporation Acylated polyoxyalkylene polyamines
US3883320A (en) * 1972-12-07 1975-05-13 Standard Oil Co Reducing deposits and smoke from jet fuels with additives incorporating an ammonium salt
US3960889A (en) * 1973-07-09 1976-06-01 Texaco Inc. Dehydrohalogenated polyalkene-maleic anhydride reaction product
US3879306A (en) * 1973-11-05 1975-04-22 Texaco Inc Automatic transmission fluid
US4194985A (en) * 1974-01-14 1980-03-25 The Lubrizol Corporation Polymeric compositions, method for their preparation, and lubricants containing them
US4005021A (en) * 1974-06-10 1977-01-25 Standard Oil Company (Indiana) Oil-soluble reaction products of (a) a high molecular weight olefin polymer, acrylonitrile, chlorine, an amine and maleic anhydride, with (g) an aliphatic amines; and lubricant compositions containing the same
US4081388A (en) * 1975-04-18 1978-03-28 Orogil Compositions based on alkenylsuccinimides as additives for lubricating oils
US4089794A (en) * 1975-06-25 1978-05-16 Exxon Research & Engineering Co. Polymeric additives for fuels and lubricants
US4138370A (en) * 1976-04-26 1979-02-06 Exxon Research & Engineering Co. Multipurpose lubricating oil additive based on electrophilically terminated anion of oxidized ethylene copolymer
US4029148A (en) * 1976-09-13 1977-06-14 Atlantic Richfield Company Well fracturing method
US4257779A (en) * 1976-12-23 1981-03-24 Texaco Inc. Hydrocarbylsuccinic anhydride and aminotriazole reaction product additive for fuel and mineral oils
US4263015A (en) * 1976-12-23 1981-04-21 Texaco Inc. Rust inhibitor and oil composition containing same
US4171273A (en) * 1977-03-14 1979-10-16 Texaco Inc. Fatty alkyl succinate ester and succinimide modified copolymers of ethylene and an alpha olefin
FR2404668A1 (en) * 1977-10-03 1979-04-27 Exxon Research Engineering Co COMPOSITION OF LUBRICATING OIL ADDITIONED TO A POLYOL ESTER AND AN IMIDE
US4173540A (en) * 1977-10-03 1979-11-06 Exxon Research & Engineering Co. Lubricating oil composition containing a dispersing-varnish inhibiting combination of polyol ester compound and a borated acyl nitrogen compound
US4153567A (en) * 1977-11-10 1979-05-08 Milliken Research Corporation Additives for lubricants and fuels
US4163644A (en) * 1978-04-25 1979-08-07 The Rolfite Company Suspension of coal in fuel oils
US4326972A (en) * 1978-06-14 1982-04-27 The Lubrizol Corporation Concentrates, lubricant compositions and methods for improving fuel economy of internal combustion engine
US4159956A (en) * 1978-06-30 1979-07-03 Chevron Research Company Succinimide dispersant combination
US4240803A (en) * 1978-09-11 1980-12-23 Mobil Oil Corporation Fuel containing novel detergent
US4256595A (en) * 1978-09-28 1981-03-17 Texaco Inc. Diesel lubricant composition containing 5-amino-triazole-succinic anhydride reaction product
US4239633A (en) * 1979-06-04 1980-12-16 Exxon Research & Engineering Co. Molybdenum complexes of ashless polyol ester dispersants as friction-reducing antiwear additives for lubricating oils
US4248719A (en) * 1979-08-24 1981-02-03 Texaco Inc. Quaternary ammonium salts and lubricating oil containing said salts as dispersants
US4237022A (en) * 1979-10-01 1980-12-02 The Lubrizol Corporation Tartarimides and lubricants and fuels containing the same
EP0031236A2 (en) * 1979-12-20 1981-07-01 The British Petroleum Company p.l.c. Lubricant additives, their method of preparation and lubricants containing them
EP0031236A3 (en) * 1979-12-20 1981-09-09 The British Petroleum Company P.L.C. Lubricant additives, their method of preparation and lubricants containing them
US4400282A (en) * 1980-12-05 1983-08-23 Gulf Research & Development Company Lubricating oils containing quaternary ammonium thiomolybdates
US4326973A (en) * 1981-01-13 1982-04-27 Texaco Inc. Quaternary ammonium succinimide salt composition and lubricating oil containing same
US4440658A (en) * 1981-01-16 1984-04-03 Mobil Oil Corporation Anti-rust compositions
US4505718A (en) * 1981-01-22 1985-03-19 The Lubrizol Corporation Organo transition metal salt/ashless detergent-dispersant combinations
US4652273A (en) * 1981-07-30 1987-03-24 Institut Francais Du Petrole Hydrocarbon middle distillates composition containing nitrogen-containing additives for decreasing its cloud point
US4579674A (en) * 1981-12-28 1986-04-01 Texaco Inc. Hydrocarbylsuccinimide of a secondary hydroxyl-substituted polyamine and lubricating oil containing same
US4491455A (en) * 1982-02-10 1985-01-01 Nippon Oil And Fats Co., Ltd. Method for improving cold flow of fuel oils
US4440659A (en) * 1982-02-19 1984-04-03 Ethyl Corporation Lubricating oil ashless dispersant and lubricating oils containing same
US4491527A (en) * 1982-04-26 1985-01-01 The Lubrizol Corporation Ester-heterocycle compositions useful as "lead paint" inhibitors in lubricants
US4623684A (en) 1982-08-09 1986-11-18 The Lubrizol Corporation Hydrocarbyl substituted carboxylic acylating agent derivative containing combinations, and fuels containing same
US4559155A (en) * 1982-08-09 1985-12-17 The Lubrizol Corporation Hydrocarbyl substituted carboxylic acylating agent derivative containing combinations, and fuels containing same
US4564460A (en) * 1982-08-09 1986-01-14 The Lubrizol Corporation Hydrocarbyl-substituted carboxylic acylating agent derivative containing combinations, and fuels containing same
US4596663A (en) * 1982-08-09 1986-06-24 The Lubrizol Corporation Carboxylic acylating agents substituted with olefin polymers of high molecular weight mono-olefins, derivatives thereof, and fuels and lubricants containing same
US4613342A (en) * 1982-08-09 1986-09-23 The Lubrizol Corporation Hydrocarbyl substituted carboxylic acylating agent derivative containing combinations, and fuels containing same
US4575526A (en) * 1982-08-09 1986-03-11 The Lubrizol Corporation Hydrocarbyl substituted carboxylic acylaging agent derivative containing combinations, and fuels containing same
US4744798A (en) * 1982-09-30 1988-05-17 Mobil Oil Corporation Benzophenone derivatives as fuel additives
US4637886A (en) * 1982-12-27 1987-01-20 Exxon Research & Engineering Co. Macrocyclic polyamine and polycyclic polyamine multifunctional lubricating oil additives
US4560490A (en) * 1983-02-04 1985-12-24 Institut Francais Du Petrole Dispersing additive compositions for lubricating oils and their manufacture
US4617137A (en) * 1984-11-21 1986-10-14 Chevron Research Company Glycidol modified succinimides
US4631070A (en) * 1984-11-21 1986-12-23 Chevron Research Company Glycidol modified succinimides and fuel compositions containing the same
US4695390A (en) * 1985-01-04 1987-09-22 The Lubrizol Corporation Reaction product of polyalrylene-substituted polycarboxylic acid acylating agent, polyamine and sulfolene as a dispersant
US5053152A (en) * 1985-03-14 1991-10-01 The Lubrizol Corporation High molecular weight nitrogen-containing condensates and fuels and lubricants containing same
US5368615A (en) * 1985-03-14 1994-11-29 The Lubrizol Corporation High molecular weight nitrogen-containing condensates and fuels and lubricants containing same
US5296154A (en) * 1985-03-14 1994-03-22 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
US5160648A (en) * 1985-03-14 1992-11-03 The Lubrizol Corporation High molecular weight nitrogen-containing condensates and fuels and lubricants containing same
US6355074B1 (en) 1985-07-11 2002-03-12 Exxon Chemical Patents Inc Oil soluble dispersant additives useful in oleaginous compositions
US6127321A (en) * 1985-07-11 2000-10-03 Exxon Chemical Patents Inc Oil soluble dispersant additives useful in oleaginous compositions
US6051537A (en) * 1985-07-11 2000-04-18 Exxon Chemical Patents Inc Dispersant additive mixtures for oleaginous compositions
US4804389A (en) * 1985-08-16 1989-02-14 The Lubrizol Corporation Fuel products
US4659338A (en) * 1985-08-16 1987-04-21 The Lubrizol Corporation Fuel compositions for lessening valve seat recession
WO1987003003A1 (en) 1985-11-08 1987-05-21 The Lubrizol Corporation Fuel compositions
US5354484A (en) * 1986-06-13 1994-10-11 The Lubrizol Corporation Phosphorus-containing lubricant and functional fluid compositions
US4755311A (en) * 1986-08-14 1988-07-05 The Lubrizol Corporation Phosphorus-, sulfur- and boron-containing compositions, and lubricant and functional fluid compositions containing same
WO1988001272A2 (en) 1986-08-14 1988-02-25 The Lubrizol Corporation Borated amine salts of monothiophosphoric acids
US4866139A (en) * 1986-10-07 1989-09-12 Exxon Chemical Patents Inc. Lactone modified, esterified dispersant additives useful in oleaginous compositions
US4906394A (en) * 1986-10-07 1990-03-06 Exxon Chemical Patents Inc. Lactone modified mono-or dicarboxylic acid based adduct dispersant compositions
US4866141A (en) * 1986-10-07 1989-09-12 Exxon Chemical Patents Inc. Lactone modified, esterfied or aminated additives useful in oleaginous compositions and compositions containing same
US4963275A (en) * 1986-10-07 1990-10-16 Exxon Chemical Patents Inc. Dispersant additives derived from lactone modified amido-amine adducts
US5032320A (en) * 1986-10-07 1991-07-16 Exxon Chemical Patents Inc. Lactone modified mono- or dicarboxylic acid based adduct dispersant compositions
US4954276A (en) * 1986-10-07 1990-09-04 Exxon Chemical Patents Inc. Lactone modified adducts or reactants and oleaginous compositions containing same
US4866140A (en) * 1986-10-07 1989-09-12 Exxon Chemical Patents Inc. Lactone modified adducts or reactants and oleaginous compositions containing same
US4954277A (en) * 1986-10-07 1990-09-04 Exxon Chemical Patents Inc. Lactone modified, esterified or aminated additives useful in oleaginous compositions and compositions containing same
US5788722A (en) * 1986-10-16 1998-08-04 Exxon Chemical Patents Inc High functionality low molecular weight oil soluble dispersant additives useful in oleaginous compositions
US5756428A (en) * 1986-10-16 1998-05-26 Exxon Chemical Patents Inc. High functionality low molecular weight oil soluble dispersant additives useful in oleaginous composition
US5141658A (en) * 1986-11-07 1992-08-25 Dibiase Stephen A Lubricant composition comprising a sulfur additive and a borated dispersant
US4870197A (en) * 1986-12-12 1989-09-26 Exxon Chemical Patents Inc. Method for preparing salts of polyolefinic substituted dicarboxylic acids
US5451333A (en) * 1987-05-26 1995-09-19 Exxon Chemical Patents Inc. Haze resistant dispersant-detergent compositions
US5312554A (en) * 1987-05-26 1994-05-17 Exxon Chemical Patents Inc. Process for preparing stable oleaginous compositions
US4820432A (en) * 1987-07-24 1989-04-11 Exxon Chemical Patents Inc. Lactone-modified, Mannich base dispersant additives useful in oleaginous compositions
US4971711A (en) * 1987-07-24 1990-11-20 Exxon Chemical Patents, Inc. Lactone-modified, mannich base dispersant additives useful in oleaginous compositions
US4863624A (en) * 1987-09-09 1989-09-05 Exxon Chemical Patents Inc. Dispersant additives mixtures for oleaginous compositions
EP0310365A1 (en) * 1987-09-30 1989-04-05 Amoco Corporation Engine seal compatible dispersant for lubricating oils
EP0310367A1 (en) * 1987-09-30 1989-04-05 Amoco Corporation Medium speed diesel engine lubricating oils
US4908145A (en) * 1987-09-30 1990-03-13 Amoco Corporation Engine seal compatible dispersants for lubricating oils
US5080815A (en) * 1987-09-30 1992-01-14 Amoco Corporation Method for preparing engine seal compatible dispersant for lubricating oils comprising reacting hydrocarbyl substituted discarboxylic compound with aminoguanirise or basic salt thereof
US5174915A (en) * 1987-09-30 1992-12-29 Ethyl Petroleum Additives, Inc. Medium speed diesel engine lubricating oils
US5320765A (en) * 1987-10-02 1994-06-14 Exxon Chemical Patents Inc. Low ash lubricant compositions for internal combustion engines
US5102566A (en) * 1987-10-02 1992-04-07 Exxon Chemical Patents Inc. Low ash lubricant compositions for internal combustion engines (pt-727)
US5141657A (en) * 1987-10-02 1992-08-25 Exxon Chemical Patents Inc. Lubricant compositions for internal combustion engines
US5026495A (en) * 1987-11-19 1991-06-25 Exxon Chemical Patents Inc. Oil soluble dispersant additives useful in oleaginous compositions
US5407591A (en) * 1987-11-19 1995-04-18 Exxon Chemical Patents Inc. Oil soluble dispersant additives comprising the reaction product of a mannich base and a polyepoxide
US5085788A (en) * 1987-11-19 1992-02-04 Exxon Chemical Patents Inc. Oil soluble dispersant additives useful in oleaginous compositions
US5160350A (en) * 1988-01-27 1992-11-03 The Lubrizol Corporation Fuel compositions
US5256325A (en) * 1988-02-29 1993-10-26 Exxon Chemical Patents Inc. Polyanhydride modified adducts or reactants and oleaginous compositions containing same
