EP0551466B1 - Verwendung einer Additivzusammensetzung zur Verbesserung der Filtrierbarkeit von mit Wasser kontaminierten Schmiermittelzusammensetzungen - Google Patents

Verwendung einer Additivzusammensetzung zur Verbesserung der Filtrierbarkeit von mit Wasser kontaminierten Schmiermittelzusammensetzungen Download PDF

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Publication number
EP0551466B1
EP0551466B1 EP92915925A EP92915925A EP0551466B1 EP 0551466 B1 EP0551466 B1 EP 0551466B1 EP 92915925 A EP92915925 A EP 92915925A EP 92915925 A EP92915925 A EP 92915925A EP 0551466 B1 EP0551466 B1 EP 0551466B1
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Prior art keywords
acid
group
metal
carbon atoms
aliphatic
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EP92915925A
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English (en)
French (fr)
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EP0551466A1 (de
Inventor
Timothy Cooper
James Noel Vinci
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Lubrizol Corp
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Lubrizol Corp
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    • C10M2219/00—Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions
    • C10M2219/04—Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions containing sulfur-to-oxygen bonds, i.e. sulfones, sulfoxides
    • C10M2219/044—Sulfonic acids, Derivatives thereof, e.g. neutral salts
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    • C10M2219/04—Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions containing sulfur-to-oxygen bonds, i.e. sulfones, sulfoxides
    • C10M2219/046—Overbasedsulfonic acid salts
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    • C10M2219/08—Thiols; Sulfides; Polysulfides; Mercaptals
    • C10M2219/082—Thiols; Sulfides; Polysulfides; Mercaptals containing sulfur atoms bound to acyclic or cycloaliphatic carbon atoms
    • C10M2219/087—Thiols; Sulfides; Polysulfides; Mercaptals containing sulfur atoms bound to acyclic or cycloaliphatic carbon atoms containing hydroxy groups; Derivatives thereof, e.g. sulfurised phenols
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    • C10M2219/088—Neutral salts
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    • C10M2219/08—Thiols; Sulfides; Polysulfides; Mercaptals
    • C10M2219/082—Thiols; Sulfides; Polysulfides; Mercaptals containing sulfur atoms bound to acyclic or cycloaliphatic carbon atoms
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    • C10M2219/089—Overbased salts
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    • C10M2223/00—Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions
    • C10M2223/02—Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions having no phosphorus-to-carbon bonds
    • C10M2223/04—Phosphate esters
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    • C10M2223/041—Triaryl phosphates
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    • C10M2223/02—Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions having no phosphorus-to-carbon bonds
    • C10M2223/04—Phosphate esters
    • C10M2223/042—Metal salts thereof
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    • C10M2223/02—Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions having no phosphorus-to-carbon bonds
    • C10M2223/04—Phosphate esters
    • C10M2223/045—Metal containing thio derivatives
    • C—CHEMISTRY; METALLURGY
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    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2010/00—Metal present as such or in compounds
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    • C10N2010/02—Groups 1 or 11
    • C—CHEMISTRY; METALLURGY
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    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2040/00—Specified use or application for which the lubricating composition is intended
    • C10N2040/25—Internal-combustion engines
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2040/00—Specified use or application for which the lubricating composition is intended
    • C10N2040/25—Internal-combustion engines
    • C10N2040/251—Alcohol fueled engines
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
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    • C10N2040/00—Specified use or application for which the lubricating composition is intended
    • C10N2040/25—Internal-combustion engines
    • C10N2040/255—Gasoline engines
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2040/00—Specified use or application for which the lubricating composition is intended
    • C10N2040/25—Internal-combustion engines
    • C10N2040/255—Gasoline engines
    • C10N2040/28—Rotary engines

Definitions

  • This invention relates to the use of compositions useful as additives for lubricants and functional fluids, and to additive concentrates, lubricants and functional fluids containing said additives. More particularly, this invention relates to the use of compositions comprising a major amount of an oil of lubricating viscosity, (A) a metal salt selected from the group consisting of sulfonates, phenates, carboxylates and mixtures thereof, (B) an aliphatic carboxylic acid or anhydride, or carboxylic acid containing derivative thereof, wherein the aliphatic group contains at least about 20 carbon atoms and optionally (C) a metal salt of (C)(I) at least one organic phosphorus acid or a mixture of (C)(I) at least one organic phosphorus acid and (C)(II) at least one carboxylic acid. Also disclosed are lubricants and functional fluids containing these additives and methods for improving the wet filterability of lubricants and functional fluids. This invention also relates
  • lubricants are required to meet a variety of performance requirements. It is known in the art to add various chemical additives to a lubricating oil basestock in order to provide or reinforce needed properties.
  • the lubricant may contain nothing more than the lubricating base stock, although even in this case, additives such as oxidation and corrosion inhibitors and antifoam agents are often included.
  • Chemical additives to provide extreme pressure and antiwear performance are known. These include, but are not limited to, phosphorus-containing additives, sulfur-containing additives and others. Phosphorus additives include metal-free and metal-containing derivatives of phosphorus acids.
  • Hoke U.S. Patents 4,032,461; 4,208,357; and 4,282,171, refers to various phosphorus and sulfur-containing amides and thioamides.
  • Metal salts of phosphorodithioic acids are known lubricant additives. See, for example, Le Suer et al, U.S. 3,390,082 and Chamberlin, U.S. 4,326,974.
  • Metals salts of mixtures of carboxylic and phosphorus acids are also known, as are post-treated metal salts of phosphorus acids. See, for example, Clason et al, U.S. 4,308,154, Schroeck, U.S. 4,289,635, Schroeck, U.S. 4,507,215 and Schroeck, U.S. 4,263,150.
  • Metals salts of organic acids, and particularly overbased metal salts of organic acids are also well-known lubricating oil additives.
  • EP-A-0 096 539 relates to improved crankase lubricating oil compositions effective in both gasoline and diesel internal combustion engines. These compositions exhibit improved engine deposit control and varnish inhibition. They contain polyisobutenylsuccinic anhydride as a supplemental dispersant-detergent in combination with the conventional lubricating oil dispersant, an overbased metal detergent, a zinc dialkyldithiophosphate and optionally a dispersant-viscosity index improver.
  • EP-A-0 096 539 does not recognize the problem of filterability when metal-containing compositions are exposed to moisture.
  • lubricating oils described in the aforementioned patents provide exemplary performance. However, in several applications, it has been found to be desirable, and sometimes necessary, that the lubricant possess even further enhanced performance characteristics.
  • lubricating oil compositions such as functional fluids, and especially hydraulic fluids, are used in equipment designed to very close tolerances.
  • a hydraulic fluid which is employed as the lubricant and power transmitting fluid in hydraulic pumps must provide extreme pressure, antiwear and oxidation performance. Because of the close operating tolerances, it is usually necessary that hydraulic fluids be kept meticulously clean. To accomplish this end, very fine filters are employed to remove solid contaminants from the circulating hydraulic fluid. The filter must remove abrasive contaminants, but still must allow free fluid flow through the system.
  • lubricating oil compositions including hydraulic fluids, containing metal salts of organic acids, and particularly those containing overbased metal salts, when exposed to moisture, may clog filters.
  • moisture may arise from, for example, environmental contamination or condensation of atmospheric moisture.
  • filters become clogged, fluid flow is reduced, or in extreme cases, essentially stops.
  • Filterability of moisture (water) containing lubricating compositions is referred to herein as wet filterability.
  • the nature of the moisture-contaminated lubricating oil is not understood, that is, it is not known with certainty whether, for example, the moisture (water) is simply dispersed within the oil composition, whether a chemical reaction has taken place or if the moisture is incorporated in some other fashion. What is known is that when the oil composition is contaminated with moisture, filterability, especially filterability through fine filters, is impaired.
  • moisture contamination contributing to filterability difficulties is present in the oil composition in amounts ranging up to about 1% by weight of the oil composition, although more than 1% by weight of water may be present as a contaminant and may contribute to filterability difficulties.
  • a lubricant or functional fluid that does not tend to generate materials that clog filters when the fluid is exposed to moisture.
  • a zinc-containing lubricating oil composition resisted loss of zinc when the oil is exposed to water.
  • the present invention provides the use of compositions useful as additives for lubricants and additive concentrates and lubricants containing these additives.
  • Lubricants and functional fluids containing these additives have a reduced tendency to clog filters when the lubricants are exposed to moisture and resist depletion of zinc when exposed to water.
  • the present invention provides the use of a composition
  • a composition comprising a major amount of an oil of lubricating viscosity, and minor amounts of (A) a metal salt selected from the group consisting of sulfonates, phenates, carboxylates and mixtures thereof, (B) an aliphatic carboxylic acid or anhydride, or carboxylic-acid group containing derivative thereof, wherein the aliphatic group contains at least about 20 carbon atoms and optionally (C) a metal salt of (C)(I) at least one organic phosphorus acid or mixture of (C)(I) at least one organic phosphorus acid and (C)(II) at least one carboxylic acid.
  • Component (B) is present in an effective amount to improve wet filterability of the composition.
  • the composition may comprise a phosphite.
  • the present invention provides a method for improving the wet filterability of lubricants and functional fluid compositions. Also provided is a method for imparting to lubricating oil compositions the ability to resist depletion of zinc when the compositions are exposed to water.
  • hydrocarbon based group is used throughout this specification and in the appended claims to denote a group having a carbon atom directly attached to the remainder of the molecule and having a predominantly hydrocarbon character within the context of this invention.
  • hydrocarbon based group includes hydrocarbon, as well as substantially hydrocarbon, groups.
  • substantially hydrocarbon describes groups may contain non-hydrocarbon substituents, or non-carbon atoms in a ring or chain, which do not alter the predominantly hydrocarbon nature of the group.
  • Hydrocarbon based groups can contain up to three, preferably up to one, non-hydrocarbon substituent, or non-carbon heteroatom in a ring or chain, for every ten carbon atoms, provided this non-hydrocarbon substituent or non-carbon heteroatom does not significantly alter the predominantly hydrocarbon character of the group.