US5053150A (en) * 1988-02-29 1991-10-01 Exxon Chemical Patents Inc. Polyepoxide modified adducts or reactants and oleaginous compositions containing same
US5370810A (en) * 1988-02-29 1994-12-06 Exxon Chemical Patents Inc. Polyepoxide modified adducts or reactants and oleaginous compositions containing same PT-696
US5385687A (en) * 1988-02-29 1995-01-31 Exxon Chemical Patents Inc. Polyanhydride modified adducts or reactants and oleaginous compositions containing same
US4957645A (en) * 1988-02-29 1990-09-18 Exxon Chemical Patents Inc. Oil soluble dispersant additives useful in oleaginous compositions
US5275748A (en) * 1988-02-29 1994-01-04 Exxon Chemical Patents Inc. Polyanhydride modified adducts or reactants and oleaginous compositions containing same
US5030369A (en) * 1988-02-29 1991-07-09 Exxon Chemical Patents Inc. Oil soluble dispersant additives useful in oleaginous compositions
US5482519A (en) * 1988-02-29 1996-01-09 Exxon Chemical Patents Inc. Polyepoxide modified adducts or reactants and oleaginous compositions containing same
US5217634A (en) * 1988-02-29 1993-06-08 Exxon Chemical Patents Inc. Polyepoxide modified adducts or reactants and oleaginous compositions containing same
US5198133A (en) * 1988-03-14 1993-03-30 Ethyl Petroleum Additives, Inc. Modified succinimide or sucinamide dispersants and their production
US5164103A (en) * 1988-03-14 1992-11-17 Ethyl Petroleum Additives, Inc. Preconditioned atf fluids and their preparation
US5439606A (en) * 1988-03-14 1995-08-08 Ethyl Petroleum Additives, Inc. Modified succinimide or succinamide dispersants and their production
US4855074A (en) * 1988-03-14 1989-08-08 Ethyl Petroleum Additives, Inc. Homogeneous additive concentrates and their formation
US5389273A (en) * 1988-03-14 1995-02-14 Ethyl Petroleum Additives, Inc. Modified succinimide or succinamide dispersants and their production
US4943382A (en) * 1988-04-06 1990-07-24 Exxon Chemical Patents Inc. Lactone modified dispersant additives useful in oleaginous compositions
US5041622A (en) * 1988-04-22 1991-08-20 The Lubrizol Corporation Three-step process for making substituted carboxylic acids and derivatives thereof
US4952328A (en) * 1988-05-27 1990-08-28 The Lubrizol Corporation Lubricating oil compositions
US4981602A (en) * 1988-06-13 1991-01-01 The Lubrizol Corporation Lubricating oil compositions and concentrates
US4904401A (en) * 1988-06-13 1990-02-27 The Lubrizol Corporation Lubricating oil compositions
EP0351964A1 (en) 1988-06-24 1990-01-24 Exxon Chemical Patents Inc. Synergistic combination of additives useful in power transmitting compositions
US4957649A (en) * 1988-08-01 1990-09-18 The Lubrizol Corporation Lubricating oil compositions and concentrates
US4938881A (en) * 1988-08-01 1990-07-03 The Lubrizol Corporation Lubricating oil compositions and concentrates
US5334329A (en) * 1988-10-07 1994-08-02 The Lubrizol Corporation Lubricant and functional fluid compositions exhibiting improved demulsibility
US5340487A (en) * 1988-11-07 1994-08-23 Exxon Chemical Patents Inc. Dispersant adducts comprising alcohol adducts of dicarboxylic acid monoepoxy thiol reaction products
US5057617A (en) * 1988-11-07 1991-10-15 Exxon Chemical Patents Inc. Dispersant additives prepared from monoepoxy thiols
US4954572A (en) * 1988-11-07 1990-09-04 Exxon Chemical Patents Inc. Dispersant additives prepared from monoepoxy alcohols
US5205947A (en) * 1988-11-07 1993-04-27 Exxon Chemical Patents Inc. Dispersant additives comprising amine adducts of dicarboxylic acid monoepoxy thiol reaction products
JP2864146B2 (en) 1989-04-21 1999-03-03 アジップ・ペトローリ・エセ・ピ・ア Manufacturing method of fuel or lubricating oil
US5182041A (en) * 1989-05-01 1993-01-26 Texaco Inc. Dispersant - anti-oxidant additive and lubricating oil composition containing same
EP0399764A1 (en) 1989-05-22 1990-11-28 Ethyl Petroleum Additives Limited Lubricant compositions
US5147414A (en) * 1989-08-03 1992-09-15 Texaco Inc. Process for producing ori control additives
US5312555A (en) * 1990-02-16 1994-05-17 Ethyl Petroleum Additives, Inc. Succinimides
US5411559A (en) * 1990-02-16 1995-05-02 Ethyl Corporation Succinimides
US5024677A (en) * 1990-06-11 1991-06-18 Nalco Chemical Company Corrosion inhibitor for alcohol and gasohol fuels
EP0611818A1 (en) 1990-07-31 1994-08-24 Exxon Chemical Patents Inc. Low pressure derived mixed phosphorous- and sulfur-containing reaction products useful in power transmitting compositions and process for preparing the same
US5232616A (en) * 1990-08-21 1993-08-03 Chevron Research And Technology Company Lubricating compositions
US5302304A (en) * 1990-12-21 1994-04-12 Ethyl Corporation Silver protective lubricant composition
US5955404A (en) * 1991-04-17 1999-09-21 Mobil Oil Corporation Lubricant and fuel compositions containing an organo-substituted diphenyl sulfide
US5614480A (en) * 1991-04-19 1997-03-25 The Lubrizol Corporation Lubricating compositions and concentrates
US5562864A (en) * 1991-04-19 1996-10-08 The Lubrizol Corporation Lubricating compositions and concentrates
US5490945A (en) * 1991-04-19 1996-02-13 The Lubrizol Corporation Lubricating compositions and concentrates
US5221491A (en) * 1991-08-09 1993-06-22 Exxon Chemical Patents Inc. Two-cycle oil additive
EP0558835A1 (en) 1992-01-30 1993-09-08 Albemarle Corporation Biodegradable lubricants and functional fluids
US5304315A (en) * 1992-04-15 1994-04-19 Exxon Chemical Patents Inc. Prevention of gel formation in two-cycle oils
US5330667A (en) * 1992-04-15 1994-07-19 Exxon Chemical Patents Inc. Two-cycle oil additive
US5292813A (en) * 1992-10-02 1994-03-08 Exxon Research & Engineering Co. Fullerene-grafted polymers and processes of making
US5292444A (en) * 1992-10-02 1994-03-08 Exxon Research And Engineering Company Lube oil compositions containing fullerene-grafted polymers
US5430105A (en) * 1992-12-17 1995-07-04 Exxon Chemical Patents Inc. Low sediment process for forming borated dispersant
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
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
US5554310A (en) * 1992-12-17 1996-09-10 Exxon Chemical Patents Inc. Trisubstituted unsaturated polymers
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
US5356552A (en) * 1993-03-09 1994-10-18 Chevron Research And Technology Company, A Division Of Chevron U.S.A. Inc. Chlorine-free lubricating oils having modified high molecular weight succinimides
US6294506B1 (en) 1993-03-09 2001-09-25 Chevron Chemical Company Lubricating oils having carbonated sulfurized metal alkyl phenates and carbonated metal alkyl aryl sulfonates
EP0629614A1 (en) * 1993-05-27 1994-12-21 Hoechst Aktiengesellschaft Substituted succinimides
US5554768A (en) * 1993-05-27 1996-09-10 Hoechst Aktiengesellschaft Substituted Succinimides
WO1994029413A1 (en) * 1993-06-16 1994-12-22 Ethyl Corporation Ashless dispersants, their preparation, and their use
WO1995000607A1 (en) * 1993-06-25 1995-01-05 Ethyl Corporation Fluoroelastomer-friendly crankcase and drivetrain lubricants and their use
US5454962A (en) * 1993-06-25 1995-10-03 Ethyl Petroleum Additives, Inc. Fluoroelastomer-friendly crankcase and drivetrain lubricants and their use
US5439607A (en) * 1993-12-30 1995-08-08 Exxon Chemical Patents Inc. Multifunctional viscosity index improver-dispersant antioxidant
EP0683220A2 (en) 1994-05-18 1995-11-22 Ethyl Corporation Lubricant additive compositions
EP0713907A2 (en) 1994-09-26 1996-05-29 Ethyl Petroleum Additives Limited Zinc additives of enhanced performance capabilities
US6306802B1 (en) 1994-09-30 2001-10-23 Exxon Chemical Patents Inc. Mixed antioxidant composition
EP0713908A1 (en) 1994-11-22 1996-05-29 Ethyl Corporation Power transmission fluids
US5814111A (en) * 1995-03-14 1998-09-29 Shell Oil Company Gasoline compositions
EP0778333A2 (en) 1995-11-09 1997-06-11 The Lubrizol Corporation Carboxylic compositions, derivatives, lubricants, fuels and concentrates
EP0776963A1 (en) 1995-12-01 1997-06-04 Chevron Chemical Company Polyalkylene succinimides and post-treated derivatives thereof
CN1064271C (en) * 1995-12-28 2001-04-11 华南理工大学 Surfactant for emulsified-liquid film and preparation method thereof
EP0831104A2 (en) 1996-08-20 1998-03-25 Chevron Chemical Company Novel dispersant terpolymers
US6376434B1 (en) * 1996-10-29 2002-04-23 Idemitsu Kosan Co., Ltd. Lube oil compositions for diesel engines
US6624123B2 (en) * 1997-04-11 2003-09-23 Chevron Chemical S.A. Use of surfactants with high molecular weight for improving the filterability in hydraulic lubricants
EP0921136A1 (en) * 1997-12-03 1999-06-09 The Lubrizol Corporation Nitrogen containing dispersant-viscosity improvers
US6265358B1 (en) 1997-12-03 2001-07-24 The Lubrizol Corporation Nitrogen containing dispersant-viscosity improvers
US6486101B2 (en) 1997-12-03 2002-11-26 The Lubrizol Corporation Nitrogen containing dispersant-viscosity improvers
US6860241B2 (en) 1999-06-16 2005-03-01 Dober Chemical Corp. Fuel filter including slow release additive
EP1188813A1 (en) * 2000-09-19 2002-03-20 Ethyl Corporation Lubricants comprising friction modifiers
US6855674B2 (en) 2000-12-22 2005-02-15 Infineum International Ltd. Hydroxy aromatic Mannich base condensation products and the use thereof as soot dispersants in lubricating oil compositions
US20030173251A1 (en) * 2000-12-22 2003-09-18 Antonio Gutierrez Hydroxy aromatic mannich base condensation products and the use thereof as soot dispersants in lubricating oil compositions
US6440905B1 (en) * 2001-04-24 2002-08-27 The Lubrizol Corporation Surfactants and dispersants by in-line reaction
US20050045527A1 (en) * 2001-05-17 2005-03-03 Goze Maria Caridad B. Low noack volatility poly alpha-olefins
US6949688B2 (en) 2001-05-17 2005-09-27 Exxonmobil Chemical Patents Inc. Low Noack volatility poly α-olefins
US20020193650A1 (en) * 2001-05-17 2002-12-19 Goze Maria Caridad B. Low noack volatility poly alpha-olefins
US6824671B2 (en) 2001-05-17 2004-11-30 Exxonmobil Chemical Patents Inc. Low noack volatility poly α-olefins
US6827750B2 (en) 2001-08-24 2004-12-07 Dober Chemical Corp Controlled release additives in fuel systems
US7581558B2 (en) 2001-08-24 2009-09-01 Cummins Filtration Ip Inc. Controlled release of additives in fluid systems
US8109287B2 (en) 2001-08-24 2012-02-07 Cummins Filtration Ip, Inc. Controlled release of additives in fluid systems
US7938277B2 (en) 2001-08-24 2011-05-10 Dober Chemical Corporation Controlled release of microbiocides
US6835218B1 (en) 2001-08-24 2004-12-28 Dober Chemical Corp. Fuel additive compositions
US7001531B2 (en) 2001-08-24 2006-02-21 Dober Chemical Corp. Sustained release coolant additive composition
US7591279B2 (en) 2001-08-24 2009-09-22 Cummins Filtration Ip Inc. Controlled release of additives in fluid systems
EP2272940A1 (en) 2001-09-14 2011-01-12 Afton Chemical Intangibles LLC Fuels compositions for direct injection gasoline engines
US6617287B2 (en) 2001-10-22 2003-09-09 The Lubrizol Corporation Manual transmission lubricants with improved synchromesh performance
US6756348B2 (en) 2001-11-29 2004-06-29 Chevron Oronite Company Llc Lubricating oil having enhanced resistance to oxidation, nitration and viscosity increase
US6642191B2 (en) 2001-11-29 2003-11-04 Chevron Oronite Company Llc Lubricating oil additive system particularly useful for natural gas fueled engines
US6627584B2 (en) 2002-01-28 2003-09-30 Ethyl Corporation Automatic transmission fluid additive comprising reaction product of hydrocarbyl acrylates and dihydrocarbyldithiophosphoric acids
US20030172584A1 (en) * 2002-03-13 2003-09-18 Henly Timothy J. Fuel lubricity additives derived from hydrocarbyl succinic anhydrides and hydroxy amines, and middle distillate fuels containing same
US7182795B2 (en) 2002-03-13 2007-02-27 Atton Chemical Intangibles Llc Fuel lubricity additives derived from hydrocarbyl succinic anhydrides and hydroxy amines, and middle distillate fuels containing same
US6869917B2 (en) 2002-08-16 2005-03-22 Exxonmobil Chemical Patents Inc. Functional fluid lubricant using low Noack volatility base stock fluids
US20040033908A1 (en) * 2002-08-16 2004-02-19 Deckman Douglas E. Functional fluid lubricant using low Noack volatility base stock fluids
US20040147410A1 (en) * 2003-01-15 2004-07-29 Milner Jeffrey L Extended drain, thermally stable, gear oil formulations
US7888299B2 (en) 2003-01-15 2011-02-15 Afton Chemical Japan Corp. Extended drain, thermally stable, gear oil formulations
US20040235682A1 (en) * 2003-05-22 2004-11-25 Chevron Oronite Company Llc Low emission diesel lubricant with improved corrosion protection
EP1503316A1 (en) 2003-07-30 2005-02-02 Ethyl Petroleum Additives, Inc. Fuel consumption economy credits method
US20050027592A1 (en) * 2003-07-30 2005-02-03 Pettigrew F. Alexander Powered platform fuel consumption economy credits method
EP1512736A1 (en) * 2003-09-05 2005-03-09 Infineum International Limited Stabilised diesel fuel additive compositions
US20050065043A1 (en) * 2003-09-23 2005-03-24 Henly Timothy J. Power transmission fluids having extended durability
US20070054813A1 (en) * 2003-09-25 2007-03-08 Chip Hewette Boron free automotive gear oil
US7884058B2 (en) 2003-09-30 2011-02-08 Chevron Oronite Company Llc Stable colloidal suspensions and lubricating oil compositions containing same
US20050070445A1 (en) * 2003-09-30 2005-03-31 Nelson Kenneth D. Stable colloidal suspensions and lubricating oil compositions containing same
US20100279901A1 (en) * 2003-11-10 2010-11-04 Iyer Ramnath N Methods for providing steel-on-steel friction and/or steel-on-paper friction with lubricant compositions for power transmitting fluids
EP2230292A1 (en) 2003-11-10 2010-09-22 Afton Chemical Corporation Methods of lubricating transmissions
US9267093B2 (en) 2003-11-10 2016-02-23 Afton Chemical Corporation Methods for providing steel-on-steel friction and/or steel-on-paper friction with lubricant compositions for power transmitting fluids
US20050101494A1 (en) * 2003-11-10 2005-05-12 Iyer Ramnath N. Lubricant compositions for power transmitting fluids
US20080009426A1 (en) * 2003-11-10 2008-01-10 Iyer Ramnath N Lubricant Compositions and Methods Comprising Dispersant and Detergent
US20050101497A1 (en) * 2003-11-12 2005-05-12 Saathoff Lee D. Compositions and methods for improved friction durability in power transmission fluids
US20080090744A1 (en) * 2003-11-12 2008-04-17 Saathoff Lee D Compositions and Methods for Improved Friction Durability in Power Transmission Fluids
US20050181959A1 (en) * 2004-02-17 2005-08-18 Esche Carl K.Jr. Lubricant and fuel additives derived from treated amines
US7645728B2 (en) 2004-02-17 2010-01-12 Afton Chemical Corporation Lubricant and fuel additives derived from treated amines
US7947636B2 (en) 2004-02-27 2011-05-24 Afton Chemical Corporation Power transmission fluids
EP1568759A2 (en) 2004-02-27 2005-08-31 Afton Chemical Corporation Power transmission fluids
US7361629B2 (en) 2004-03-10 2008-04-22 Afton Chemical Corporation Additives for lubricants and fuels
US20050202980A1 (en) * 2004-03-10 2005-09-15 Loper John T. Novel additives for lubricants and fuels
US7863228B2 (en) 2004-03-10 2011-01-04 Afton Chemical Corporation Additives for lubricants and fuels
US7875576B2 (en) 2004-07-29 2011-01-25 Chevron Oronite Company Llc Lubricating oil composition for internal combustion engines
US20060025313A1 (en) * 2004-07-29 2006-02-02 Chevron Oronite Company Llc Lubricating oil composition for internal combustion engines
EP1640438A1 (en) 2004-09-17 2006-03-29 Infineum International Limited Improvements in Fuel Oils
US8690969B2 (en) 2004-09-17 2014-04-08 Infineum International Limited Fuel oils
US20060059770A1 (en) * 2004-09-17 2006-03-23 Sutkowski Andrew C Fuel oils
US9481841B2 (en) 2004-12-09 2016-11-01 The Lubrizol Corporation Process of preparation of an additive and its use
US20060135375A1 (en) * 2004-12-21 2006-06-22 Chevron Oronite Company Llc Anti-shudder additive composition and lubricating oil composition containing the same
EP1674557A2 (en) 2004-12-21 2006-06-28 Chevron Oronite Company LLC An anti-shudder additive composition and lubricating oil composition containing the same
EP2116590A1 (en) 2005-02-18 2009-11-11 Infineum International Limited Soot dispersants and lubricating oil compositions containing same
US8557752B2 (en) 2005-03-23 2013-10-15 Afton Chemical Corporation Lubricating compositions
EP1871861B1 (en) 2005-04-08 2020-01-15 The Lubrizol Corporation Additive system for lubricants
US7745542B2 (en) 2005-04-29 2010-06-29 Chevron Oronite Company Llc Lubricating oil additive composition and method of making the same
US20070027267A1 (en) * 2005-04-29 2007-02-01 Chevron Oronite Company Llc Lubricating oil additive composition and method of making the same
US20060264339A1 (en) * 2005-05-19 2006-11-23 Devlin Mark T Power transmission fluids with enhanced lifetime characteristics
EP3406692A1 (en) 2005-06-16 2018-11-28 The Lubrizol Corporation Fuel composition comprising a quaternary ammonium salt detergent
EP2998384A1 (en) 2005-06-16 2016-03-23 The Lubrizol Corporation Diesel fuel composition comprising a quaternary ammonium salt detergent
US20070004603A1 (en) * 2005-06-30 2007-01-04 Iyer Ramnath N Methods for improved power transmission performance and compositions therefor
US20070000745A1 (en) * 2005-06-30 2007-01-04 Cameron Timothy M Methods for improved power transmission performance
US20070042916A1 (en) * 2005-06-30 2007-02-22 Iyer Ramnath N Methods for improved power transmission performance and compositions therefor
US7820602B2 (en) 2005-07-12 2010-10-26 King Industries, Inc. Amine tungstates and lubricant compositions
US20070042917A1 (en) * 2005-07-12 2007-02-22 Ramanathan Ravichandran Amine Tungstates and Lubricant Compositions
US8080500B2 (en) 2005-07-12 2011-12-20 King Industries, Inc. Amine tungstates and lubricant compositions
US20080194440A1 (en) * 2005-07-12 2008-08-14 Ramanathan Ravichandran Amine tungstates and lubricant compositions
US20090029888A1 (en) * 2005-07-12 2009-01-29 Ramanathan Ravichandran Amine tungstates and lubricant compositions
EP1757673A1 (en) 2005-08-23 2007-02-28 Chevron Oronite Company LLC Lubricating oil composition for internal combustion engines
US7618928B2 (en) 2005-08-31 2009-11-17 Chevron Oronite Company Llc Lubricating oil additive composition and method of making the same
US20070049503A1 (en) * 2005-08-31 2007-03-01 Chevron Oronite Company Llc Lubricating oil additive composition and method of making the same
US20070078066A1 (en) * 2005-10-03 2007-04-05 Milner Jeffrey L Lubricant formulations containing extreme pressure agents
US20070142660A1 (en) * 2005-11-09 2007-06-21 Degonia David J Salt of a sulfur-containing, phosphorus-containing compound, and methods thereof
US8299003B2 (en) 2005-11-09 2012-10-30 Afton Chemical Corporation Composition comprising a sulfur-containing, phosphorus-containing compound, and/or its salt, and uses thereof
US20070105728A1 (en) * 2005-11-09 2007-05-10 Phillips Ronald L Lubricant composition
US20070142237A1 (en) * 2005-11-09 2007-06-21 Degonia David J Lubricant composition
US20080319216A1 (en) * 2005-11-09 2008-12-25 Degonia David J Salt of a Sulfur-Containing, Phosphorus-Containing Compound, And Methods Thereof
US7928260B2 (en) 2005-11-09 2011-04-19 Afton Chemical Corporation Salt of a sulfur-containing, phosphorus-containing compound, and methods thereof
US20070142659A1 (en) * 2005-11-09 2007-06-21 Degonia David J Sulfur-containing, phosphorus-containing compound, its salt, and methods thereof
US20070111906A1 (en) * 2005-11-12 2007-05-17 Milner Jeffrey L Relatively low viscosity transmission fluids
US20070123437A1 (en) * 2005-11-30 2007-05-31 Chevron Oronite Company Llc Lubricating oil composition with improved emission compatibility
US7981846B2 (en) 2005-11-30 2011-07-19 Chevron Oronite Company Llc Lubricating oil composition with improved emission compatibility
US9752020B2 (en) 2005-12-28 2017-09-05 Bridgestone Corporation Rubber composition having good wet-traction properties and a low aromatic-oil content
US20070149689A1 (en) * 2005-12-28 2007-06-28 Xiaorong Wang Rubber composition having good wet-traction properties and a low aromatic-oil content
EP2371933A1 (en) 2006-02-06 2011-10-05 The Lubrizol Corporation Tartaric acid derivatives as fuel economy improvers and antiwear agents in crankcase oils and preparation thereof
US20070270317A1 (en) * 2006-05-19 2007-11-22 Milner Jeffrey L Power Transmission Fluids
EP3205698A1 (en) 2006-06-15 2017-08-16 Dow Global Technologies LLC Functionalized olefin interpolymers, compositions and articles prepared therefrom, and methods for making the same
EP2363444A1 (en) 2006-06-15 2011-09-07 Dow Global Technologies LLC Functionalized olefin interpolymers, compositions and articles prepared therefrom, and methods for making the same
EP2363420A1 (en) 2006-06-15 2011-09-07 Dow Global Technologies LLC Functionalized olefin interpolymers, compositions and articles prepared therefrom, and methods for making the same
EP2363445A1 (en) 2006-06-15 2011-09-07 Dow Global Technologies LLC Functionalized propylene interpolymers, compositions and articles prepared therefrom, and methods for making the same
US7879775B2 (en) 2006-07-14 2011-02-01 Afton Chemical Corporation Lubricant compositions
US7902133B2 (en) 2006-07-14 2011-03-08 Afton Chemical Corporation Lubricant composition
US20080015124A1 (en) * 2006-07-14 2008-01-17 Devlin Mark T Lubricant composition
EP3339404A1 (en) 2006-07-18 2018-06-27 Infineum International Limited Lubricating oil compositions
WO2008013698A1 (en) 2006-07-21 2008-01-31 Exxonmobil Research And Engineering Company Method for lubricating heavy duty geared apparatus
US7833953B2 (en) 2006-08-28 2010-11-16 Afton Chemical Corporation Lubricant composition
US20080103236A1 (en) * 2006-10-27 2008-05-01 Chevron Oronite Company Llc Lubricating oil additive composition and method of making the same
US7816309B2 (en) 2006-10-27 2010-10-19 Chevron Oronite Company Llc Lubricating oil additive composition and method of making the same
US20080103074A1 (en) * 2006-10-27 2008-05-01 Chevron Oronite Company Llc Lubricating oil additive composition and method of making the same
US7928044B2 (en) 2006-10-27 2011-04-19 Chevron Oronite Company Llc Lubricating oil additive composition and method of making the same
EP1916292A1 (en) 2006-10-27 2008-04-30 Chevron Oronite Company LLC A lubricating oil additive composition and method of making the same
EP1916293A1 (en) 2006-10-27 2008-04-30 Chevron Oronite Company LLC A lubricating oil additive composition and method of making the same
US20080113888A1 (en) * 2006-10-27 2008-05-15 Chevron Oronite Company Llc Lubricating oil additive composition and method of making the same
EP1927650A1 (en) 2006-10-27 2008-06-04 Chevron Oronite Company LLC A lubricating oil additive composition and method of making the same
US7820605B2 (en) 2006-10-27 2010-10-26 Chevron Oronite Company Llc Lubricating oil additive composition and method of making the same
US20080103075A1 (en) * 2006-10-27 2008-05-01 Chevron Oronite Company Llc Lubricating oil additive composition and method of making the same
US20080103076A1 (en) * 2006-10-27 2008-05-01 Chevron Oronite Company Llc Lubricating oil additive composition and method of making the same
US7820604B2 (en) 2006-10-27 2010-10-26 Chevron Oronite Company Llc Lubricating oil additive composition and method of making the same
US20080113889A1 (en) * 2006-10-27 2008-05-15 Chevron Oronite Company Llc lubricating oil additive composition and method of making the same
US7858566B2 (en) 2006-10-27 2010-12-28 Chevron Oronite Company Llc Lubricating oil additive composition and method of making the same
US8067347B2 (en) 2006-10-27 2011-11-29 Chevron Oronite Company Llc Lubricating oil additive composition and method of making the same
US8425772B2 (en) 2006-12-12 2013-04-23 Cummins Filtration Ip, Inc. Filtration device with releasable additive
EP1947161A1 (en) 2006-12-13 2008-07-23 Infineum International Limited Fuel oil compositions
EP1942177A2 (en) 2006-12-19 2008-07-09 Chevron Oronite Company LLC Lubricating oil providing enhanced piston cleanliness
EP1947164A1 (en) 2006-12-21 2008-07-23 Chevron Oronite Technology B.V. Engine lubricant with enhanced thermal stability
US7700673B2 (en) 2006-12-22 2010-04-20 Bridgestone Corporation Reduced oil rubber compositions including N-substituted polyalkylene succinimide derivates and methods for preparing such compositions
US20080153972A1 (en) * 2006-12-22 2008-06-26 Xiaorong Wang Reduced Oil Rubber Compositions Including N-Substituted Polyalkylene Succinimide Derivates and Methods For Preparing Such Compositions
US20080182768A1 (en) * 2007-01-31 2008-07-31 Devlin Cathy C Lubricant composition for bio-diesel fuel engine applications
DE102008005330A1 (en) 2007-01-31 2008-08-07 Afton Chemical Corp. Lubricant composition for biodiesel fuel engine uses
EP1959003A2 (en) 2007-02-08 2008-08-20 Infineum International Limited Soot dispersants and lubricating oil compositions containing same
EP1970430A2 (en) 2007-03-09 2008-09-17 Afton Chemical Corporation Fuel composition containing a hydrocarbyl-substituted succinimide
US9011556B2 (en) 2007-03-09 2015-04-21 Afton Chemical Corporation Fuel composition containing a hydrocarbyl-substituted succinimide
US20080241095A1 (en) * 2007-03-26 2008-10-02 Syrinek Allen R Antifoulant for hydrocarbon processing equipment