  • hydrocarbon-based groups are purely hydrocarbon, that is, they are substantially free of non-hydrocarbon substituents or heteroatoms.
  • heteroatoms such as oxygen, sulfur and nitrogen, or substituents, which include, for example, hydroxyl, halo (especially chloro and fluoro), alkoxyl, alkyl mercapto, alkyl sulfoxy, etc.
  • hydrocarbon based groups include, but are not necessarily limited to, the following:
  • Component (A) is a metal salt selected from the group consisting of sulfonates, phenates or carboxylates. These salts may be normal salts or they may be overbased salts. Overbased salts are preferred.
  • the metals may be alkali or alkaline earth metals, copper or zinc. In a preferred embodiment the metals are alkali or alkaline earth metals, more preferably, sodium, potassium, calcium or magnesium.
  • Component (A) may be a normal metal salt, that is, a salt wherein the metal content is substantially that which is present according to the stoichiometry of the metal and the particular organic compound reacted with the metal.
  • These salts are sometimes referred to as "neutral” salts despite the fact that, depending upon the nature of the anion and cation, the salt may display basic properties, i.e., may display basic character as opposed to neutral or acidic character, especially in aqueous media.
  • metal salts of sulfonic acids, phenols and carboxylic acids are preferred.
  • Preferred metals are alkali or alkaline earth metals, copper or zinc.
  • Normal metal salts are readily prepared by the reaction of an acid with a metal compound such as a hydroxide or carbonate, double displacement reactions, such as the reaction of a sodium salt with calcium chloride, etc.
  • a metal compound such as a hydroxide or carbonate
  • double displacement reactions such as the reaction of a sodium salt with calcium chloride, etc.
  • the skilled worker is aware of numerous means for preparing normal metal salts, and further elaboration here is unnecessary.
  • overbased is characterized by a metal content in excess of that which would be present according to the stoichiometry of the metal and the particular organic compound reacted with the metal, e.g., a carboxylic or sulfonic acid or phenol.
  • the carboxylic acid or an alkali or alkaline earth metal salt thereof can be reacted with a metal base and the product will contain an amount of metal in excess of that necessary to neutralize the acid, for example, 4.5 times as much metal as present in the normal salt or a metal excess of 3.5 equivalents.
  • the actual stoichiometric excess of metal can vary considerably, for example, from 0.1 equivalent to 50 or more equivalents depending on the reactions, the process conditions, and the like.
  • the overbased materials useful in accordance with the present invention contain from 1.1 to 40 or more equivalents of metal, more preferably from 1.5 to 30 and most preferably from 2 to 25 equivalents of metal for each equivalent of material which is overbased.
  • overbased is used to designate materials containing a stoichiometric excess of metal and is, therefore, inclusive of those materials which have been referred to in the art as overbased, superbased, hyperbased, etc., as discussed supra, and hereinbelow.
  • metal ratio is used in the prior art and herein to designate the ratio of the total chemical equivalents of the metal in the overbased material (e.g., a metal sulfonate or carboxylate) to the chemical equivalents of the metal in the product which would be expected to result in the reaction between the organic material to be overbased (e.g., sulfonic or carboxylic acid) and the metal-containing reactant (e.g., calcium hydroxide, barium oxide, etc.) according to the known chemical reactivity and stoichiometry of the two reactants.
  • the metal-containing reactant e.g., calcium hydroxide, barium oxide, etc.
  • the equivalent weight of the acidic organic compound is its molecular weight divided by the number of acidic groups (i.e., sulfonic acid, carboxy or acidic hydroxy groups) present per molecule.
  • the acidic organic compound contains a diluent such as oil or unreacted alkylate. Often the acidic organic compound is not a pure single species.
  • the equivalent weight of the acidic organic compound can be determined by a suitable analytical technique such as acid number (e.g. ASTM procedures D-664 and/or D-974).
  • the metal ratio is one, and in the overbased carboxylate, the metal ratio may be 4.5.
  • the "metal ratio" of the product will depend upon whether the number of equivalents of metal in the overbased product is compared to the number of equivalents expected to be present for a given single component or a combination of all such components.
  • the metal ratio may be expressed in terms of percentages. For a normal metal salt, the percentage is 100%; for overbased materials, the percentage is greater than 100. For the overbased calcium carboxylate example above, the percentage is 450.
  • overbased materials are prepared by treating a reaction mixture comprising the organic material to be overbased, a reaction medium consisting essentially of at least one inert, organic solvent for said organic material, a stoichiometric excess of a metal base, and a promoter with an acidic material.
  • a reaction mixture comprising the organic material to be overbased, a reaction medium consisting essentially of at least one inert, organic solvent for said organic material, a stoichiometric excess of a metal base, and a promoter with an acidic material.
  • organic materials which are overbased are their solubility in the particular reaction medium utilized in the overbasing process.
  • the reaction medium used frequently comprises petroleum fractions, particularly mineral oils
  • these organic materials have generally been oil-soluble.
  • another reaction medium e.g., aromatic hydrocarbons, aliphatic hydrocarbons, kerosene, etc.
  • many organic materials which are soluble in mineral oils will be soluble in many of the other indicated suitable reaction media.
  • Materials which can be overbased are generally oil-soluble organic acids including sulfonic acids, phosphorus acids, thiophosphorus acids, sulfur acids, alkylphenols, coupled alkylphenols, carboxylic, acids, thiocarboxylic acids, and the like, as well as the corresponding alkali and alkaline earth metal salts thereof.
  • Representative examples of each of these classes of organic acids, as well as other organic acids, e.g., nitrogen acids, arsenic acids, etc., are disclosed along with methods of preparing overbased products therefrom in the above-cited patents.
  • U.S. Patent No. 2,777,874 identifies organic acids suitable for preparing overbased materials.
  • overbased materials derived from oil-soluble metal-free, non-tautomeric neutral and basic organic polar compounds such as ester, amines, amides, alcohols, ethers, sulfides, sulfoxides, and the like are disclosed in U.S. Patent Nos. 2,968,642; 2,971,014 and 2,989,463.
  • Another class of materials which can be overbased are the oil-soluble, nitro-substituted aliphatic hydrocarbons, particularly nitro-substituted polyolefins such as polyethylene, polypropylene, polyisobutylene, etc. Materials of this type are illustrated in U.S. Patent No. 2,959,551.
  • mixtures of alkylated phenols and the oil-soluble reaction product of alkylene polyamines such as propylene diamine or N-alkylated propylene diamine with formaldehyde or formaldehyde producing compound can be overbased.
  • alkylene polyamines such as propylene diamine or N-alkylated propylene diamine with formaldehyde or formaldehyde producing compound (e.g., paraformaldehyde)
  • formaldehyde or formaldehyde producing compound e.g., paraformaldehyde
  • formaldehyde or formaldehyde producing compound e.g., paraformaldehyde
  • the metal compounds used in preparing the overbased materials are normally the basic salts, oxides and hydroxides of alkali and alkaline earth metals, although corresponding metal compounds such as lead, zinc, manganese, copper, etc., can be used in the preparation of overbased materials. Mixtures of different metal compounds can be used to prepare mixed metal overbased products.
  • the anionic portion of the metal compound can be hydroxyl, oxide, carbonate, hydrogen carbonate, acetate, hydrogen sulfite, halide, amide, borate, etc., as disclosed in the above-cited patents.
  • the preferred overbased materials are prepared from alkali and alkaline earth metal oxides, hydroxides, and alcoholates such as the alkaline earth metal lower alkoxides.
  • the more preferred metals are calcium, magnesium, sodium, lithium, and/or barium.
  • the most preferred alkali metal is sodium, and calcium is the most preferred alkaline earth metal.
  • mixed metal overbased products are also useful.
  • the promoters that is, the materials which permit the incorporation of the excess metal into the overbased material, are also quite diverse and well known in the art as evidenced by the cited patents. A particularly comprehensive discussion of suitable promoters is found in U.S. Patent Nos. 2,777,874; 2,695,910 and 2,616,904. These include the alcoholic and phenolic promoters which are preferred.
  • the alcoholic promoters include the alkanols of one to about eighteen carbon atoms, preferably one to about twelve carbon atoms, and more preferably one to about five carbon atoms, such as methanol, ethanol, n-butanol, amyl alcohol, octanol, isopropanol, isobutanol, and mixtures of these and the like.
  • Polyols are also useful promoters.
  • a particularly preferred polyol is ethylene glycol.
  • Phenolic promoters include a variety of hydroxy- substituted benzenes and naphthalenes.
  • a particularly useful class of phenols are the alkylated phenols of the type listed in U.S. Patent No. 2,777,874, e.g., heptylphenols, octylphenols, and nonylphenols. Mixtures of various promoters are sometimes used.
  • Suitable acidic materials are also disclosed in the above-cited patents, for example, U.S. Patent No. 2,616,904. Included within the known group of useful acidic materials are liquid acids such as formic acid, acetic acid, nitric acid, sulfuric acid, hydrochloric acid, hydrobromic acid, carbamic acid, substituted carbamic acids, etc.
  • Acetic acid is a very useful acidic material, although inorganic acidic materials such as boric acid, HCl, SO 2 , SO 3 , CO 2 , H 2 S, N 2 O 3 , etc., are ordinarily employed as the acidic materials.
  • the most preferred acidic materials are carbon dioxide and acetic acid, with carbon dioxide being especially preferred.
  • H 2 O can be used as the acidic material.
  • examples include overbasing with MgO or aluminum isopropoxide.
  • the material to be overbased, an inert, non-polar, organic solvent therefor, the metal base, the promoter and the acidic material are brought together and a chemical reaction ensues.
  • the exact nature of the resulting overbased product is not known. However, it can be adequately described for purposes of the present specification as a single phase homogeneous mixture of the solvent and (1) either a metal complex formed from the metal base, the acidic material, and the material being overbased and/or (2) an amorphous metal salt formed from the reaction of the acidic material with the metal base and the material which is said to be overbased.
  • the resulting overbased material can be described for purposes of this invention as an oil solution of either a metal-containing complex of the acidic material, the metal base, and the carboxylic acid or as an oil solution of amorphous calcium carbonate and calcium carboxylate.
  • the temperature at which the acidic material is contacted with the remainder of the reaction mass depends to a large measure upon the promoting agent used. With a phenolic promoter, the temperature usually ranges from 80°C to 300°C, and preferably from 100°C to 200°C. When an alcohol or mercaptan is used as the promoting agent, the temperature usually will not exceed the reflux temperature of the reaction mixture and preferably will not exceed about 100°C.
  • the overbased materials may retain all or a portion of the promoter. That is, if the promoter is not volatile (e.g., an alkyl phenol) or otherwise readily removable from the overbased material, at least some promoter remains in the overbased product. The presence or absence of the promoter in the overbased material does not represent a critical aspect of the invention. Obviously, it is within the skill of the art to select a volatile promoter such as a lower alkanol, e.g., methanol, ethanol, etc., so that the promoter can be readily removed prior to incorporation within the compositions of the present invention.
  • a volatile promoter such as a lower alkanol, e.g., methanol, ethanol, etc.
  • overbased materials are the metal-overbased water-insoluble organic acids, preferably those containing at least eight aliphatic carbons, although the acids may contain as few as six aliphatic carbon atoms if the acid molecule includes an aromatic ring such as phenyl, naphthyl, etc.
  • Representative organic acids suitable for preparing these overbased materials are discussed and identified in detail in the above-cited patents.
  • U.S. Patent Nos. 2,616,904 and 2,777,874 disclose a variety of very suitable organic acids.
  • Overbased carboxylic and sulfonic acids and phenols are particularly suitable.
  • Suitable carboxylic acids include aliphatic, cycloaliphatic and aromatic mono- and polybasic carboxylic acids free from acetylenic unsaturation, including naphthenic acids, alkyl- or alkenyl-substituted cyclopentanoic acids, alkyl- or alkenyl-substituted cyclohexanoic acids, and alkyl- or alkenyl-substituted aromatic carboxylic acids.
  • the aliphatic acids generally contain from 8 to 50, and preferably from 12 to 25, carbon atoms.
  • the cycloaliphatic and aliphatic carboxylic acids can be saturated or unsaturated.
  • Specific examples include 2-ethylhexanoic acid, linolenic acid, propylene tetramer-substituted maleic acid, behenic acid, isostearic acid, pelargonic acid, capric acid, palmitoleic acid, linoleic acid, lauric acid, oleic acid, ricinoleic acid, undecylic acid, dioctylcyclopentanecarboxylic acid, myristic acid, dilauryldecahydronaphthalene-carboxylic acid, stearyl-octahydroindenecarboxylic acid, palmitic acid, alkyl- and alkenylsuccinic acids, acids formed by oxidation of petrolatum or of hydrocarbon waxes, and commercially available mixtures of two or more carboxylic acids, such as tall oil acids, rosin acids, and the like.
  • carboxylic acids include propenyl-substituted glutaric acid, polybutenyl-substituted succinic acids derived from a polybutene (Mn equals about 200-1500, preferably about 300-1500), propenyl-substituted succinic acids derived from polypropylenes (Mn equals 200-1000), acids, acids formed by oxidation of petrolatum or of hydrocarbon waxes, available mixtures of two or more carboxylic acids and mixtures of these acids, their metal salts, and/or their anhydrides.
  • the carboxylic acids are aromatic carboxylic acids.
  • a group of useful aromatic carboxylic acids are those of the formula wherein R 1 is an aliphatic hydrocarbon based group preferably derived from polyalkenes, a is a number in the range of 1 to 4, usually 1 or 2, Ar is an aromatic group, each X is independently sulfur or oxygen, preferably oxygen, b is a number in the range of from 1 to 4, usually 1 or 2, c is a number in the range of zero to 4, usually 1 to 2, with the proviso that the sum of a, b and c does not exceed the number of valences of Ar.
  • aromatic carboxylic acids include substituted benzoic, phthalic and salicylic acids.
  • the R 1 group is a hydrocarbon based group that is directly bonded to the aromatic group Ar.
  • R 1 groups include substituents derived from polymerized olefins such as polyethylenes, polypropylenes, polybutylenes, ethylene-propylene copolymers, chlorinated olefin polymers and oxidized ethylene-propylene copolymers.
  • the aromatic group Ar may have the same structure as any of the aromatic groups Ar discussed below.
  • the aromatic groups that are useful herein include the polyvalent aromatic groups derived from benzene, naphthalene, anthracene, etc., preferably benzene.
  • Specific examples of Ar groups include phenylenes and naphthylene, e.g., methylphenylenes, ethoxyphenylenes, isopropylphenylenes, hydroxyphenylenes, dipropoxynaphthylenes, etc.
  • a useful class of carboxylic acids are those of the formula wherein R 1 is defined above, a is a number in the range of from 1 to 4, preferably 1 to 3; b is a number in the range of 1 to 4, preferably 1 to 2, c is a number in the range of zero to 4, preferably 1 to 2, and more preferably 1; with the proviso that the sum of a, b and c does not exceed 6.
  • b and c are each one and the carboxylic acid is a salicylic acid.
  • Zinc, calcium and magnesium salts of the aromatic carboxylic acids, and especially the salicylic acids, are preferred.
  • the sulfonic acids for use in the preparation of component (A) include those represented by the formulas R a (SO 3 H) r and (R b ) x T(SO 3 H) y .
  • R a is an aliphatic or aliphatic-substituted cycloaliphatic hydrocarbon or essentially hydrocarbon radical free from acetylenic unsaturation and containing up to about 60 carbon atoms.
  • R a is aliphatic, it usually contains at least about 15 carbon atoms; when it is an aliphatic-substituted cycloaliphatic radical, the aliphatic substituents usually contain a total of at least about 12 carbon atoms.
  • R a examples are alkyl, alkenyl and alkoxyalkyl radicals, and aliphatic-substituted cycloaliphatic radicals wherein the aliphatic substituents are alkyl, alkenyl, alkoxy, alkoxyalkyl, carboxyalkyl and the like.
  • the cycloaliphatic nucleus is derived from a cycloalkane or a cycloalkene such as cyclopentane, cyclohexane, cyclohexene or cyclopentene.
  • Ra is cetylcyclohexyl, laurylcyclohexyl, cetyloxyethyl, octadecenyl, and radicals derived from petroleum, saturated and unsaturated paraffin wax, and olefin polymers including polymerized monoolefins and diolefins containing 2-8 carbon atoms per olefinic monomer unit.
  • R a can also contain other substituents such as phenyl, cycloalkyl, hydroxy, mercapto, halo, nitro, amino, nitroso, lower alkoxy, lower alkylmercapto, carboxy, carbalkoxy, oxo or thio, or interrupting groups such as -NH-, -O- or -S-, as long as the essentially hydrocarbon character thereof is not destroyed.
  • R b is generally a hydrocarbon or substantially hydrocarbon radical free from acetylenic unsaturation and containing from 4 to 60 aliphatic carbon atoms, preferably an aliphatic hydrocarbon radical such as alkyl or alkenyl. It may also, however, contain substituents or interrupting groups such as those enumerated above provided the essentially hydrocarbon character thereof is retained. In general, any non-hydrocarbon atoms present in R a or R b do not account for more than 10% of the total weight thereof. Preferably, R a and R b are substantially free of non-hydrocarbon atoms.
  • the radical T is a cyclic nucleus which may be derived from an aromatic hydrocarbon such as benzene, naphthalene, anthracene or biphenyl, or from a heterocyclic compound such as pyridine, indole or isoindole.
  • T is an aromatic hydrocarbon nucleus, especially a benzene or naphthalene nucleus.
  • the subscript x is at least 1 and is generally 1-3.
  • the subscripts r and y have an average value of 1-4 per molecule, more often 1.
  • Illustrative sulfonic acids useful in the preparation of component A are mahogany sulfonic acids, petrolatum sulfonic acids, mono- and polywax-substituted naphthalene sulfonic acids, cetylchlorobenzene sulfonic acids, cetylphenol sulfonic acids, cetylphenol disulfide sulfonic acids, cetoxycapryl benzene sulfonic acids, dicetyl thianthrene sulfonic acids, dilauryl beta-naphthol sulfonic acids, dicapryl nitronaphthalene sulfonic acids, saturated paraffin wax sulfonic acids, unsaturated paraffin wax sulfonic acids, hydroxy-substituted paraffin wax sulfonic acids, tetraisobutylene sulfonic acids, tetra-amylene sulfonic acids, chloro-substitute
  • the overbased materials have a metal ratio of at least 1.1, preferably at least 1.5, and more preferably at least 2 to 4.
  • An especially suitable group of the preferred sulfonic acid and carboxylic acid overbased materials has a metal ratio of at least 7.0. While overbased materials having a metal ratio of 75 have been prepared, normally the maximum metal ratio will not exceed 50 and, in most cases, not more than 40. Especially preferred are those having a metal ratio from 7 to 20, except for overbased phenols, wherein the metal ratio generally ranges up to 10, more often up to 5.
  • the overbased materials utilized in the compositions of the invention usually contain from 10% to 70% by weight of metal-containing components. The exact nature of these metal-containing components is not known. The remainder of the overbased materials comprise the inert organic reaction medium and any promoter which is not removed from the overbased product. For purposes of this application, the organic material which is subjected to overbasing is considered a part of the metal-containing components. Normally, the liquid reaction medium constitutes at least about 30% by weight of the reaction mixture utilized to prepare the overbased materials.
  • component A is prepared from phenols; that is, compounds containing a hydroxy radical bound directly to an aromatic ring.
  • phenol as used herein includes compounds having more than one hydroxy group bound to an aromatic ring, such as catechol, resorcinol and hydroquinone. It also includes alkylphenols such as the cresols and ethylphenols, and alkenylphenols.