US7682491B2 (en) 2007-03-26 2010-03-23 Nalco Company Antifoulant for hydrocarbon processing equipment
US20080274921A1 (en) * 2007-05-04 2008-11-06 Ian Macpherson Environmentally-Friendly Lubricant Compositions
EP2017329A1 (en) 2007-05-04 2009-01-21 Afton Chemical Corporation Environmentally-Friendly Lubricant Compositions
US20100152078A1 (en) * 2007-05-04 2010-06-17 Ian Macpherson Environmentally-friendly lubricant compositions
EP2420553A1 (en) 2007-05-04 2012-02-22 Afton Chemical Corporation Environmentally-Friendly Lubricant Compositions
CN101402889B (en) * 2007-05-22 2013-05-22 雅富顿公司 Fuel additive to control deposit formation
US20110010985A1 (en) * 2007-05-22 2011-01-20 Peter Wangqi Hou Fuel Additive to Control Deposit Formation
US20080289249A1 (en) * 2007-05-22 2008-11-27 Peter Wangqi Hou Fuel additive to control deposit formation
EP2000523A1 (en) 2007-05-30 2008-12-10 Chevron Oronite S.A. Lubricating oil with enhanced protection against wear and corrosion
WO2008154334A1 (en) 2007-06-08 2008-12-18 Infineum International Limited Additives and lubricating oil compositions containing same
EP2009082A2 (en) 2007-06-20 2008-12-31 Chevron Oronite Company LLC Synergistic lubricating oil composition containing a mixture of a nitro-substituted diarylamine and a diarylamine
EP2302020A1 (en) 2007-07-28 2011-03-30 Innospec Limited Use of additives for improving oxidation stability of a fuel oil composition
EP2025737A1 (en) 2007-08-01 2009-02-18 Afton Chemical Corporation Environmentally-friendly fuel compositions
US20090031614A1 (en) * 2007-08-01 2009-02-05 Ian Macpherson Environmentally-Friendly Fuel Compositions
US20090071067A1 (en) * 2007-09-17 2009-03-19 Ian Macpherson Environmentally-Friendly Additives And Additive Compositions For Solid Fuels
EP2042582A2 (en) 2007-09-24 2009-04-01 Afton Chemical Corporation Surface passivation and to methods for the reduction of fuel thermal degradation deposits
KR101766986B1 (en) 2007-09-27 2017-08-09 이노스펙 리미티드 Fuel compositions
US9157041B2 (en) 2007-09-27 2015-10-13 Innospec Limited Fuel compositions
US9315752B2 (en) 2007-09-27 2016-04-19 Innospec Limited Fuel compositions
US9034060B2 (en) 2007-09-27 2015-05-19 Innospec Fuel Specialties Llc Additives for diesel engines
US20100299992A1 (en) * 2007-09-27 2010-12-02 Jacqueline Reid Fuel compositions
US20100293844A1 (en) * 2007-09-27 2010-11-25 Macmillan John Alexander Additives for Diesel Engines
US9243199B2 (en) 2007-09-27 2016-01-26 Innospec Limited Fuel compositions
US9163190B2 (en) 2007-09-27 2015-10-20 Innospec Limited Fuel compositions
US20100258070A1 (en) * 2007-09-27 2010-10-14 Innospec Limited Fuel compositions
US20090093384A1 (en) * 2007-10-03 2009-04-09 The Lubrizol Corporation Lubricants That Decrease Micropitting for Industrial Gears
US20090156445A1 (en) * 2007-12-13 2009-06-18 Lam William Y Lubricant composition suitable for engines fueled by alternate fuels
EP2072611A1 (en) 2007-12-13 2009-06-24 Afton Chemical Corporation Lubricant composition suitable for engines fueled by alternate fuels
EP2078745A1 (en) 2007-12-20 2009-07-15 Chevron Oronite Company LLC Lubricating oil compositions comprising a molybdenum compound and a zinc dialkyldithiophosphate
US20100331224A1 (en) * 2007-12-20 2010-12-30 Boffa Alexander B Lubricating Oil Compositions Comprising A Molybdenum Compound And A Zinc Dialkyldithiophosphate
EP2077315A1 (en) 2007-12-20 2009-07-08 Chevron Oronite Company LLC Lubricating oil compositions containing a tetraalkyl-napthalene-1,8 diamine antioxidant
EP2075264A1 (en) 2007-12-26 2009-07-01 Infineum International Limited Method of forming polyalkene substituted carboxylic acid compositions
US9637613B2 (en) 2007-12-31 2017-05-02 Bridgestone Corporation Metal soaps incorporated in rubber compositions and method for incorporating such soaps in rubber compositions
US9090127B2 (en) 2007-12-31 2015-07-28 Bridgestone Corporation Metal soaps incorporated in rubber compositions and method for incorporating such soaps in rubber compositions
EP2083063A1 (en) 2008-01-22 2009-07-29 Infineum International Limited Lubricating oil composition
US8420583B2 (en) 2008-01-24 2013-04-16 Afton Chemical Corporation Olefin copolymer dispersant VI improver and lubricant compositions and uses thereof
US20090192061A1 (en) * 2008-01-24 2009-07-30 Boegner Philip J Olefin copolymer dispersant vi improver and lubricant compositions and uses thereof
EP2083024A1 (en) 2008-01-24 2009-07-29 Afton Chemical Corporation Olefin copolymer dispersant VI improver and lubricant compositions and uses thereof
EP2090642A1 (en) 2008-02-08 2009-08-19 Infineum International Limited Engine lubrication
US20090233822A1 (en) * 2008-03-11 2009-09-17 Afton Chemical Corporation Ultra-low sulfur clutch-only transmission fluids
DE102009012567A1 (en) 2008-03-11 2009-10-01 Afton Chemical Corp. Clutch-only transmission fluid useful for lubrication comprises oil formulated with additive components having metal detergent, phosphorus-based wear preventative, phosphorylated and boronated dispersant, sulfurized extreme pressure agent
US8546311B2 (en) 2008-03-11 2013-10-01 Volkswagen Aktiengesellsschaft Method for lubricating a clutch-only automatic transmission component requiring lubrication
DE102009001301A1 (en) 2008-03-11 2009-09-24 Volkswagen Ag Method for lubricating a component only for the clutch of an automatic transmission, which requires lubrication
US8703669B2 (en) 2008-03-11 2014-04-22 Afton Chemical Corporation Ultra-low sulfur clutch-only transmission fluids
WO2009119831A1 (en) 2008-03-28 2009-10-01 富士フイルム株式会社 Composition and method for forming coating film
EP2107102A2 (en) 2008-04-04 2009-10-07 Afton Chemical Corporation A succinimide lubricity additive for diesel fuel
US20090249683A1 (en) * 2008-04-04 2009-10-08 Schwab Scott D Succinimide lubricity additive for diesel fuel and a method for reducing wear scarring in an engine
US8690968B2 (en) * 2008-04-04 2014-04-08 Afton Chemical Corporation Succinimide lubricity additive for diesel fuel and a method for reducing wear scarring in an engine
US8455568B2 (en) 2008-04-25 2013-06-04 Chevron Oronite Company Llc Lubricating oil additive composition and method of making the same
US20090270531A1 (en) * 2008-04-25 2009-10-29 Chevron Oronite Company Llc Lubricating oil additive composition and method of making the same
US7883638B2 (en) 2008-05-27 2011-02-08 Dober Chemical Corporation Controlled release cooling additive compositions
US8591747B2 (en) 2008-05-27 2013-11-26 Dober Chemical Corp. Devices and methods for controlled release of additive compositions
US8702995B2 (en) 2008-05-27 2014-04-22 Dober Chemical Corp. Controlled release of microbiocides
EP2133406A1 (en) * 2008-06-09 2009-12-16 Idemitsu Kosan Co., Ltd. Lubricating oil composition for internal combustion engine
US20110098378A1 (en) * 2008-06-26 2011-04-28 Xiaorong Wang Rubber compositions including metal-functionalized polyisobutylene derivatives and methods for preparing such compositions
US8546464B2 (en) 2008-06-26 2013-10-01 Bridgestone Corporation Rubber compositions including metal-functionalized polyisobutylene derivatives and methods for preparing such compositions
WO2010005947A2 (en) 2008-07-11 2010-01-14 Innospec Fuel Specialties, LLC Fuel composition with enhanced low temperature properties
JP2010047747A (en) * 2008-07-22 2010-03-04 Sanyo Chem Ind Ltd Lubricant additive and lubricant composition
US20100075876A1 (en) * 2008-09-24 2010-03-25 David John Claydon Fuel compositions
US8709108B2 (en) 2008-09-24 2014-04-29 Afton Chemical Corporation Fuel compositions
US20100081588A1 (en) * 2008-09-30 2010-04-01 Chevron Oronite Company Llc Lubricating oil compositions
US9029304B2 (en) 2008-09-30 2015-05-12 Chevron Oronite Company Llc Lubricating oil additive composition and method of making the same
US8153566B2 (en) 2008-09-30 2012-04-10 Cherron Oronite Company LLC Lubricating oil compositions
US20100081594A1 (en) * 2008-09-30 2010-04-01 Chevron Oronite Company Llc Lubricating oil additive composition and method of making the same
EP3127992A1 (en) 2008-10-10 2017-02-08 The Lubrizol Corporation Additives to reduce metal pick-up in fuels
EP3486300A1 (en) 2008-10-10 2019-05-22 The Lubrizol Corporation Additives to reduce metal pick-up in fuels
US20100160193A1 (en) * 2008-12-22 2010-06-24 Chevron Oronite LLC Additive composition and method of making the same
US8748359B2 (en) 2008-12-22 2014-06-10 Chevron Oronite Company Llc Post-treated additive composition and method of making the same
EP2199377A1 (en) 2008-12-22 2010-06-23 Infineum International Limited Additives for fuel oils
US8859473B2 (en) 2008-12-22 2014-10-14 Chevron Oronite Company Llc Post-treated additive composition and method of making the same
US20100160194A1 (en) * 2008-12-22 2010-06-24 Chevron Oronite LLC Post-treated additive composition and method of making the same
WO2010074996A2 (en) 2008-12-22 2010-07-01 Chevron Oronite Company Llc A post-treated additive composition and method of making the same
US20100160192A1 (en) * 2008-12-22 2010-06-24 Chevron Oronite LLC lubricating oil additive composition and method of making the same
US20100206260A1 (en) * 2009-02-18 2010-08-19 Chevron Oronite Company Llc Method for preventing exhaust valve seat recession
WO2010096472A2 (en) 2009-02-18 2010-08-26 Chevron Oronite Company Llc Method for preventing exhaust valve seat recession
US8969273B2 (en) 2009-02-18 2015-03-03 Chevron Oronite Company Llc Lubricating oil compositions
US9394499B2 (en) 2009-02-25 2016-07-19 Innospec Limited Methods relating to fuel compositions
US9085740B2 (en) 2009-02-25 2015-07-21 Innospec Limited Methods relating to fuel compositions
EP2644684A1 (en) 2009-02-25 2013-10-02 Innospec Limited Methods and uses relating to fuel compositions
US20100234621A1 (en) * 2009-03-12 2010-09-16 Schertzer Bryan M Process for reacting an alpha, beta-unsaturated dicarboxylic acid compound with an ethylenically unsaturated hydrocarbon
US8242287B2 (en) 2009-03-12 2012-08-14 Nalco Company Process for reacting an α, β-unsaturated dicarboxylic acid compound with an ethylenically unsaturated hydrocarbon
WO2010104738A1 (en) 2009-03-12 2010-09-16 Nalco Company An improved process for reacting an a, b-unsaturated dicarboxylic acid compound with an ethylenically unsaturated hydrocarbon
US10308593B2 (en) 2009-03-18 2019-06-04 Infineum International Limited Additives for fuel oils
EP2236590A1 (en) 2009-04-01 2010-10-06 Infineum International Limited Lubricating oil composition
WO2010115594A1 (en) 2009-04-07 2010-10-14 Infineum International Limited Marine engine lubrication
EP3381998A1 (en) 2009-05-15 2018-10-03 The Lubrizol Corporation Quaternary ammonium ester salts
WO2010136822A2 (en) 2009-05-29 2010-12-02 Innospec Limited Method and use
WO2010139994A1 (en) 2009-06-01 2010-12-09 Innospec Limited Improvements in efficiency
US20120260876A1 (en) * 2009-06-01 2012-10-18 Innospec Limited Method of increasing fuel efficiency
EP3587458A1 (en) 2009-06-16 2020-01-01 Chevron Phillips Chemical Company LP Compositions comprising polyalphaolefins
WO2010147993A1 (en) 2009-06-16 2010-12-23 Chevron Phillips Chemical Company Lp Oligomerization of alpha olefins using metallocene-ssa catalyst systems and use of the resultant polyalphaolefins to prepare lubricant blends
US8389609B2 (en) 2009-07-01 2013-03-05 Bridgestone Corporation Multiple-acid-derived metal soaps incorporated in rubber compositions and method for incorporating such soaps in rubber compositions
US20110039994A1 (en) * 2009-07-01 2011-02-17 Xiaorong Wang Multiple-Acid-Derived Metal Soaps Incorporated In Rubber Compositions And Method For Incorporating Such Soaps In Rubber Compositions
EP2290040A1 (en) 2009-07-31 2011-03-02 Chevron Japan Ltd. Friction modifier and transmission oil
EP3272840A1 (en) 2009-07-31 2018-01-24 Chevron Japan Ltd. Friction modifier and transmission oil
EP2290041A2 (en) 2009-08-24 2011-03-02 Infineum International Limited A lubricating oil composition
EP2913387A1 (en) 2009-09-02 2015-09-02 Chevron Oronite Company LLC Natural gas engine lubricating oil compositions
US20110060062A1 (en) * 2009-09-10 2011-03-10 Bridgestone Corporation Compositions and method for making hollow nanoparticles from metal soaps
US9803060B2 (en) 2009-09-10 2017-10-31 Bridgestone Corporation Compositions and method for making hollow nanoparticles from metal soaps
DE202009013309U1 (en) 2009-10-05 2010-03-04 Afton Chemical Corp. Fuel and fuel compositions
EP2169034A2 (en) 2009-10-05 2010-03-31 Afton Chemical Corporation Fuel compositions
US20110105371A1 (en) * 2009-11-05 2011-05-05 Afton Chemical Corporation Olefin copolymer vi improvers and lubricant compositions and uses thereof