  • phenols containing at least one alkyl or alkenyl substituent containing 3-100 and especially 6-50 carbon atoms such as heptylphenol, octylphenol, dodecylphenol, tetrapropenealkylated phenol, octadecylphenol and polybutenylphenols. Phenols containing more than one substituent may also be used, but the monoalkylphenols are preferred because of their availability and ease of production.
  • condensation products of the above-described phenols with at least one lower aldehyde the term "lower" denoting aldehydes containing not more than 7 carbon atoms.
  • Suitable aldehydes include formaldehyde, acetaldehyde, propionaldehyde, the butyraldehydes, the valeraldehydes and benzaldehyde.
  • aldehyde-yielding reagents such as paraformaldehyde, trioxane, methylol, Methyl Formcel and paraldehyde. Formaldehyde and the formaldehyde-yielding reagents are especially preferred.
  • the metal phenates are overbased metal phenates, more preferably overbased sulfurized metal phenates, preferably alkaline earth metal phenates, and especially calcium phenates.
  • the phenol group of the phenates includes an aromatic moiety with at least one hydrocarbon-based radical and an oxygen atom attached to such aromatic moiety, as indicated in Formula I, below.
  • the phenol group may be sulfurized and reacted with a metal, as discussed below, to form component (A).
  • the term "normal" metal phenates is used to refer to those phenates wherein the ratio of equivalents of metal to the phenolic O group is about 1:1, in accordance with Formula I (R a - Ar - O -) x M wherein (R a - Ar - O-) is the phenol group; M is a metal; x is the valence of M.
  • Ar is an aromatic moiety which is preferably benzene; R is a hydrocarbon-based radical; and a is an integer of from 1 up to the number of unsatisfied valences in Ar, preferably 1 or 2.
  • overbased metal phenates refers to metal phenates wherein the ratio of metal to the phenol group is greater than that of normal metal phenates. Such phenates are sometimes referred to interchangeably as "basic” or "overbased".
  • Component (A) generally contains up to 1000%, preferably up to 500%, of the metal present in the corresponding normal metal phenate.
  • component (A) contains from 250% to 450%, preferably up to 350%, of the metal present in the corresponding normal metal phenate.
  • alkali or alkaline earth metals copper or zinc may be used in the phenate of component (A); however, alkaline earth metal compounds are preferred, and calcium is especially preferred.
  • component (A) preferably comprises a sulfurized metal phenate and the metal contents referred to hereinabove apply equally to this preferred embodiment.
  • component (A) is a sulfurized phenate it has a phenol to sulfur group molar ratio of from 2:1 to 1:2, preferably 2:1 to 1:1, and advantageously 4:3.
  • basic is used herein the same way in which it was used in the definition of other components above, that is, it refers to salts having a metal ratio in excess of 1.
  • the neutral and basic salts of phenol sulfides provide antioxidant and detergent properties to the oil compositions of the invention.
  • component (A) includes, for example, basic sulfurized tetrapropenyl phenate with, for example, about 230% or 380% of the calcium present in the corresponding normal calcium phenate, and a phenol to sulfur group molar ratio of about 4:3.
  • the alkylphenols from which the neutral and overbased salts are prepared generally comprise phenols containing hydrocarbon substituents with at least 6 carbon atoms; the substituents may contain up to 700 aliphatic carbon atoms. Also included are substantially hydrocarbon substituents, as defined hereinabove.
  • the preferred hydrocarbon substituents are derived from the polymerization of olefins such as ethylene, propene, etc.
  • alkylphenol sulfides is meant to include di-(alkylphenol)monosulfides, disulfides, polysulfides, and other products obtained by the reaction of the alkylphenol with sulfur monochloride, sulfur dichloride or elemental sulfur.
  • the molar ratio of the phenol to the sulfur compound can be, depending on the sulfur compound, from 1:0.5 to 1:1.5, or higher.
  • phenol sulfides are readily obtained by mixing, at a temperature above about 60°C, one mole of an alkylphenol and about 0.5-1 mole of sulfur dichloride. The reaction mixture is usually maintained at about 100°C for about 2-5 hours, after which time the resulting sulfide is stripped of volatiles and filtered.
  • temperatures of about 200°C or higher are sometimes desirable. It is also desirable that the drying operation be conducted under nitrogen or a similar inert gas.
  • a commonly employed method for preparing the basic (or overbased) salts of these phenols comprises heating the phenol with a stoichiometric excess of a metal neutralizing agent such as a metal oxide, hydroxide, carbonate, bicarbonate, sulfide, etc., at temperatures above about 50°C.
  • a metal neutralizing agent such as a metal oxide, hydroxide, carbonate, bicarbonate, sulfide, etc.
  • promoters may be used in the overbasing process to aid in the incorporation of the excess metal. Promoters include such compounds as phenolic substances including phenol; alcohols such as methanol, 2-propanol, octyl alcohol, etc.; amines such as aniline and dodecyl amine, etc.
  • the basic salt is treated with carbon dioxide after it has been formed.
  • Neutral salts are prepared by mixing and heating a basic metal compound with the desired phenol compound.
  • the preparation of basic (overbased) phenates can be accomplished by any of the standard techniques known to those skilled in the art for producing basic sulfurized metal phenates. These techniques include, for example, one-step processes wherein sulfurization and basing (or overbasing) with the metal are effected simultaneously, and two-step processes wherein the phenol is first sulfurized, forming an alkylphenol sulfide, then based. Each of these techniques is well known to those skilled in the art and, accordingly, need not be further discussed herein.
  • the source of sulfur is generally elemental sulfur, or sulfur halide, for example, SCl 2 or S 2 Cl 2 .
  • Patents disclosing suitable procedures for preparing component (B) include U.S. Pat. Nos. 2,680,096; 3,036,971; 3,178,368; 3,437,595; and Re 29,661.
  • Suitable basic alkyl phenol sulfides are disclosed, for example, in U.S. Pat. Nos. 3,372,116, 3,410,798 and 3,562,159, 4,021,419 and 4,740,321.
  • the metal salts, component (A) are generally employed in the compositions of this invention in amounts ranging from 0.01 to 5% by weight of the total lubricating oil composition. More often, they are used in amounts ranging from 0.02 to 5%, frequently up to 2% and preferably from 0.01% to 1% by weight of the lubricating compositions.
  • Examples A-1 through A-10 are non-limiting examples of the preparation of metal carboxylates, sulfonates and mixtures thereof.
  • the methanol and other volatile materials are stripped from the carbonated mixture by blowing nitrogen through it at 57 l/h (2 cfh) while the temperature is slowly increased to 150°C over 90 minutes. After stripping is completed, the remaining mixture is held at 155°C-165°C for about 30 minutes and filtered to yield an oil solution of the desired basic sodium sulfonate having a metal ratio of about 7.75.
  • Example A-1 a solution of 780 parts (1 equivalent) of an alkylated benzenesulfonic acid (57% by weight 100 neutral mineral oil and unreacted alkylated benzene) and 119 parts of the polybutenyl succinic anhydride in 442 parts of mineral oil is mixed with 800 parts (20 equivalents) of sodium hydroxide and 704 parts (22 equivalents) of methanol. The mixture is blown with carbon dioxide at 198 l/h (7 cfh) for 11 minutes as the temperature slowly increases to 97°C. The rate of carbon dioxide flow is reduced to 170 l/h (6 cfh) and the temperature decreases slowly to 88°C over about 40 minutes.
  • an alkylated benzenesulfonic acid 57% by weight 100 neutral mineral oil and unreacted alkylated benzene
  • 119 parts of the polybutenyl succinic anhydride in 442 parts of mineral oil is mixed with 800 parts (20 equivalents) of sodium hydroxide and 704 parts (22
  • the rate of carbon dioxide flow is reduced to 5 cfh for about 35 minutes and the temperature slowly decreases to 73°C.
  • the volatile materials are stripped by blowing nitrogen through the carbonated mixture at 57 l/h (2 cfh) for 105 minutes as the temperature is slowly increased to 160°C. After stripping is completed, the mixture is held at 160°C for an additional 45 minutes and then filtered to yield an oil solution of the desired basic sodium sulfonate having a metal ratio of about 19.75.
  • a mixture of 906 parts of an oil solution of an alkyl phenyl sulfonic acid (having a molecular weight of 450), 564 parts mineral oil, 600 parts toluene, 98.7 parts magnesium oxide and 120 parts water is blown with carbon dioxide at a temperature of 78°-85°C for 7 hours at a rate of about 85 l/h (3 cubic feet) of carbon dioxide per hour.
  • the reaction mixture is constantly agitated throughout the carbonation. After carbonation, the reaction mixture is stripped to 165°C/20 torr and the residue filtered.
  • the filtrate is an oil solution (34% oil) of the desired overbased magnesium sulfonate having a metal ratio of about 3.
  • a polybutenyl succinic anhydride is prepared by reacting a chlorinated polybutene (having an average chlorine content of 4.3% and derived from a polybutene consisting predominantly of isobutene units having a number average molecular weight of about 1150) with maleic anhydride at about 200°C.
  • a chlorinated polybutene having an average chlorine content of 4.3% and derived from a polybutene consisting predominantly of isobutene units having a number average molecular weight of about 1150
  • maleic anhydride at about 200°C.
  • the mixture is heated to 115°C and 125 parts of water is added drop-wise over a period of one hour.
  • the mixture is then allowed to reflux at 150°C until,all the barium oxide is reacted. Stripping and filtration provides a filtrate
  • a basic calcium sulfonate having a metal ratio of about 15 is prepared by carbonation, in increments, of a mixture of calcium hydroxide, a neutral sodium petroleum sulfonate, calcium chloride, methanol and an alkyl phenol, followed by removal of volatile materials and filtration of the residue.
  • a mixture of 323 parts of mineral oil, 4.8 parts of water, 0.74 parts of calcium chloride, 79 parts of lime, and 128 parts of methyl alcohol is prepared, and warmed to a temperature of about 50°C.
  • 1000 parts of an alkyl phenyl sulfonic acid having a molecular weight of 500 with mixing.
  • the mixture then is blown with carbon dioxide at a temperature of about 50°C at a rate of about 2.45 kg/h (5.4 pounds per hour) for about 2.5 hours.
  • 102 additional parts of oil are added and the mixture is stripped of volatile materials at a temperature of about 150-155°C at 55 mm. pressure.
  • the residue is filtered and the filtrate is the desired oil solution of the overbased calcium sulfonate having calcium content of about 3.7% and a metal ratio of about 1.7.
  • a mixture of 490 parts (by weight) of a mineral oil, 110 parts of water, 61 parts of heptylphenol, 340 parts of barium mahogany sulfonate, and 227 parts of barium oxide is heated at 100°C for 0.5 hour and then to 150°C. Carbon dioxide is then bubbled into the mixture until the mixture is substantially neutral. The mixture is filtered and the filtrate found to have a sulfate ash content of 25%.
  • the filtrate will comprise the basic carboxylic magnesium salt containing 200% of the stoichiometrically equivalent amount of magnesium.
  • the filtrate will comprise the basic carboxylic magnesium salts and have a sulfated ash content of 15.7% (sulfated ash) corresponding to 276% of the stoichiometrically equivalent amount.
  • a reaction mixture comprising 2900 grams (3 equivalents) of an oil solution of the magnesium salt of polyisobutylene (average molecular weight--480)-substituted salicyclic acids, 624 grams of mineral oil, 277 grams (1 equivalent) of a commercial mixture of tall oil acids, 1800 grams of xylene, 195 grams (9 equivalents) of magnesium oxide, and 480 grams of water are carbonated at the reflux temperature (about 95°C) for one hour.
  • the carbonated mixture is then stripped by first heating to 160°C with nitrogen blowing 85 l/h (3 cubic feet per hour) and thereafter heating to 165°C at a pressure of 30 mm. (Hg).
  • This stripped carbonated product is filtered, the filtrate being an oil solution of the desired basic magnesium salt.
  • the salt is characterized by a metal ratio of 2.7.
  • a phenol sulfide is prepared by reacting sulfur dichloride with a polyisobutenyl phenol in which the polyisobutenyl substituent has an average of 23.8 carbon atoms, in the presence of sodium acetate (an acid acceptor used to avoid discoloration of the product).
  • a mixture of 1755 parts of this phenol sulfide, 500 parts of mineral oil, 335 parts of calcium hydroxide and 407 parts of methanol is heated to 43-50°C and carbon dioxide is bubbled through the mixture for about 7.5 hours. The mixture is then heated to drive off volatile matter, an additional 422.5 parts of oil are added to provide a 60% solution in oil. This solution contains 5.6% calcium and 1.59% sulfur.
  • the mixture is maintained at 110°C for 2 hours, heated to 165°C and maintained at this temperature until it is dry. Thereupon, the mixture is cooled to 25°C and 180 parts of methanol are added. The mixture is heated to 50°C and 366 parts (9.9 equivalents) of calcium hydroxide and 50 parts (0.633 equivalent) of calcium acetate are added. The mixture is agitated for 45 minutes and is then treated at 50-70°C with carbon dioxide at a rate of 57 - 142 l/h (2-5 cubic feet per hour) for 3 hours. The mixture is dried at 165°C and the residue is filtered. The filtrate has a calcium content of 3.3%, a neutralization number of 39 (basic) and a metal ratio of 4.4.
  • the mixture is maintained at 95-110°C for 2 hours, heated to and maintained at 160°C for one hour and then cooled to 60°C whereupon 920 parts of 1-propanol, 307 parts (10.95 equivalents) of calcium oxide, and 46.3 parts (0.78 equivalent) of acetic acid are added.
  • the mixture is then contacted with carbon dioxide at a rate of 57 l/h (2 cubic feet per hour) for 2.5 hours.
  • the mixture is dried at 190°C and the residue is filtered to give the desired product.
  • a mixture of 485 parts (1 moles OH) of a polyisobutene-substituted phenol wherein the substituent has a number average molecular weight of about 400, 32 parts (1 equivalent) of sulfur, 111 parts (3 equivalents) of calcium hydroxide, 16 parts (0.2 equivalent) of calcium acetate, 485 parts of diethylene glycol monomethyl ether and 414 parts of mineral oil is heated at 120-205°C under nitrogen for 4 hours. Hydrogen sulfide evolution begins as the temperature rises above 125°C. The material is allowed to distill and hydrogen sulfide is absorbed in a sodium hydroxide solution. Heating is discontinued when no further hydrogen sulfide absorption is noted; the remaining volatile material is removed by distillation at 95°C/10 mm Hg pressure. The distillation residue is filtered. The product thus obtained is a 60% solution of the desired product in mineral oil.
  • Component (B) is an aliphatic carboxylic acid or an anhydride thereof, wherein the aliphatic group contains at least 20 carbon atoms and up to 500 carbon atoms, preferably from 30 to 300 carbon atoms and often from 30 to 150 carbon atoms.
  • component (B) is an aliphatic substituted succinic anhydride or acid containing from 20 to 500 carbon atoms in the aliphatic substituent, preferably from 30 to 400 carbon atoms, and often from 50 to 200 carbon atoms.
  • Patents describing useful aliphatic carboxylic acids or anhydrides and methods for preparing them include, among numerous others, U.S. Pat. Nos.
  • the carboxylic acids are usually derived by the reaction of a carboxylic acid containing compound with a polyalkene or halogenated derivative thereof or a suitable olefin.
  • the polyalkenes from which the carboxylic acids (B) are derived are homopolymers and interpolymers of polymerizable olefin monomers of 2 to 16 carbon atoms; usually 2 to 6 carbon atoms.
  • the interpolymers are those in which two or more olefin monomers are interpolymerized according to well-known conventional procedures to form polyalkenes having units within their structure derived from each of said two or more olefin monomers.
  • "interpolymer(s)" as used herein is inclusive of copolymers, terpolymers, tetrapolymers, and the like.
  • the polyalkenes from which the substituent groups are derived are often conventionally referred to as "polyolefin(s)".
  • monolefinic monomers such as ethylene, propylene, butene-1, isobutene, and octene-1 or polyolefinic monomers (usually diolefinic monomers) such as butadiene-1,3 and isoprene.
  • internal olefin monomers When internal olefin monomers are employed, they normally will be employed with terminal olefins to produce polyalkenes which are interpolymers.
  • a particular polymerized olefin monomer can be classified as both a terminal olefin and an internal olefin, it will be deemed to be a terminal olefin.
  • 1,3-pentadiene i.e., piperylene
  • Preferred carboxylic acids include polyolefin substituted succinic acids, succinic anhydrides, ester acids or lactone acids.
  • Component (B) is generally used in the lubricating oil compositions of this invention in amounts ranging from 0.01% to 10% by weight of the lubricating oil composition, preferably from 0.01% to 5% by weight and often up to 1% by weight. Most preferably, component (B) is present in amounts ranging from 0.02% to 1% by weight.
  • Non-limiting examples of compounds useful as component (B) include those in the following examples:
  • a mixture of 6400 parts (4 moles) of a polybutene comprising predominantly isobutene units and having a molecular weight of about 1600 and 408 parts (4.16 moles) of maleic anhydride is heated at 225-240°C for 4 hours. It is then cooled to 170°C and an additional 102 parts (1.04 moles) of maleic anhydride is added, followed by 70 parts (0.99 mole) of chlorine; the latter is added over 3 hours at 170-215°C. The mixture is heated for an additional 3 hours at 215°C and is then vacuum stripped at 220°C and filtered through diatomaceous earth. The product is the desired polybutenyl-substituted succinic anhydride having a saponification number of 61.8.
  • a monocarboxylic acid is 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 temperature.
  • 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 according with the procedure described in British Patent No. 581,899.
  • a polybutenyl succinic anhydride is prepared by the reaction of a chlorinated polybutylene with maleic anhydride at 200°C.
  • the polybutenyl radical has an average molecular weight of 805 and contains primarily isobutene units.
  • the resulting alkenyl succinic anhydride is found to have an acid number of 113 (corresponding to an equivalent weight of 500).
  • a lactone acid is prepared by reacting 2 equivalents of a polyolefin (Mn about 900) substituted succinic anhydride with 1.02 equivalents of water at a temperature of about 90°C in the presence of a catalytic amount of concentrated sulfuric acid. Following completion of the reaction, the sulfuric acid catalyst is neutralized with sodium carbonate and the reaction mixture is filtered.
  • An ester acid is prepared by reacting 2 equivalents of an alkyl substituted succinic anhydride having an average of about 35 carbon atoms in the alkyl group with 1 mole of ethanol.
  • a reactor is charged with 1000 parts of polybutene having a molecular weight determined by vapor phase osmometry of about 950 and which consists primarily of isobutene units, followed by the addition of 108 parts of moleic anhydride.
  • the mixture is heated to 110°C followed by the sub-surface addition of 100 parts Cl 2 over 6.5 hours at a temperature ranging from 110 to 188°C.
  • the exothermic reaction is controlled as not to exceed 188°C.
  • the batch is blown with nitrogen then stored.
  • Example B-7 The procedure of Example B-7 is repeated employing 1000 parts of polybutene having a molecular weight determined by vapor phase osmometry of about 1650 and consisting primarily of isobutene units and 106 parts moleic anhydride. Cl 2 is added beginning at 130°C and added a near continuous rate such that the maximum temperature of 188°C is reached near the end of chlorination. The residue is blown with nitrogen and collected.
  • compositions of the present invention may also contain (C) a metal salt of (C)(I) at least one organic phosphorus acid or mixture of (C)(I) at least one organic phosphorus acid and (C)(II) at least one carboxylic acid.
  • the phosphorus acid (B)(I) is preferably at least one acid of the general formula wherein R 1 and R 2 is the same or different and each of R 1 and R 2 is independently H or a hydrocarbon-based group with the proviso that at least one of R 1 and R 2 is a hydrocarbon-based group and each X is independently S or 0.
  • the phosphorus acid (C)(I) has the general formula wherein R 1 and R 2 are as defined hereinabove. These are referred to as phosphorodithioic acids.