EP2325291A1 (en) 2009-11-05 2011-05-25 Afton Chemical Corporation Olefin Copolymer VI improvers and lubricant compositions and uses thereof
US8415284B2 (en) 2009-11-05 2013-04-09 Afton Chemical Corporation Olefin copolymer VI improvers and lubricant compositions and uses thereof
WO2011059626A1 (en) 2009-11-10 2011-05-19 The Lubrizol Corporation Lubricant system clean-up compositions and methods thereof
US8486877B2 (en) 2009-11-18 2013-07-16 Chevron Oronite Company Llc Alkylated hydroxyaromatic compound substantially free of endocrine disruptive chemicals
US20110118160A1 (en) * 2009-11-18 2011-05-19 Chevron Oronite Company Llc Alkylated hydroxyaromatic compound substantially free of endocrine disruptive chemicals
US8709984B2 (en) 2009-12-15 2014-04-29 Chevron Oronite Company Llc Lubricating oil compositions
US9062273B2 (en) 2009-12-15 2015-06-23 Chevron Oronite Company Llc Lubricating oil compositions containing titanium complexes
US20110143980A1 (en) * 2009-12-15 2011-06-16 Chevron Oronite Company Llc Lubricating oil compositions containing titanium complexes
US20110143979A1 (en) * 2009-12-15 2011-06-16 Chevron Oronite Company Llc Lubricating oil compositions
US8969265B2 (en) 2009-12-15 2015-03-03 Chevron Oronite Company Llc Lubricating oil compositions
EP3447111A1 (en) 2010-03-10 2019-02-27 Innospec Limited Fuel composition comprising detergent and quaternary ammonium salt additive
EP2966151A1 (en) 2010-03-10 2016-01-13 Innospec Limited Fuel composition comprising detergent and quaternary ammonium salt additive
WO2011110860A1 (en) 2010-03-10 2011-09-15 Innospec Limited Fuel composition comprising detergent and quaternary ammonium salt additive
US8933001B2 (en) 2010-03-31 2015-01-13 Chevron Oronite Company Llc Method for improving fluorocarbon elastomer seal compatibility
US9150811B2 (en) 2010-03-31 2015-10-06 Cherron Oronite Company LLC Method for improving copper corrosion performance
US8841243B2 (en) 2010-03-31 2014-09-23 Chevron Oronite Company Llc Natural gas engine lubricating oil compositions
US8901050B2 (en) 2010-03-31 2014-12-02 Chevron Oronite Company Llc Method for improving copper corrosion performance
US8993496B2 (en) 2010-03-31 2015-03-31 Chevron Oronite Company Llc Method for improving fluorocarbon elastomer seal compatibility
WO2011126641A2 (en) 2010-03-31 2011-10-13 Chevron Oronite Company Llc Method for improving copper corrosion performance
WO2011126642A2 (en) 2010-03-31 2011-10-13 Chevron Oronite Company Llc Method for improving copper corrosion performance
US9932536B2 (en) 2010-05-10 2018-04-03 Innospec Limited Gasoline composition, method and use
US9493720B2 (en) 2010-05-10 2016-11-15 Innospec Limited Gasoline composition, method and use
WO2011141731A1 (en) 2010-05-10 2011-11-17 Innospec Limited Composition, method and use
WO2011143051A1 (en) 2010-05-12 2011-11-17 The Lubrizol Corporation Tartaric acid derivatives in hths fluids
WO2011146289A1 (en) 2010-05-18 2011-11-24 The Lubrizol Corporation Methods and compositions that provide detergency
EP3705555A1 (en) 2010-05-25 2020-09-09 The Lubrizol Corporation Method to provide power gain in an engine
WO2011149799A1 (en) 2010-05-25 2011-12-01 The Lubrizol Corporation Method to provide power gain in an engine
WO2011159742A1 (en) 2010-06-15 2011-12-22 The Lubrizol Corporation Methods of removing deposits in oil and gas applications
US8318643B2 (en) 2010-06-29 2012-11-27 Cherron Oronite Technology B.V. Trunk piston engine lubricating oil compositions
EP2402421A2 (en) 2010-06-29 2012-01-04 Chevron Oronite Technology B.V. Trunk Piston Engine Lubricating Oil Compositions
EP3070153A1 (en) 2010-09-07 2016-09-21 The Lubrizol Corporation Hydroxychroman derivatives as antioxidants
WO2012033668A1 (en) 2010-09-07 2012-03-15 The Lubrizol Corporation Hydroxychroman derivatives as engine oil antioxidants
WO2012051075A2 (en) 2010-10-12 2012-04-19 Chevron Oronite Company Llc Lubricating composition containing multifunctional borated hydroxylated amine salt of a hindered phenolic acid
WO2012051064A2 (en) 2010-10-12 2012-04-19 Chevron Oronite Company Llc Lubricating composition containing multifunctional hydroxylated amine salt of a hindered phenolic acid
US8796192B2 (en) 2010-10-29 2014-08-05 Chevron Oronite Company Llc Natural gas engine lubricating oil compositions
US8703680B2 (en) 2010-11-24 2014-04-22 Chevron Oronite Company Llc Lubricating composition containing friction modifier blend
WO2012076896A1 (en) 2010-12-09 2012-06-14 Innospec Limited Improvements in or relating to additives for fuels and lubricants
US8716202B2 (en) 2010-12-14 2014-05-06 Chevron Oronite Company Llc Method for improving fluorocarbon elastomer seal compatibility
WO2012084906A1 (en) 2010-12-22 2012-06-28 Rhodia Operations Fuel additive composition containing a dispersion of iron particles and a detergent
EP3348626A1 (en) 2010-12-22 2018-07-18 Rhodia Operations Use of a fuel additive composition based on a dispersion of particles of iron and a detergent
US8802755B2 (en) 2011-01-18 2014-08-12 Bridgestone Corporation Rubber compositions including metal phosphate esters
EP2479245A1 (en) 2011-01-19 2012-07-25 Afton Chemical Corporation Fuel additives and gasoline containing the additives
WO2012099734A2 (en) 2011-01-21 2012-07-26 Chevron Oronite Company Llc Improved process for preparation of low molecular weight molybdenum succinimide complexes
US8476460B2 (en) 2011-01-21 2013-07-02 Chevron Oronite Company Llc Process for preparation of low molecular weight molybdenum succinimide complexes
US8426608B2 (en) 2011-01-21 2013-04-23 Chevron Oronite Company Llc Process for preparation of high molecular weight molybdenum succinimide complexes
WO2012099736A2 (en) 2011-01-21 2012-07-26 Chevron Oronite Company Llc Improved process for preparation of high molecular weight molybdenum succinimide complexes
US9523057B2 (en) 2011-02-22 2016-12-20 Afton Chemical Corporation Fuel additives to maintain optimum injector performance
US8702968B2 (en) 2011-04-05 2014-04-22 Chevron Oronite Technology B.V. Low viscosity marine cylinder lubricating oil compositions
WO2012162020A1 (en) 2011-05-26 2012-11-29 The Lubrizol Corporation Stabilized blends containing antioxidants
WO2012162027A1 (en) 2011-05-26 2012-11-29 The Lubrizol Corporation Stabilized blends containing friction modifiers
WO2012162219A1 (en) 2011-05-26 2012-11-29 The Lubrizol Corporation Stabilized blends containing friction modifiers
WO2012162282A1 (en) 2011-05-26 2012-11-29 The Lubrizol Corporation Stabilized blends containing friction modifiers
WO2012177529A1 (en) 2011-06-21 2012-12-27 The Lubrizol Corporation Lubricating compositions containing salts of hydrocarbyl substituted acylating agents
WO2013003406A1 (en) 2011-06-29 2013-01-03 Exxonmobil Research And Engineering Company Low viscosity engine oil with superior engine wear protection
WO2013003392A1 (en) 2011-06-30 2013-01-03 Exxonmobil Research And Engineering Company Method of improving pour point of lubricating compositions containing polyalkylene glycol mono ethers
US8586520B2 (en) 2011-06-30 2013-11-19 Exxonmobil Research And Engineering Company Method of improving pour point of lubricating compositions containing polyalkylene glycol mono ethers
WO2013003394A1 (en) 2011-06-30 2013-01-03 Exxonmobil Research And Engineering Company Lubricating compositions containing polyetheramines
WO2013003405A1 (en) 2011-06-30 2013-01-03 Exxonmobil Research And Engineering Company Lubricating compositions containing polyalkylene glycol mono ethers
WO2013043332A1 (en) 2011-09-23 2013-03-28 The Lubrizol Corporation Quaternary ammonium salts in heating oils
WO2013055480A1 (en) 2011-10-10 2013-04-18 Exxonmobil Research And Engineering Company Low viscosity engine oil compositions
WO2013055482A1 (en) 2011-10-10 2013-04-18 Exxonmobil Research And Engineering Company Lubricating compositions
WO2013055481A1 (en) 2011-10-10 2013-04-18 Exxonmobil Research And Engineering Company High efficiency engine oil compositions
WO2013066915A1 (en) 2011-11-01 2013-05-10 Exxonmobil Research And Engineering Company Lubricants with improved low-temperature fuel economy
US8933002B2 (en) 2011-11-10 2015-01-13 Chevron Oronite Company Llc Lubricating oil compositions
WO2013074498A1 (en) 2011-11-14 2013-05-23 Exxonmobil Research And Engineering Company Method for improving engine fuel efficiency
EP2604676A1 (en) 2011-12-16 2013-06-19 Chevron Oronite Technology B.V. Trunk piston engine lubricating oil compositions
US9206374B2 (en) 2011-12-16 2015-12-08 Chevron Oronite Sas Trunk piston engine lubricating oil compositions
WO2013096532A1 (en) 2011-12-22 2013-06-27 Exxonmobil Research And Engineering Company Method for improving engine fuel efficiency
US9249091B2 (en) 2011-12-27 2016-02-02 Chevron Oronite Company Llc Post-treated sulfurized salt of an alkyl-substituted hydroxyaromatic composition
WO2013123102A2 (en) 2012-02-17 2013-08-22 The Lubrizol Corporation Lubricating composition including esterified copolymer and low dispersant levels suitable for driveline applications
WO2013123160A1 (en) 2012-02-17 2013-08-22 The Lubrizol Corporation Mixtures of olefin-ester copolymer with polyolefin as viscosity modifier
WO2013181318A1 (en) 2012-06-01 2013-12-05 Exxonmobil Research And Engineering Company Lubricant compostions and processes for preparing same
US8703666B2 (en) 2012-06-01 2014-04-22 Exxonmobil Research And Engineering Company Lubricant compositions and processes for preparing same
WO2014008121A1 (en) 2012-07-02 2014-01-09 Exxonmobil Research And Engineering Company Enhanced durability performance of lubricants using functionalized metal phosphate nanoplatelets
US9228149B2 (en) 2012-07-02 2016-01-05 Exxonmobil Research And Engineering Company Enhanced durability performance of lubricants using functionalized metal phosphate nanoplatelets
WO2014047017A1 (en) 2012-09-24 2014-03-27 The Lubrizol Corporation Lubricant comprising a mixture of an olefin-ester copolymer with an ethylene alpha-olefin copolymer
EP3489332A1 (en) 2012-10-23 2019-05-29 The Lubrizol Corporation Diesel detergent without a low molecular weight penalty
WO2014066344A1 (en) 2012-10-23 2014-05-01 The Lubrizol Corporation Diesel detergent without a low molecular weight penalty
US9487729B2 (en) 2012-10-24 2016-11-08 Exxonmobil Chemical Patents Inc. Functionalized polymers and oligomers as corrosion inhibitors and antiwear additives
WO2014066444A1 (en) 2012-10-24 2014-05-01 Exxonmobil Research And Engineering Comapny Functionalized polymers and oligomers as corrosion inhibitors and antiwear additives
US9670341B2 (en) 2012-11-02 2017-06-06 Bridgestone Corporation Rubber compositions comprising metal carboxylates and processes for making the same
EP2727984A1 (en) 2012-11-02 2014-05-07 Infineum International Limited Marine engine lubrication
EP2735603A1 (en) 2012-11-21 2014-05-28 Infineum International Limited Marine engine lubrication
WO2014107315A1 (en) 2013-01-04 2014-07-10 Exxonmobil Research And Engineering Company Method for improving engine fuel efficiency
EP2765179A1 (en) 2013-02-07 2014-08-13 Infineum International Limited Marine engine lubrication
WO2014137800A1 (en) 2013-03-07 2014-09-12 The Lubrizol Corporation Ion tolerant corrosion inhibitors and inhibitor combinations for fuels
US9149814B2 (en) 2013-03-13 2015-10-06 Ecolab Usa Inc. Composition and method for improvement in froth flotation
WO2014158533A1 (en) 2013-03-14 2014-10-02 Exxonmobil Research And Engineering Company Lubricating composition providing high wear resistance
US9434906B2 (en) 2013-03-25 2016-09-06 Chevron Oronite Company, Llc Marine diesel engine lubricating oil compositions
WO2014193692A1 (en) 2013-05-28 2014-12-04 The Lubrizol Corporation Asphaltene inhibition
US10669507B2 (en) 2013-09-23 2020-06-02 Chevron Japan Ltd. Fuel economy engine oil composition
EP2851413A1 (en) 2013-09-23 2015-03-25 Chevron Japan Ltd. Fuel economy engine oil composition
EP2851412A1 (en) 2013-09-24 2015-03-25 Infineum International Limited Marine engine lubrication
WO2015050690A1 (en) 2013-10-03 2015-04-09 Exxonmobil Research And Engineering Company Compositions with improved varnish control properties
US9909079B2 (en) 2013-10-18 2018-03-06 Chevron Oronite Company Llc Lubricating oil composition for protection of silver bearings in medium speed diesel engines
US9062271B2 (en) 2013-10-30 2015-06-23 Chevron Oronite Technology B.V. Process for preparing an overbased salt of a sulfurized alkyl-substituted hydroxyaromatic composition
US10669506B2 (en) 2013-11-06 2020-06-02 Chevron Oronite Technology B.V. Marine diesel cylinder lubricant oil compositions
US10364403B2 (en) 2013-11-06 2019-07-30 Chevron Oronite Technology B.V. Marine diesel cylinder lubricant oil compositions