  • the hydrocarbon-based groups R 1 and R 2 may be alkyl, cycloalkyl, aralkyl or alkaryl groups.
  • Illustrative alkyl groups include isopropyl, isobutyl, n-butyl, sec-butyl, the various amyl groups, n-hexyl, ethylisobutyl carbinyl, heptyl, 2-ethylhexyl, diisobutyl, isooctyl, nonyl, behenyl, decyl, dodecyl, tridecyl, etc.
  • Illustrative alkaryl groups include lower alkylphenyl groups such as butylphenyl, amylphenyl, heptylphenyl, etc. Cycloalkyl groups likewise are useful and these include chiefly cyclohexyl and the lower alkyl-cyclohexyl radicals. Lower alkyl groups contain from one to about seven carbon atoms. Many substituted hydrocarbon groups may also be used, e.g., chloropentyl, dichlorophenyl, and dichlorodecyl.
  • Preferred acids of the general formula are readily obtainable from the reaction of phosphorus pentasulfide (P 2 S 5 ) with an alcohol or mixtures of alcohols.
  • the reaction involves mixing at a temperature of 20°C to 200°C, 4 moles of the alcohol with one mole of phosphorus pentasulfide. Hydrogen sulfide is liberated in this reaction.
  • the oxygen-containing analogs of these acids are conveniently prepared by treating the dithioic acid with water or steam which, in effect, replaces one or both of the sulfur atoms.
  • the mixed phosphates are readily prepared by reacting 3 moles of an alcohol with 1 mole of phosphorus pentoxide (P 2 O 5 ).
  • hydrocarbon-based group as used herein with respect to R 1 and R 2 is used to define a monovalent radical derived from a hydrocarbon-based material by removal of a hydrogen from a carbon atom of the hydrocarbon-based material. This carbon atom is directly bonded to the remainder of the molecule.
  • the hydrocarbon-based groups may be straight chains, e.g., isopropyl-, n-pentyl, sec-butyl-, etc. or branched, e.g., 2-methyl-4-pentyl-, isooctyl-, etc.
  • the groups R 1 and R 2 are substantially saturated.
  • double bonds in aromatic rings (e.g., benzene) are not to be considered as contributing to unsaturation with respect to the terminology “substantially saturated”.
  • aromatic rings e.g., benzene
  • all the carbon-to-carbon bonds in a substantially saturated radical will be saturated linkages; that is, the radical will be free from acetylenic and ethylenic linkages.
  • aromatic unsaturation is not to be considered ethylenic unsaturation.
  • the hydrocarbon-based radical may contain at least 3 carbon atoms and up to 100 carbon atoms with a preferred range from 3 to 50 carbon atoms, more preferably from 3 to 16 carbon atoms. Other preferred ranges are from 6 to 18 carbons, more preferably from 6 to 8 carbons. Mixtures wherein R 1 and R 2 are different are useful. Typical examples of R and R 1 include isopropyl-, n-butyl-, n-pentyl-, 4-methyl-2-pentyl-, isooctyl-, n-dodecyl-, etc.
  • Mixtures such as isopropyl- and isooctyl, sec-butyl and n-decyl-, isopropyl- and 4-methyl-2-pentyl- and the like are useful. Mixtures are often statistical mixtures which comprise a mixture wherein some of the molecules have both R 1 and R 2 alike and additional molecules wherein R 1 and R 2 are different.
  • lower when used herein to denote radicals such as lower alkyl is intended to describe a radical containing up to 7 carbon atoms.
  • the salts are prepared by reacting one or more of the phosphorus-containing acids described hereinabove with a metal base.
  • Suitable metal bases include the free metals previously enumerated and their oxides, hydroxides, alkoxides and basic salts. Examples include sodium hydroxide, calcium hydroxide, zinc oxide, copper oxide, calcium acetate and the like.
  • Other methods include "double-displacement" reactions wherein one metal salt of a phosphorus acid is reacted with a salt, such as a halide, of another metal. Metal exchange may take place.
  • a sodium dithiophosphate can be reacted with calcium chloride to form a calcium dithiophosphate and sodium chloride.
  • Sodium chloride is then removed by means commonly used in the art, such as filtration, water washing, etc.
  • metal salts of phosphorus-containing acids as described hereinabove, which have been post-treated with other reagents to improve various properties.
  • Examples include post-treatments with phosphites, epoxides, amines and the like. Such post-treatments and products so obtained are described in the following U.S. Patents: 3,004,996 3,213,022 3,151,075 3,213,023 3,211,648 4,263,150 3,211,649 4,289,635 3,213,020 4,507,215 3,213,021
  • the metal salts (C) useful in the lubricating compositions of this invention may be metal salts of a mixture of (C)(I) at least one organic phosphorus acid and (C)(II) at least one carboxylic acid wherein the various elements of the formula are as described hereinabove.
  • These metal salts are salts of at least two acidic components.
  • the phosphorus-containing acids (C)(I) have been described hereinabove.
  • the carboxylic acid reactant (C)(II) may be a monocarboxylic or polycarboxylic acid, usually containing from 1 to 3 carboxy groups and preferably only 1. It may contain from 2 to 40, preferably from 2 to 20 carbon atoms.
  • the preferred carboxylic acids are those having the formula R 3 COOH, wherein R 3 is an aliphatic or alicyclic hydrocarbon-based group preferably free from acetylenic unsaturation.
  • Suitable acids include acetic, propionic, butanoic, hexanoic, decanoic, dodecanoic, octadecanoic and eicosanoic acids, as well as olefinic acids such as acrylic, oleic, linoleic, and linoleic acid dimer.
  • R 3 is a saturated aliphatic radical and especially a branched alkyl radical such as the isopropyl or 3-heptyl radical.
  • Illustrative polycarboxylic acids are oxalic, malonic, succinic, alkyl- and alkenylsuccinic, glutaric, adipic, pimelic, sebacic, maleic, fumaric and citric acids.
  • the salt of a mixture of (C)(I) and (C)(II) may be prepared by merely blending a metal salt of compoment (C)(I) with a metal salt of component (C)(II) in the desired ratio.
  • This ratio is between 0.5:1 and 500:1 on an equivalent basis.
  • the ratio is between 0.5:1 and 200:1.
  • the ratio can be from 0.5:1 to 100:1, preferably from 0.5:1 to 50:1, and more preferably from 0.5:1 to 20:1.
  • the ratio can be from 0.5:1 to 4.5:1, preferably 2.5:1 to 4.25:1.
  • the equivalent weight of a phosphorus containing acid (C) (I) is its molecular weight divided by the number of acidic groups, and that of a carboxylic acid is its molecular weight divided by the number of carboxy groups therein.
  • the information required to determine equivalents can usually be determined from the structural formula of components (C)(I) and (C)(II) or empirically through well-known titration procedures.
  • a second and preferred method for preparing the metal salts of mixtures of acids (C) (I) and (C) (II) is to prepare a mixture of the acids in the desired ratio and to react the acid mixture with a suitable metal base.
  • this method of preparation it is frequently possible to prepare a neutral salt or a salt containing an excess of metal with respect to the number of equivalents of acid present; thus, mixed metal salts containing as many as 2 equivalents and especially up to about 1.5 equivalents of metal per equivalent of acid may be prepared.
  • the equivalent of a metal for this purpose is its atomic weight divided by its valence.
  • neutral salt refers to salts characterized by metal content equal to that which would be present according to the stoichiometry of the metal and the particular organic compound reacted with the metal.
  • a phosphorodithioic acid (RO) 2 PSSH
  • a basic metal compound e.g., zinc oxide
  • the neutral metal salt produced would contain one equivalent of zinc for each equivalent of acid, i.e., [(RO) 2 PSS] 2 Zn.
  • component (C) can contain more or less than the stoichiometric amount of metal.
  • the products containing less than the stoichiometric amount of metal are acidic materials.
  • the products containing more than the stoichiometric amount of metal are overbased materials.
  • Component (C) may have 80% to 200%, preferably 100% to 150%, more preferably 100% to 135%, and advantageously 103% to 110% of the metal present in the corresponding neutral salt.
  • Variants of the above-described methods may also be used to prepare the mixed metal salts of this invention.
  • a metal salt, component (C) may be blended with the free acid as component (C)(II), and the resulting blend reacted with additional metal base.
  • Suitable metal bases for the preparations of the metal salts (C) of this invention include the free metals previously enumerated and their oxides, hydroxides, alkoxides and basic salts. Examples are sodium hydroxide, sodium methoxide, sodium carbonate, potassium hydroxide, potassium carbonate, magnesium oxide, magnesium hydroxide, calcium hydroxide, calcium acetate, zinc oxide, zinc acetate, lead oxide, nickel oxide, copper oxide, antimony trioxide and the like.
  • the temperature at which the metal salts used in this invention are prepared is generally between 30°C and 150°C, preferably up to 125°C. If component (C) is prepared by neutralization of a mixture of acids with a metal base, it is preferred to employ temperatures above 50°C and especially above 75°C. It is frequently advantageous to conduct the reaction in the presence of a substantially inert, normally liquid organic diluent such as naphtha, benzene, xylene, mineral oil or the like. If the diluent is mineral oil or is physically and chemically similar to mineral oil, it frequently need not be removed before using component (C) in the compositions of the invention.
  • a substantially inert, normally liquid organic diluent such as naphtha, benzene, xylene, mineral oil or the like. If the diluent is mineral oil or is physically and chemically similar to mineral oil, it frequently need not be removed before using component (C) in the compositions of the invention.
  • the metal salt (C) may be contacted under reaction conditions with at least one phosphite of the general formula (R 4 O) 3 P wherein each R 4 is independently hydrogen or a hydrocarbon-based group.
  • Component (C), when present, is generally used in the lubricating oil compositions of this invention in amounts ranging up to 10% of the total weight of the lubricating oil composition. More often, component (C), when used, is present in amounts ranging from 0.05% to 5%, preferably from 0.1 to 2% and more preferably from 0.1 to 1% by weight of the lubricating oil composition.