US10457884B2 (en) 2013-11-18 2019-10-29 Afton Chemical Corporation Mixed detergent composition for intake valve deposit control
WO2015073296A2 (en) 2013-11-18 2015-05-21 Russo Joseph M Mixed detergent composition for intake valve deposit control
US9708549B2 (en) 2013-12-18 2017-07-18 Chevron Phillips Chemical Company Lp Method for making polyalphaolefins using aluminum halide catalyzed oligomerization of olefins
WO2015095336A1 (en) 2013-12-18 2015-06-25 Chevron Phillips Chemical Company Lp Method for making polyolefins using aluminum halide catalyzed oligomerization of olefins
WO2015099821A1 (en) 2013-12-23 2015-07-02 Exxonmobil Research And Engineering Company Method for improving engine fuel efficiency
WO2015099907A1 (en) 2013-12-23 2015-07-02 Exxonmobil Research And Engineering Company Low viscosity ester lubricant and method for using
WO2015099820A1 (en) 2013-12-23 2015-07-02 Exxonmobil Research And Engineering Company Method for improving engine fuel efficiency
WO2015099819A1 (en) 2013-12-23 2015-07-02 Exxonmobil Research And Engineering Company Method for improving engine fuel efficiency
US9885004B2 (en) 2013-12-23 2018-02-06 Exxonmobil Research And Engineering Company Method for improving engine fuel efficiency
US10208269B2 (en) 2013-12-23 2019-02-19 Exxonmobil Research And Engineering Company Low viscosity ester lubricant and method for using
US9506008B2 (en) 2013-12-23 2016-11-29 Exxonmobil Research And Engineering Company Method for improving engine fuel efficiency
US10190072B2 (en) 2013-12-23 2019-01-29 Exxonmobil Research And Engineering Company Method for improving engine fuel efficiency
WO2015134129A2 (en) 2014-03-05 2015-09-11 The Lubrizol Corporation Emulsifier components and methods of using the same
EP3415589A1 (en) 2014-04-29 2018-12-19 Infineum International Limited Lubricating oil compositions
EP2940110A1 (en) 2014-04-29 2015-11-04 Infineum International Limited Lubricating oil compositions
WO2015171292A1 (en) 2014-05-08 2015-11-12 Exxonmobil Research And Engineering Company Method for preventing or reducing engine knock and pre-ignition
US9896634B2 (en) 2014-05-08 2018-02-20 Exxonmobil Research And Engineering Company Method for preventing or reducing engine knock and pre-ignition
WO2015171980A1 (en) 2014-05-09 2015-11-12 Exxonmobil Research And Engineering Company Method for preventing or reducing low speed pre-ignition
WO2015171981A1 (en) 2014-05-09 2015-11-12 Exxonmobil Research And Engineering Company Method for preventing or reducing low speed pre-ignition
US10519394B2 (en) 2014-05-09 2019-12-31 Exxonmobil Research And Engineering Company Method for preventing or reducing low speed pre-ignition while maintaining or improving cleanliness
WO2015171978A1 (en) 2014-05-09 2015-11-12 Exxonmobil Research And Engineering Company Method for preventing or reducing low speed pre-ignition
WO2015183455A1 (en) 2014-05-29 2015-12-03 Exxonmobil Research And Engineering Company Lubricating oil compositions with engine wear protection
US9506009B2 (en) 2014-05-29 2016-11-29 Exxonmobil Research And Engineering Company Lubricating oil compositions with engine wear protection
EP3536766A1 (en) 2014-05-30 2019-09-11 The Lubrizol Corporation Epoxide quaternized quaternary ammonium salts
WO2015184276A1 (en) 2014-05-30 2015-12-03 The Lubrizol Corporation Epoxide quaternized quaternary ammonium salts
WO2015183908A1 (en) 2014-05-30 2015-12-03 The Lubrizol Corporation Low molecular weight imide containing quaternary ammonium salts
EP3511396A1 (en) 2014-05-30 2019-07-17 The Lubrizol Corporation Low molecular weight imide containing quaternary ammonium salts
EP3524663A1 (en) 2014-05-30 2019-08-14 The Lubrizol Corporation Imidazole containing quaternary ammonium salts
WO2015184301A2 (en) 2014-05-30 2015-12-03 The Lubrizol Corporation Coupled quaternary ammonium salts
WO2015184251A1 (en) 2014-05-30 2015-12-03 The Lubrizol Corporation Branched amine containing quaternary ammonium salts
WO2015184280A1 (en) 2014-05-30 2015-12-03 The Lubrizol Corporation Imidazole containing quaternary ammonium salts
EP3521404A1 (en) 2014-05-30 2019-08-07 The Lubrizol Corporation Low molecular weight imide containing quaternary ammonium salts
WO2015183916A1 (en) 2014-05-30 2015-12-03 The Lubrizol Corporation Low molecular weight amide/ester containing quaternary ammonium salts
EP3517593A1 (en) 2014-05-30 2019-07-31 The Lubrizol Corporation Low molecular weight amide/ester containing quaternary ammonium salts
WO2015184247A1 (en) 2014-05-30 2015-12-03 The Lubrizol Corporation High molecular weight imide containing quaternary ammonium salts
WO2015184254A1 (en) 2014-05-30 2015-12-03 The Lubrizol Corporation High molecular weight amide/ester containing quaternary ammonium salts
EP3514220A1 (en) 2014-05-30 2019-07-24 The Lubrizol Corporation Low molecular weight amide/ester containing quaternary ammonium salts
WO2016018462A1 (en) 2014-07-31 2016-02-04 Chevron U.S.A. Inc. Sae 15w-30 lubricating oil composition having improved oxidative stability
US10689593B2 (en) 2014-08-15 2020-06-23 Exxonmobil Research And Engineering Company Low viscosity lubricating oil compositions for turbomachines
US10450525B2 (en) 2014-08-27 2019-10-22 Chevron Oronite Company Llc Process for alaknolamide synthesis
US9944877B2 (en) 2014-09-17 2018-04-17 Exxonmobil Research And Engineering Company Composition and method for preventing or reducing engine knock and pre-ignition in high compression spark ignition engines
WO2016043944A1 (en) 2014-09-17 2016-03-24 Exxonmobil Research And Engineering Company Composition and method for preventing or reducing engine knock and pre-ignition in high compression spark ignition engines
US9957459B2 (en) 2014-11-03 2018-05-01 Exxonmobil Research And Engineering Company Low transition temperature mixtures or deep eutectic solvents and processes for preparation thereof
WO2016073149A1 (en) 2014-11-03 2016-05-12 Exxonmobil Research And Engineering Company Low transition temperature mixtures or deep eutectic solvents and processes for preparation thereof
US10920161B2 (en) 2014-11-03 2021-02-16 Exxonmobil Research And Engineering Company Low transition temperature mixtures or deep eutectic solvents and processes for preparation thereof
EP4089158A1 (en) 2014-11-14 2022-11-16 Chevron Oronite Technology B.V. Low sulfur marine distillate fuel trunk piston engine oil composition
EP3020790A1 (en) 2014-11-14 2016-05-18 Chevron Oronite Technology B.V. Trunk piston engine oil composition for low sulfur marine distillate fueled engines
US9506007B2 (en) 2014-11-14 2016-11-29 Chevron Oronite Technology B.V. Low sulfur marine distillate fuel trunk piston engine oil composition
US9879202B2 (en) 2014-12-04 2018-01-30 Infineum International Limited Marine engine lubrication
US10364404B2 (en) 2014-12-04 2019-07-30 Infineum International Limited Marine engine lubrication
EP3029133A1 (en) 2014-12-04 2016-06-08 Infineum International Limited Marine engine lubrication
WO2016106211A1 (en) 2014-12-24 2016-06-30 Exxonmobil Research And Engineering Company Methods for authentication and identification of petroleum products
WO2016106214A1 (en) 2014-12-24 2016-06-30 Exxonmobil Research And Engineering Company Methods for determining condition and quality of petroleum products
WO2016109322A1 (en) 2014-12-30 2016-07-07 Exxonmobil Research And Engineering Company Lubricating oil compositions containing encapsulated microscale particles
WO2016109325A1 (en) 2014-12-30 2016-07-07 Exxonmobil Research And Engineering Company Lubricating oil compositions containing encapsulated microscale particles
WO2016109382A1 (en) 2014-12-30 2016-07-07 Exxonmobil Research And Engineering Company Lubricating oil compositions with engine wear protection
US10781397B2 (en) 2014-12-30 2020-09-22 Exxonmobil Research And Engineering Company Lubricating oil compositions with engine wear protection
US10000717B2 (en) 2014-12-30 2018-06-19 Exxonmobil Research And Engineering Company Lubricating oil compositions containing encapsulated microscale particles
US10066184B2 (en) 2014-12-30 2018-09-04 Exxonmobil Research And Engineering Company Lubricating oil compositions containing encapsulated microscale particles
US10000721B2 (en) 2014-12-30 2018-06-19 Exxonmobil Research And Engineering Company Lubricating oil compositions with engine wear protection
WO2016109376A1 (en) 2014-12-30 2016-07-07 Exxonmobil Research And Engineering Company Lubricating oil compositions with engine wear protection
US9926509B2 (en) 2015-01-19 2018-03-27 Exxonmobil Research And Engineering Company Lubricating oil compositions with engine wear protection and solubility
US9528074B2 (en) 2015-02-13 2016-12-27 Chevron Oronite Technology B.V. Lubricating oil compositions with enhanced piston cleanliness
US9528071B2 (en) 2015-02-13 2016-12-27 Chevron Oronite Technology B.V. Lubricating oil compositions with enhanced piston cleanliness
US10138438B2 (en) 2015-02-18 2018-11-27 Chevron Oronite Technology B.V. Low sulfur marine distillate fuel trunk piston engine oil composition
US10150930B2 (en) 2015-02-18 2018-12-11 Chevron Oronite Technology B.V. Low sulfur marine distillate fuel trunk piston engine oil composition
WO2016140998A1 (en) 2015-03-04 2016-09-09 Huntsman Petrochemical Llc Novel organic friction modifiers
EP3072948A1 (en) 2015-03-23 2016-09-28 Chevron Japan Ltd. Lubricating oil compositions for construction machines
EP3072949A1 (en) 2015-03-23 2016-09-28 Chevron Japan Ltd. Lubricating oil composition for construction machines
US10457887B2 (en) 2015-05-19 2019-10-29 Chevron Oronite Technology B.V. Trunk piston engine oil composition
WO2016191409A1 (en) 2015-05-28 2016-12-01 Exxonmobil Research And Engineering Company Composition and method for preventing or reducing engine knock and pre-ignition in high compression spark ignition engines
US10119093B2 (en) 2015-05-28 2018-11-06 Exxonmobil Research And Engineering Company Composition and method for preventing or reducing engine knock and pre-ignition in high compression spark ignition engines
WO2016200606A1 (en) 2015-06-09 2016-12-15 Exxonmobil Research And Engineering Company Inverse micellar compositions containing lubricant additives
WO2017007670A1 (en) 2015-07-07 2017-01-12 Exxonmobil Research And Engineering Company Composition and method for preventing or reducing engine knock and pre-ignition in high compression spark ignition engines
US10119090B2 (en) 2015-07-07 2018-11-06 Exxonmobil Research And Engineering Company Composition and method for preventing or reducing engine knock and pre-ignition in high compression spark ignition engines
WO2017013257A1 (en) 2015-07-22 2017-01-26 Chevron Oronite Technology B.V. Marine diesel cylinder lubricant oil compositions
US10407640B2 (en) 2015-07-22 2019-09-10 Chevron Oronite Technology B.V. Marine diesel cylinder lubricant oil compositions
US9732300B2 (en) 2015-07-23 2017-08-15 Chevron Phillipa Chemical Company LP Liquid propylene oligomers and methods of making same
US10435491B2 (en) 2015-08-19 2019-10-08 Chevron Phillips Chemical Company Lp Method for making polyalphaolefins using ionic liquid catalyzed oligomerization of olefins
EP3135750A1 (en) 2015-08-26 2017-03-01 Infineum International Limited Lubricating oil compositions
WO2017079123A1 (en) 2015-11-02 2017-05-11 Lubrizol Oilfield Solutions, Inc. Lubricant for water based drilling fluid
WO2017083042A1 (en) 2015-11-09 2017-05-18 The Lubrizol Corporation Using quaternary amine additives to improve water separation
WO2017096159A1 (en) 2015-12-02 2017-06-08 The Lubrizol Corporation Ultra-low molecular weight amide/ester containing quaternary ammonium salts having short hydrocarbon tails
WO2017096175A1 (en) 2015-12-02 2017-06-08 The Lubrizol Corporation Ultra-low molecular weight imide containing quaternary ammonium salts having short hydrocarbon tails
US10316712B2 (en) 2015-12-18 2019-06-11 Exxonmobil Research And Engineering Company Lubricant compositions for surface finishing of materials
US10550335B2 (en) 2015-12-28 2020-02-04 Exxonmobil Research And Engineering Company Fluxed deasphalter rock fuel oil blend component oils
US10947464B2 (en) 2015-12-28 2021-03-16 Exxonmobil Research And Engineering Company Integrated resid deasphalting and gasification
US10590360B2 (en) 2015-12-28 2020-03-17 Exxonmobil Research And Engineering Company Bright stock production from deasphalted oil
WO2017117178A1 (en) 2015-12-28 2017-07-06 Exxonmobil Research And Engineering Company Bright stock production from deasphalted oil
US10550341B2 (en) 2015-12-28 2020-02-04 Exxonmobil Research And Engineering Company Sequential deasphalting for base stock production
US10647925B2 (en) 2015-12-28 2020-05-12 Exxonmobil Research And Engineering Company Fuel components from hydroprocessed deasphalted oils
US10808185B2 (en) 2015-12-28 2020-10-20 Exxonmobil Research And Engineering Company Bright stock production from low severity resid deasphalting
US10377962B2 (en) 2016-02-26 2019-08-13 Exxonmobil Research And Engineering Company Lubricant compositions containing controlled release additives
WO2017146896A1 (en) 2016-02-26 2017-08-31 Exxonmobil Research And Engineering Company Lubricant compositions containing controlled release additives
US10377961B2 (en) 2016-02-26 2019-08-13 Exxonmobil Research And Engineering Company Lubricant compositions containing controlled release additives
WO2017146897A1 (en) 2016-02-26 2017-08-31 Exxonmobil Research And Engineering Company Lubricant compositions containing controlled release additives
WO2017172254A1 (en) 2016-03-31 2017-10-05 Exxonmobil Research And Engineering Company Lubricant compositions
US9951290B2 (en) 2016-03-31 2018-04-24 Exxonmobil Research And Engineering Company Lubricant compositions
US10494579B2 (en) 2016-04-26 2019-12-03 Exxonmobil Research And Engineering Company Naphthene-containing distillate stream compositions and uses thereof
WO2017223306A1 (en) 2016-06-22 2017-12-28 Lubrizol Oilfield Solutions, Inc. Gas hydrate inhibitors
WO2018013249A1 (en) 2016-07-12 2018-01-18 Chevron Phillips Chemical Company Lp Decene oligomers
US10647626B2 (en) 2016-07-12 2020-05-12 Chevron Phillips Chemical Company Lp Decene oligomers
WO2018013181A1 (en) 2016-07-13 2018-01-18 Chevron Oronite Company Llc Synergistic lubricating oil composition containing mixture of antioxidants
US10077410B2 (en) 2016-07-13 2018-09-18 Chevron Oronite Company Llc Synergistic lubricating oil composition containing mixture of antioxidants
WO2018026982A1 (en) 2016-08-03 2018-02-08 Exxonmobil Research And Engineering Company Lubricating engine oil for improved wear protection and fuel efficiency
US10640725B2 (en) 2016-08-05 2020-05-05 Rutgers, The State University Of New Jersey Thermocleavable friction modifiers and methods thereof
WO2018027227A1 (en) 2016-08-05 2018-02-08 Rutgers, The State University Of New Jersey Thermocleavable friction modifiers and methods thereof
WO2018039571A1 (en) 2016-08-25 2018-03-01 Evonik Degussa Gmbh Amine alkenyl substituted succinimide reaction product fuel additives, compositions, and methods
US10899985B2 (en) 2016-08-25 2021-01-26 Evonik Operations Gmbh Amine alkenyl substituted succinimide reaction product fuel additives, compositions, and methods
WO2018041732A1 (en) 2016-08-29 2018-03-08 Chevron Oronite Technology B.V. Marine diesel cylinder lubricant oil compositions
US11427780B2 (en) 2016-09-12 2022-08-30 The Lubrizol Corporation Total base number boosters for marine diesel engine lubricating compositions
WO2018048781A1 (en) 2016-09-12 2018-03-15 The Lubrizol Corporation Total base number boosters for marine diesel engine lubricating compositions
US10479956B2 (en) 2016-09-20 2019-11-19 Exxonmobil Research And Engineering Company Non-newtonian engine oil with superior engine wear protection and fuel economy
WO2018057377A1 (en) 2016-09-20 2018-03-29 Exxonmobil Research And Engineering Company Non-newtonian engine oil with superior engine wear protection and fuel economy
WO2018067908A1 (en) 2016-10-07 2018-04-12 Exxonmobil Research And Engineering Company Low conductivity lubricating oils for electric and hybrid vehicles
WO2018067903A1 (en) 2016-10-07 2018-04-12 Exxonmobil Research And Engineering Company Method for controlling electrical conductivity of lubricating oils in electric vehicle powertrains
WO2018067902A1 (en) 2016-10-07 2018-04-12 Exxonmobil Research And Engineering Company Lubricating oil compositions for electric vehicle powertrains
WO2018067906A1 (en) 2016-10-07 2018-04-12 Exxonmobil Research And Engineering Company High conductivity lubricating oils for electric and hybrid vehicles
WO2018067905A1 (en) 2016-10-07 2018-04-12 Exxonmobil Research And Engineering Company Method for preventing or minimizing electrostatic discharge and dielectric breakdown in electric vehicle powertrains
WO2018069460A1 (en) 2016-10-12 2018-04-19 Chevron Oronite Technology B.V. Marine diesel lubricant oil compositions
WO2018075147A1 (en) 2016-10-17 2018-04-26 The Lubrizol Corporation Acid emulsifier technology for continuous mixed emulsified acid systems
WO2018073268A1 (en) 2016-10-18 2018-04-26 Chevron Oronite Technology B.V. Marine diesel lubricant oil compositions
WO2018077621A1 (en) 2016-10-25 2018-05-03 Chevron Oronite Technology B.V. Lubricating oil compositions comprising a biodiesel fuel and a dispersant
US10781394B2 (en) 2016-10-25 2020-09-22 Chevron Oronite Technology B.V. Lubricating oil compositions comprising a biodiesel fuel and a Mannich condensation product
US10344245B2 (en) 2016-10-25 2019-07-09 Chevron Oronite Technology B.V. Lubricating oil compositions comprising a biodiesel fuel and a dispersant
WO2018101282A1 (en) 2016-11-30 2018-06-07 Chevron Japan Ltd. Lubricating oil compositions for motorcycles
US10829708B2 (en) 2016-12-19 2020-11-10 Exxonmobil Research And Engineering Company Composition and method for preventing or reducing engine knock and pre-ignition in high compression spark ignition engines
WO2018118477A1 (en) 2016-12-19 2018-06-28 Exxonmobil Research And Engineering Company Composition and method for preventing or reducing engine knock and pre-ignition compression spark ignition engines
US10647936B2 (en) 2016-12-30 2020-05-12 Exxonmobil Research And Engineering Company Method for improving lubricant antifoaming performance and filterability
WO2018125956A1 (en) 2016-12-30 2018-07-05 Exxonmobil Research And Engineering Company Low viscosity lubricating oil compositions for turbomachines
WO2018144166A1 (en) 2017-02-01 2018-08-09 Exxonmobil Research And Engineering Company Lubricating engine oil and method for improving engine fuel efficiency
WO2018144167A1 (en) 2017-02-01 2018-08-09 Exxonmobil Research And Engineering Company Lubricating engine oil and method for improving engine fuel efficiency
US10793801B2 (en) 2017-02-06 2020-10-06 Exxonmobil Chemical Patents Inc. Low transition temperature mixtures and lubricating oils containing the same
US10487289B2 (en) 2017-02-21 2019-11-26 Exxonmobil Research And Engineering Company Lubricating oil compositions and methods of use thereof
WO2018156304A1 (en) 2017-02-21 2018-08-30 Exxonmobil Research And Engineering Company Lubricating oil compositions and methods of use thereof
EP3369802A1 (en) 2017-03-01 2018-09-05 Infineum International Limited Improvements in and relating to lubricating compositions
US10273425B2 (en) 2017-03-13 2019-04-30 Afton Chemical Corporation Polyol carrier fluids and fuel compositions including polyol carrier fluids
EP3375848A1 (en) 2017-03-13 2018-09-19 Afton Chemical Corporation Polyol carrier fluids and fuel compositions including polyol carrier fluids
US10240102B2 (en) 2017-03-16 2019-03-26 Chevron Phillips Chemical Company, Lp Lubricant compositions containing hexene-based oligomers
WO2018170110A1 (en) 2017-03-16 2018-09-20 Chevron Phillips Chemical Company Lp Lubricant compositions containing hexene-based oligomers
US10876062B2 (en) 2017-03-24 2020-12-29 Exxonmobil Chemical Patents Inc. Cold cranking simulator viscosity boosting base stocks and lubricating oil formulations containing the same
US10738258B2 (en) 2017-03-24 2020-08-11 Exxonmobil Research And Engineering Company Method for improving engine fuel efficiency and energy efficiency
WO2018175830A1 (en) 2017-03-24 2018-09-27 Exxonmobil Research And Engineering Company Method for improving engine fuel efficiency and energy efficiency
US10858610B2 (en) 2017-03-24 2020-12-08 Exxonmobil Chemical Patents Inc. Cold cranking simulator viscosity boosting base stocks and lubricating oil formulations containing the same
US10808196B2 (en) 2017-03-28 2020-10-20 Exxonmobil Chemical Patents Inc. Cold cranking simulator viscosity reducing base stocks and lubricating oil formulations containing the same
US11186791B2 (en) 2017-03-30 2021-11-30 Innospec Limited Composition, method and use
US11174442B2 (en) 2017-03-30 2021-11-16 Innospec Limited Fuel compositions, methods and uses relating to quaternary ammonium salt additives for fuel used in spark ignition engines
US11015137B2 (en) 2017-03-30 2021-05-25 Innospec Limited Composition, method and use
WO2018197312A1 (en) 2017-04-27 2018-11-01 Shell Internationale Research Maatschappij B.V. Lubricating composition
WO2018211466A1 (en) 2017-05-19 2018-11-22 Chevron Oronite Company Llc Dispersants, method of making, and using same
WO2019003176A1 (en) 2017-06-30 2019-01-03 Chevron Oronite Company Llc Lubricating oil magnesium detergents and method of making and using same
WO2019003177A1 (en) 2017-06-30 2019-01-03 Chevron Oronite Company Llc Lubricating engine oil compositions containing detergent compounds
EP3421576A1 (en) 2017-06-30 2019-01-02 Infineum International Limited Refinery antifoulant process
WO2019014092A1 (en) 2017-07-13 2019-01-17 Exxonmobil Research And Engineering Company Continuous process for the manufacture of grease
WO2019012450A1 (en) 2017-07-14 2019-01-17 Chevron Oronite Company Llc Lubricating oil compositions containing non-sulfur-phosphorus containing zinc compounds and method for preventing or reducing low speed pre-ignition in direct injected spark-ignited engines
WO2019012447A1 (en) 2017-07-14 2019-01-17 Chevron Oronite Company Llc Lubricating oil compositions containing zirconium and method for preventing or reducing low speed pre-ignition in direct injected spark-ignited engines
WO2019018145A1 (en) 2017-07-21 2019-01-24 Exxonmobil Research And Engineering Company Method for improving deposit control and cleanliness performance in an engine lubricated with a lubricating oil
WO2019028310A1 (en) 2017-08-04 2019-02-07 Exxonmobil Research And Engineering Company Novel formulation for lubrication of hyper compressors providing improved pumpability under high-pressure conditions
WO2019053635A1 (en) 2017-09-13 2019-03-21 Chevron U.S.A. Inc. Method for preventing or reducing low speed pre-ignition in direct injected spark-ignited engines with cobalt-containing lubricant
US11401482B2 (en) 2017-09-13 2022-08-02 Chevron Oronite Company Llc Method for preventing or reducing low speed pre-ignition in direct injected spark-ignited engines with cobalt-containing lubricant
WO2019055291A1 (en) 2017-09-18 2019-03-21 Exxonmobil Research And Engineering Company Hydraulic oil compositions with improved hydrolytic and thermo-oxidative stability
WO2019060144A1 (en) 2017-09-22 2019-03-28 Exxonmobil Research And Engineering Company Lubricating oil compositions with viscosity and deposit control
EP3461877A1 (en) 2017-09-27 2019-04-03 Infineum International Limited Improvements in and relating to lubricating compositions
WO2019069197A1 (en) 2017-10-06 2019-04-11 Chevron Japan Ltd. Passenger car lubricating oil compositions for fuel economy
WO2019077462A1 (en) 2017-10-20 2019-04-25 Chevron Japan Ltd. Low viscosity lubricating oil composition
US11214754B2 (en) 2017-10-20 2022-01-04 Chevron Japan Ltd. Low viscosity lubricating oil composition
WO2019089181A1 (en) 2017-10-30 2019-05-09 Exxonmobil Research And Engineering Company Lubricating oil compositions with engine wear protection
WO2019089180A1 (en) 2017-10-30 2019-05-09 Exxonmobil Research And Engineering Company Lubricating oil compositions having improved cleanliness and wear performance
WO2019089177A1 (en) 2017-10-30 2019-05-09 Exxonmobil Research And Engineering Company Lubricating oil compositions with engine wear protection
US10738262B2 (en) 2017-10-30 2020-08-11 Exxonmobil Research And Engineering Company Lubricating oil compositions with engine wear protection
WO2019090038A1 (en) 2017-11-03 2019-05-09 Exxonmobil Research And Engineering Company Lubricant compositions with improved performance and methods of preparing and using the same
WO2019094019A1 (en) 2017-11-09 2019-05-16 Exxonmobil Research And Engineering Company Method for preventing or reducing low speed pre-ignition while maintaining or improving cleanliness
WO2019103808A1 (en) 2017-11-22 2019-05-31 Exxonmobil Research And Engineering Company Lubricating oil compositions with oxidative stability in diesel engines
WO2019108723A1 (en) 2017-11-30 2019-06-06 The Lubrizol Corporation Hindered amine terminated succinimide dispersants and lubricating compositions containing same
WO2019112711A1 (en) 2017-12-04 2019-06-13 Exxonmobil Research And Enginerring Company Method for preventing or reducing low speed pre-ignition
EP3495462A1 (en) 2017-12-11 2019-06-12 Infineum International Limited Low ash and ash-free acid neutralizing compositions and lubricating oil compositions containing same