  • Example B-1 The procedure of Example B-1 is repeated employing 1 mole of di(4-methyl-2-pentyl)dithiophosphoric acid and 1.1 equivalents (0.55 moles) of an oil slurry of zinc oxide.
  • the filtered product contains 8.5% phosphorus.
  • Example B-2 The procedure of Example B-2 is repeated except no oil diluent is employed.
  • the filtered product contains 9.25% phosphorus.
  • a mixture of 67 parts (1.63 equivalents) of zinc oxide and 48 parts of mineral oil is prepared at room temperature.
  • a mixture of 303 parts (1 equivalent) of the O,O-di(alkyl)phosphorodithioic acid described in Example 2 and 36 parts (0.25 equivalents) of 2-ethylhexanoic acid is added over 10 minutes and a slight exotherm is observed.
  • the temperature is increased to 80°C for 3 hours.
  • the mixture is vacuum stripped at 100°C and filtered.
  • Example C-4 Following the procedure of Example C-4, a product is prepared from 383 parts (1.2 equivalents) of a dialkyl phosphorodithioic acid containing 65% isobutyl and 35 % amyl groups, 43 parts (0.3 equivalent) of 2-ethylhexanoic acid, 71 parts (1.73 equivalents) of zinc oxide and 47 parts of mineral oil.
  • the resulting metal salt obtained as a 90% solution in mineral oil, contains 11.07% zinc.
  • Example C-4 Following the procedure of Example C-4, a product is prepared from 474 parts (1.2 equivalents) of a dialkylphosphorodithioic acid containing 80% 2-ethylhexyl groups and 20% isobutyl groups, 43 parts (0.3 equivalent) of 2-ethylhexanoic acid, 80 parts (1.95 equivalents) of zinc oxide and 57 parts of mineral oil.
  • the resulting metal salt is obtained as a 91% solution in mineral oil.
  • a mixture of 118 parts (2.8 equivalents) of zinc oxide, 25 parts (0.25 equivalent) of sebacic acid and 72 parts of mineral oil is stirred at room temperature and a mixture of 584 parts (2 equivalents) of the dialkylphosphorodithioic acid of Example 2 and 36 parts (0.25 equivalent) of 2-ethyl-hexanoic acid is added over 30 minutes. The temperature increases to 65°C during the addition. The solution is heated to 80°C for 3 hours and vacuum stripped at 180°C. The residue is filtered to yield the desired metal salt (90% solution in mineral oil) containing 11.7% zinc.
  • a product is prepared by the procedure of Example C-4 except that an equivalent amount of oleic acid is substituted for the 2-ethylhexanoic acid.
  • Triphenyl phosphite is heated with a zinc salt of a mixture of a dialkylphosphorodithioic acid and a carboxylic acid.
  • the dialkylphosphorodithioic acid used in the preparation of the zinc salt is itself prepared by the reaction of at least one alcohol with phosphorus pentasulfide which contains a stoichiometric excess of sulfur. The reaction conditions and results are given in Table I.
  • the salts are prepared by reacting zinc oxide with 4 equivalents of the dialkylphosphorodithioic acid and 1 equivalent of the carboxylic acid, a total of 1.3 equivalents of zinc oxide being used per equivalent of acid. The reactions are carried out in a small amount of mineral oil as diluent.
  • a reaction mixture is prepared by the addition of 3120 parts (24.0 moles) of 2-ethylhexanol and 444 parts (6.0 moles) of isobutyl alcohol. With nitrogen blowing at 28 l/h (1.0 cubic feet per hour), 1540 parts (6.9 moles) of P 2 S 5 is added to the mixture over a two-hour period while maintaining the temperature at 60-78°C. The mixture is held at 75°C for one hour and is stirred an additional two hours while cooling. The mixture is filtered through diatomaceous earth.
  • a slurry is prepared by the addition of 486.6 parts (11.86 equivalents) of ZnO and 243.1 parts diluent oil. With medium speed stirring 1204 parts (3.6 equivalents) of O,O-di(4-methyl-2-pentyl)phosphorodithioic acid are added to the slurry and the temperature of the resulting mixture is increased from 56°C to 87°C over a period of 20 minutes. 2407 parts (7.2 equivalents) of O,O-di-(4-methyl-2-pentyl)phosphorodithioic acid are added to the mixture. The temperature of the mixture is maintained at 86°C for 4 hours. 500 parts of the mixture are poured off.
  • the remaining 3831 parts of mixture are mixed with 156.04 parts of a commercially available mixture of C 15-18 alpha-olefins.
  • the mixture is stripped to 105°C at 15 mm. Hg.
  • the temperature of the mixture is increased from 22°C to 105°C over a 3 1/2 hour period.
  • the mixture is held at 105°C under a nitrogen flow of 14 l/h (0.5 cubic feet per hour) for an additional two hours before being allowed to cool.
  • the mixture is cooled and filtered through diatomaceous earth. The filtrate is the product.
  • Example C-1 The process of Example C-1 is repeated replacing the zinc oxide with about 1.15 equivalents of cuprous oxide.
  • Example C-1 The process of Example C-1 is repeated employing O,O-di(2-ethylhexyl)phosphorodithioic acid.
  • Example C-15 The process of Example C-15 is repeated employing 1 equivalent of copper (I) oxide for each equivalent of zinc oxide.
  • Example C-15 The process of Example C-15 is repeated employing 1 equivalent of: Example No. Metal Compound 17 Manganese (IV) oxide 18 Nickel (II) oxide 19 Molybdenum (VI) oxide 20 Tin (II) oxide
  • the triazole which may be used in this invention may be benzotriazole and alkyl-substituted benzotriazole.
  • the alkyl substituent generally contains up to 15 carbon atoms, preferably up to 8 carbon atoms.
  • the triazoles may contain other substituents on the aromatic ring such as halogens and nitro groups. Examples of suitable compounds are benzotiazole and the tolyltriazoles, ethylbenzotriazoles, hexylbenzotriazoles, octylbenzotriazoles, chlorobenzotriazoles and nitrobenzotriazoles. Benzotriazole and tolyltriazole are particularly preferred.
  • the amount of triazole included in the composition generally is less than 5%, more often less than 1% by weight.
  • the composition of the invention When the composition of the invention is to be used in a lubricating oil such as a hydraulic fluid, only small amounts of the triazole compound are required to obtain improved hydrolytic stability.
  • the composition of the invention will contain an amount of triazole compound which will provide an additive concentrate for lubricants and functional fluid which contains as little as 100 ppm of the triazole and preferably less than 50 ppm of the triazole.
  • compositions of the invention are prepared to provide the lubricant or functional fluid with a stabilizing amount of the triazole which generally is less than 20 ppm, and may be less than 3 ppm of finished lubricant or functional fluid.
  • additives which include, but are not limited to, dispersants, detergents, antioxidants, anti-wear agents, extreme pressure agents, emulsifiers, demulsifiers, foam inhibitors, friction modifiers, anti-rust agents, corrosion inhibitors, viscosity improvers, pour point depressants, dyes, and solvents to improve handleability which may include alkyl and/or aryl hydrocarbons.
  • additives may be present in various amounts depending on the intended application for the final product or may -be excluded therefrom.
  • Dispersants include, but are not limited to, hydrocarbon substituted succinimides, succinamides, carboxylic esters, Mannich dispersants and mixtures thereof as well as materials functioning both as dispersants and viscosity improvers.
  • the dispersants include nitrogen-containing carboxylic dispersants, ester dispersants, Mannich dispersants or mixtures thereof.
  • Nitrogen-containing carboxylic dispersants are prepared by reacting a hydrocarbyl carboxylic acylating agent (usually a hydrocarbyl substituted succinic anhydride) with an amine (usually a polyamine).
  • Ester dispersants are prepared by reacting a polyhydroxy compound with a hydrocarbyl carboxylic acylating agent.
  • the ester dispersant may be further treated with an amine.
  • Mannich dispersants are prepared by reacting a hydroxy aromatic compound with an amine and aldehyde.
  • the dispersants listed above may be post-treated with reagents such as urea, thiourea, carbon disulfide, aldehydes, ketones, carboxylic acids, hydrocarbon substituted succinic anhydride, nitriles, epoxides, boron compounds, phosphorus compounds and the like.
  • reagents such as urea, thiourea, carbon disulfide, aldehydes, ketones, carboxylic acids, hydrocarbon substituted succinic anhydride, nitriles, epoxides, boron compounds, phosphorus compounds and the like.
  • These dispersants are generally referred to as ashless dispersants even though they may contain elements such as boron or phosphorus which, on decomposition, will leave a non-metallic
  • Extreme pressure agents and corrosion- and oxidation-inhibiting agents include chlorinated compounds, sulfurized compounds, phosphorus containing compounds including, but not limited to, phosphosulfurized hydrocarbons and phosphorus esters, metal containing compounds and boron containing compounds.
  • Chlorinated compounds are exemplified by chlorinated aliphatic hydrocarbons such as chlorinated wax.
  • sulfurized compounds are organic sulfides and polysulfides such as benzyl disulfide, bis(chlorobenzyl)disulfide, dibutyl tetrasulfide, sulfurized methyl ester of oleic acid, sulfurized alkylphenol, sulfurized dipentene, and sulfurized terpene.
  • organic sulfides and polysulfides such as benzyl disulfide, bis(chlorobenzyl)disulfide, dibutyl tetrasulfide, sulfurized methyl ester of oleic acid, sulfurized alkylphenol, sulfurized dipentene, and sulfurized terpene.
  • Phosphosulfurized hydrocarbons include the reaction product of a phosphorus sulfide with turpentine or methyl oleate.
  • Phosphorus esters include dihydrocarbon and trihydrocarbon phosphites, phosphates and metal and amine salts thereof.
  • Phosphites may be represented by the following formulae: or (R 5 O) 3 P wherein each R 5 is independently hydrogen or a hydrocarbon based group, provided at least one R 5 is a hydrocarbon based group.