US10731103B2 (en) 2017-12-11 2020-08-04 Infineum International Limited Low ash and ash-free acid neutralizing compositions and lubricating oil compositions containing same
WO2019118115A1 (en) 2017-12-15 2019-06-20 Exxonmobil Research And Engineering Company Lubricating oil compositions containing microencapsulated additives
WO2019133411A1 (en) 2017-12-28 2019-07-04 Exxonmobil Research And Engineering Company Flat viscosity fluids and lubricating oils based on liquid crystal base stocks
WO2019133407A1 (en) 2017-12-28 2019-07-04 Exxonmobil Research And Engineering Company Low traction/energy efficient liquid crystal base stocks
WO2019133409A1 (en) 2017-12-28 2019-07-04 Exxonmobil Research And Engineering Company Friction and wear reduction using liquid crystal base stocks
US10774286B2 (en) 2017-12-29 2020-09-15 Exxonmobil Research And Engineering Company Grease compositions with improved performance and methods of preparing and using the same
WO2019133191A1 (en) 2017-12-29 2019-07-04 Exxonmobil Research And Engineering Company Lubrication of oxygenated diamond-like carbon surfaces
WO2019133218A1 (en) 2017-12-29 2019-07-04 Exxonmobil Research And Engineering Company Lubricating oil compositions with wear and sludge control
WO2019133255A1 (en) 2017-12-29 2019-07-04 Exxonmobil Research And Engineering Company Grease compositions with improved performance comprising thixotropic polyamide, and methods of preparing and using the same
WO2019142059A1 (en) 2018-01-19 2019-07-25 Chevron Oronite Company Llc Ultra low ash lubricating oil compositions
US10704009B2 (en) 2018-01-19 2020-07-07 Chevron Oronite Company Llc Ultra low ash lubricating oil compositions
WO2019162744A1 (en) 2018-02-22 2019-08-29 Chevron Japan Ltd. Lubricating oils for automatic transmissions
US10604719B2 (en) 2018-02-22 2020-03-31 Chevron Japan Ltd. Lubricating oils for automatic transmissions
WO2019166977A1 (en) 2018-03-02 2019-09-06 Chevron Oronite Technology B.V. Lubricating oil composition providing wear protection at low viscosity
EP4079828A1 (en) 2018-03-29 2022-10-26 Innospec Limited Composition, method and use
WO2019217058A1 (en) 2018-05-11 2019-11-14 Exxonmobil Research And Engineering Company Method for improving engine fuel efficiency
WO2019224647A1 (en) 2018-05-25 2019-11-28 Chevron U.S.A. Inc. Method for preventing or reducing low speed pre-ignition in direct injected spark-ignited engines with manganese-containing lubricant
US10844307B2 (en) 2018-05-25 2020-11-24 Chevron Oronite Company Llc Method for preventing or reducing low speed pre-ignition in direct injected spark-ignited engines with manganesemanganese-containing lubricant
WO2019240965A1 (en) 2018-06-11 2019-12-19 Exxonmobil Research And Engineering Company Non-zinc-based antiwear compositions, hydraulic oil compositions, and methods of using the same
WO2019244020A1 (en) 2018-06-22 2019-12-26 Chevron Oronite Company Llc Lubricating oil compositions
US11773341B2 (en) 2018-06-22 2023-10-03 Chevron Oronite Company Llc Lubricating oil compositions
WO2020023430A1 (en) 2018-07-23 2020-01-30 Exxonmobil Research And Engineering Company Lubricating oil compositions with oxidative stability in diesel engines using biodiesel fuel
WO2020023437A1 (en) 2018-07-24 2020-01-30 Exxonmobil Research And Engineering Company Lubricating oil compositions with engine corrosion protection
EP3604484A1 (en) 2018-08-03 2020-02-05 Afton Chemical Corporation Lubricity additives for fuels
WO2020068439A1 (en) 2018-09-27 2020-04-02 Exxonmobil Research And Engineering Company Low viscosity lubricating oils with improved oxidative stability and traction performance
WO2020096804A1 (en) 2018-11-05 2020-05-14 Exxonmobil Research And Engineering Company Lubricating oil compositions having improved cleanliness and wear performance
WO2020100045A1 (en) 2018-11-16 2020-05-22 Chevron Japan Ltd. Low viscosity lubricating oil compositions
US11193084B2 (en) 2018-11-16 2021-12-07 Chevron Japan Ltd. Low viscosity lubricating oil compositions
WO2020112338A1 (en) 2018-11-28 2020-06-04 Exxonmobil Research And Engineering Company Lubricating oil compositions with improved deposit resistance and methods thereof
WO2020123440A1 (en) 2018-12-10 2020-06-18 Exxonmobil Research And Engineering Company Method for improving oxidation and deposit resistance of lubricating oils
WO2020131441A1 (en) 2018-12-19 2020-06-25 Exxonmobil Research And Engineering Company Grease compositions having improved performance
WO2020132164A1 (en) 2018-12-19 2020-06-25 Exxonmobil Research And Engineering Company Lubricating oil compositions with viscosity control
WO2020131310A1 (en) 2018-12-19 2020-06-25 Exxonmobil Research And Engineering Company Method for improving high temperature antifoaming performance of a lubricating oil
WO2020131440A1 (en) 2018-12-19 2020-06-25 Exxonmobil Research And Engineering Company Grease compositions having calcium sulfonate and polyurea thickeners
WO2020132166A1 (en) 2018-12-19 2020-06-25 Exxonmobil Research And Engineering Company Lubricating oil compositions with antioxidant formation and dissipation control
WO2020131439A1 (en) 2018-12-19 2020-06-25 Exxonmobil Research And Engineering Company Grease compositions having polyurea thickeners made with isocyanate terminated prepolymers
WO2020131515A2 (en) 2018-12-19 2020-06-25 Exxonmobil Research And Engineering Company Lubricant compositions with improved wear control
EP3760696A1 (en) 2018-12-20 2021-01-06 Infineum International Limited Oil anti-foulant and/or asphaltene agglomeration process
EP3835392A1 (en) 2018-12-20 2021-06-16 Infineum International Limited Hydrocarbon marine fuel oil
WO2020139333A1 (en) 2018-12-26 2020-07-02 Exxonmobil Research And Engineering Company Formulation approach to extend the high temperature performance of lithium complex greases
EP3680312A1 (en) 2019-01-11 2020-07-15 Afton Chemical Corporation Oxazoline modified dispersants
WO2020150123A1 (en) 2019-01-17 2020-07-23 The Lubrizol Corporation Traction fluids
WO2020176171A1 (en) 2019-02-28 2020-09-03 Exxonmobil Research And Engineering Company Low viscosity gear oil compositions for electric and hybrid vehicles
WO2020257375A1 (en) 2019-06-19 2020-12-24 Exxonmobil Research And Engineering Company Heat transfer fluids and methods of use
WO2020257374A1 (en) 2019-06-19 2020-12-24 Exxonmobil Research And Engineering Company Heat transfer fluids and methods of use
WO2020257373A1 (en) 2019-06-19 2020-12-24 Exxonmobil Research And Engineering Company Heat transfer fluids and methods of use
WO2020257379A1 (en) 2019-06-19 2020-12-24 Exxonmobil Research And Engineering Company Heat transfer fluids and methods of use
WO2020257377A1 (en) 2019-06-19 2020-12-24 Exxonmobil Research And Engineering Company Heat transfer fluids and methods of use
US11092393B1 (en) 2019-06-19 2021-08-17 Exxonmobil Research And Engineering Company Heat transfer fluids and methods of use
WO2020257368A1 (en) 2019-06-19 2020-12-24 Exxonmobil Research And Engineering Company Heat transfer fluids and methods of use
WO2020257376A1 (en) 2019-06-19 2020-12-24 Exxonmobil Research And Engineering Company Heat transfer fluids and methods of use
WO2020257370A1 (en) 2019-06-19 2020-12-24 Exxonmobil Research And Engineering Company Heat transfer fluids and methods of use
US10712105B1 (en) 2019-06-19 2020-07-14 Exxonmobil Research And Engineering Company Heat transfer fluids and methods of use
WO2020257378A1 (en) 2019-06-19 2020-12-24 Exxonmobil Research And Engineering Company Heat transfer fluids and methods of use
WO2020257371A1 (en) 2019-06-19 2020-12-24 Exxonmobil Research And Engineering Company Heat transfer fluids and methods of use
WO2020264534A2 (en) 2019-06-27 2020-12-30 Exxonmobil Research And Engineering Company Method for reducing solubilized copper levels in wind turbine gear oils
EP3778841A1 (en) 2019-08-15 2021-02-17 Infineum International Limited Method for reducing piston deposits in a marine diesel engine
WO2021154497A1 (en) 2020-01-30 2021-08-05 Exxonmobil Research And Engineering Company Sulfur-free, ashless, low phosphorus lubricant compositions with improved oxidation stability
WO2021181285A1 (en) 2020-03-11 2021-09-16 Chevron Oronite Company Llc Lubricating oil compositions with improved oxidative performance comprising alkylated diphenylamine antioxidant and carboxylate detergents
WO2021181286A1 (en) 2020-03-11 2021-09-16 Chevron Oronite Company Llc Lubricating oil compositions with improved oxidative performance comprising alkylated diphenylamine antioxidant and sulfonate detergents
WO2021194813A1 (en) 2020-03-27 2021-09-30 Exxonmobil Research And Engineering Company Monitoring health of heat transfer fluids for electric systems
WO2021229517A1 (en) 2020-05-14 2021-11-18 Chevron Japan Ltd. Lubricating oil composition including comb polymethacrylate and ethylene-based olefin copolymer viscosity modifiers
WO2022010606A1 (en) 2020-07-09 2022-01-13 Exxonmobil Research And Engineering Company Engine oil lubricant compositions and methods for making same with superior engine wear protection and corrosion protection
WO2022018681A1 (en) 2020-07-23 2022-01-27 Chevron Oronite Company Llc Succinimide dispersants post-treated with aromatic glycidyl ethers that exhibit good soot handling performance
WO2022018682A1 (en) 2020-07-23 2022-01-27 Chevron Oronite Company Llc Succinimide dispersants post-treated with heteroaromatic glycidyl ethers that exhibit good soot handling performance
WO2022054023A1 (en) 2020-09-14 2022-03-17 Chevron Japan Ltd. Lubricating oil containing alkyl phosphonic acid
WO2022072962A1 (en) 2020-09-30 2022-04-07 Exxonmobil Research And Engineering Company Low friction and low traction lubricant compositions useful in dry clutch motorcycles
WO2022074547A1 (en) 2020-10-05 2022-04-14 Chevron Japan Ltd. Friction modifier system
WO2022099291A1 (en) 2020-11-06 2022-05-12 Exxonmobil Research And Engineering Company Engine oil lubricant compositions and methods for making same with steel corrosion protection
WO2022112899A1 (en) 2020-11-25 2022-06-02 Chevron Japan Ltd. Lubricating oil compositions
US11760952B2 (en) 2021-01-12 2023-09-19 Ingevity South Carolina, Llc Lubricant thickener systems from modified tall oil fatty acids, lubricating compositions, and associated methods
WO2022243947A1 (en) 2021-05-20 2022-11-24 Chevron Japan Ltd. Low ash lubricating oil composition
EP4180505A1 (en) 2021-11-15 2023-05-17 Infineum International Limited Improvements in marine fuels
US12031099B2 (en) 2021-11-15 2024-07-09 Infineum International Limited Marine fuels
WO2023111550A1 (en) 2021-12-14 2023-06-22 Innospec Limited Methods and uses relating to fuel compositions
WO2023122405A1 (en) 2021-12-21 2023-06-29 ExxonMobil Technology and Engineering Company Engine oil lubricant compostions and methods for making same with superior oil consumption
WO2023144721A1 (en) 2022-01-25 2023-08-03 Chevron Japan Ltd. Lubricating oil composition
WO2023156989A1 (en) 2022-02-21 2023-08-24 Chevron Oronite Company Llc Lubricating oil composition
WO2024030899A1 (en) 2022-08-01 2024-02-08 Chevron Oronite Company Llc Lubricating oil composition for corrosion control
US11873461B1 (en) 2022-09-22 2024-01-16 Afton Chemical Corporation Extreme pressure additives with improved copper corrosion
US12134742B2 (en) 2022-09-30 2024-11-05 Afton Chemical Corporation Fuel composition
US12024686B2 (en) 2022-09-30 2024-07-02 Afton Chemical Corporation Gasoline additive composition for improved engine performance
EP4353804A1 (en) 2022-10-11 2024-04-17 Infineum International Limited Functionalized c4 to c5 olefin polymers and lubricant compositions containing such
EP4353805A1 (en) 2022-10-11 2024-04-17 Infineum International Limited Lubricant composition containing metal alkanoate
EP4357443A1 (en) 2022-10-18 2024-04-24 Infineum International Limited Lubricating oil compositions
WO2024126998A1 (en) 2022-12-12 2024-06-20 Innospec Limited Composition, method and use
EP4397738A1 (en) 2023-01-03 2024-07-10 Infineum International Limited Method for reduction of abnormal combustion events
US11884890B1 (en) 2023-02-07 2024-01-30 Afton Chemical Corporation Gasoline additive composition for improved engine performance
US11795412B1 (en) 2023-03-03 2023-10-24 Afton Chemical Corporation Lubricating composition for industrial gear fluids
EP4428212A1 (en) 2023-03-10 2024-09-11 Infineum International Limited Asphaltene deposition control
WO2024220396A1 (en) 2023-04-17 2024-10-24 Chevron Oronite Company Llc Friction modifier for wet clutch
WO2024220394A1 (en) 2023-04-17 2024-10-24 Chevron Oronite Company Llc Friction modifier for automatic transmission fluid

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