  • each R 5 is independently a hydrogen or hydrocarbon based group having from 1 to 24, more preferably from 1 to 18, and more preferably from 2 to 8 carbon atoms, provided that at least one R 5 is a hydrocarbon based group,
  • Each R 5 may be independently alkyl, alkenyl or aryl. When R 5 is aryl it contains at least 6 carbon atoms; preferably 6 to 18 carbon atoms.
  • alkyl or alkenyl groups are propyl, butyl, hexyl, heptyl, octyl, oleyl, linoleyl, stearyl, etc.
  • aryl groups are phenyl, naphthyl, heptylphenyl, etc.
  • each R 5 is independently propyl, butyl, pentyl, hexyl, heptyl, oleyl or phenyl, more preferably butyl, oleyl or phenyl and more preferably butyl or oleyl.
  • the R 5 groups may also comprise a mixture of hydrocarbyl groups derived from commercial alcohols.
  • preferred monohydric alcohols and alcohol mixtures include commercially available "Alfol" alcohols marketed by Continental Oil Corporation.
  • Alfol 810 is a mixture containing alcohols consisting essentially of straight-chain, primary alcohols having 8 to 10 carbon atoms.
  • Alfol 812 is a mixture comprising mostly C 12 fatty alcohols.
  • Alfol 1218 is a mixture of synthetic, primary, straight-chain alcohols having from 12 to 18 carbon atoms.
  • Alfol 20+ alcohols are mixtures of 18-28 primary alcohols having mostly, on an alcohol basis, C 20 alcohols as determined by GLC (gas-liquid-chromatography).
  • Neodol 23 is a mixture of C 12 and C 13 alcohols
  • Neodol 25 is a mixture of C 12 and C 15 alcohols
  • Neodol 45 is a mixture of C 14 and C 15 linear alcohols
  • Neodol 91 is a mixture of C 9 , C 10 and C 11 alcohols.
  • Phosphites and their preparation are known and many phosphites are available commercially. Particularly useful phosphites are dibutylhydrogen phosphite, trioleyl phosphite and triphenyl phosphite. Preferred phosphite esters are generally dialkyl hydrogen phosphites.
  • dialkyl hydrogen phosphites are commercially available, such as lower dialkyl hydrogen phosphites, which are preferred.
  • Lower dialkyl hydrogen phosphites include dimethyl, diethyl, dipropyl, dibutyl, dipenyl and dihexyl hydrogen phosphites.
  • Phosphate esters include mono-, di- and trihydrocarbon-based phosphates of the general formula (R 5 O) 3 PO wherein R 5 is as defined for the phosphites described hereinabove.
  • R 5 is as defined for the phosphites described hereinabove.
  • Examples include mono-, di- and trialkyl ; mono-, di and triaryl and mixed alkyl and aryl.
  • Specific, non-limiting examples include, tri lower alkyl phosphate, dialkyl phosphates, and the like.
  • Particularly preferred are the reaction products of phosphorus pentoxide (P 2 O 5 ) with alcohols in a ratio of 3 hydroxyl groups to one P 2 O 5 yielding a mixture of mono- and dialkyl phosphates.
  • mixed alkyl hydrogen phosphites are useful in the present invention. Examples of mixed alkyl hydrogen phosphites include ethyl, butyl; propyl, pentyl; and methyl, pentyl hydrogen phosphites.
  • Metal containing compounds include metal thiocarbamates, such as zinc dioctyldithiocarbamate, and barium heptylphenyl dithiocarbamate and molybdenum compounds.
  • Boron containing compounds include borate esters and boron-nitrogen containing compounds prepared, for example, by the reaction of boric acid with a primary or secondary alkyl amine.
  • Viscosity improvers include, but are not limited to, polyisobutenes, polymethacrylate acid esters, polyacrylate acid esters, diene polymers, polyalkyl styrenes, alkenyl aryl conjugated diene copolymers, polyolefins and multifunctional viscosity improvers.
  • Pour point depressants are a particularly useful type of additive often included in the lubricating oils described herein. See for example, page 8 of "Lubricant Additives” by C. V. Smalheer and R. Kennedy Smith (Lesius-Hiles Company Publishers, Cleveland, Ohio, 1967).
  • Anti-foam agents used to reduce or prevent the formation of stable foam include silicones or organic polymers. Examples of these and additional anti-foam compositions are described in "Foam Control Agents", by Henry T. Kerner (Noyes Data Corporation, 1976), pages 125-162.
  • the components may be blended together in any suitable manner and then admixed, for example with a diluent to form a concentrate as discussed below, or with a lubricating oil, as discussed below.
  • components can be admixed separately with such diluent or lubricating oil.
  • the triazole if used, be dissolved first in the diluent by heating to a temperature of 80-90°C followed by cooling before the remaining components are blended into the diluent.
  • the blending technique for mixing the components is not critical and can be effected using any standard technique, depending upon the specific nature of the materials employed. In general, blending can be accomplished at room temperature; however, blending can be facilitated by heating the components.
  • compositions of the present invention are used as wet filterability improving additives for lubricants and functional fluids. They can be employed in a variety of lubricants based on diverse oils of lubricating viscosity, including natural and synthetic lubricating oils and mixtures thereof.
  • the lubricants include crankcase lubricating oils for spark-ignited and compression-ignited internal combustion engines, including automobile and truck engines, two-cycle engines, aviation piston engines, marine and railroad diesel engines, and the like. Also contemplated are lubricants for gas engines, stationary power engines and turbines and the like.
  • Transaxle lubricants, gear lubricants, metal-working lubricants and other lubricating oil and grease compositions, as well as functional fluids such as hydraulic fluids and automatic transmissions fluids, benefit from the incorporation therein of the compositions of the present invention. As discussed hereinabove, this invention provides special benefits when the composition is exposed to water.
  • the lubricating compositions and methods of this invention employ an oil of lubricating viscosity, including natural or synthetic lubricating oils and mixtures thereof.
  • Natural oils include animal oils, vegetable oils, mineral lubricating oils, solvent or acid treated mineral oils, and oils derived from coal or shale.
  • Synthetic lubricating oils include hydrocarbon oils, halo-substituted hydrocarbon oils, alkylene oxide polymers, esters of carboxylic acids and polyols, esters of polycarboxylic acids and alcohols, esters of phosphorus-containing acids, polymeric tetrahydrofurans, silicon-based oils and mixtures thereof.
  • oils of lubricating viscosity are described in U.S. Patent 4,326,972 and European Patent Publication 107,282.
  • a basic, brief description of lubricant base oils appears in an article by D. V. Brock , "Lubricant Base Oils", Lubrication Engineering , volume 43, pages 184-185, March, 1987. This article is herein incorporated by reference for its disclosures relating to lubricating oils.
  • a description of oils of lubricating viscosity occurs in U.S. Patent 4,582,618 (column 2, line 37 through column 3, line 63, inclusive).
  • Component (A) and component (B) are generally used in relative amounts of A:B ranging from 5:1 to 1:5, more often from 2:1 to 1:2, by weight.
  • Component (A) is used in the lubricating oil compositions of this invention in amounts ranging from 0.01 to 5% by weight, often up to 2% by weight. A preferred range is from 0.01 to 1% by weight of the total weight of the composition.
  • Components (B) and (C) are utilized in amounts within the above-specified amounts relative to component (A).
  • compositions to be used in the present invention illustrate compositions to be used in the present invention.
  • the amount of each component in the Examples also reflects the amount of oil present in the indicated components.
  • compositions used in this invention are useful as additives for a wide variety of lubricating compositions.
  • Preferred lubricating compositions are functional fluids, with hydraulic fluids being particularly preferred.
  • the following are non-limiting examples of lubricating compositions used in this invention.
  • Example A-1 To a 100 neutral mineral oil basestock is added, with mixing and gentle heating, 1% by weight of the product of Example A-1, 0.3% by weight of the product of Example B-4, and 0.01 percent by weight of a silicone antifoam.
  • Example 1 To a mineral oil basestock (250 neutral) is added 0.85 percent by weight of the additive concentrate of Example 1.
  • Example 7 is repeated except additive concentrate of Example 1 is replaced with that of Example 4.
  • Example 6 To the lubricating oil composition of Example 6 is added 0.05% by weight of the product of Example C-1.
  • Example 7 is repeated except the additive concentrate of Example 4 replaces that of Example 1.
  • a hydraulic fluid basestock (ISO 46) is added 0.1 parts of dibutyl hydrogen phosphite, 0.01 parts of tolyltriazole, 0.1 parts of a magnesium salicylate, 0.05 parts of the reaction product of propylene oxide with tetrapropenyl succinic anhydride, 0.2 parts of tricresyl phosphate, 0.25 parts of hindered phenol, 0.25 parts of di(nonylphenyl) amine and 0.05 parts of the product of Example B-7.
  • a hydraulic fluid is prepared according to the procedure of Example 13 replacing 0.05 parts of the product of Example B-7 with 0.03 parts of the product of Example B-6.
  • a composition comprising an oil of lubricating viscosity, 0.85 percent by weight of the product of Example A-4, 0.15 parts of the product of Example B-6, 0.2 parts of hindered phenol, 0.002 percent by weight of tolyltriazole and 0.01 percent by weight of an organic polymer antifoam.
  • Example 7 replacing the product of Example C-11 with that of Example C-16.
  • the filterability of hydraulic fluids can be determined employing the AFNOR E48-690/1 test published by l'Association Francaise DeNormalisation, Tour Europe Cedex 7 92 080 Paris-La Defense, France. This test consists of filtering, under constant pressure, at constant temperature, through a membrane with a determined absolute stopping power, a specified volume of fluid contained in a container of defined dimensions. This test employs an essentially uncontaminated fluid.
  • a modification of this test entails the use of a water-treated fluid. To the fluid is added a fixed amount of water, the mixture is agitated, then stored. After the aging period, the water-treated fluid is evaluated as above.

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Claims (42)

  1. Verwendung einer Zusammensetzung zur Verbesserung der Feuchtfiltrierbarkeit in einer Schmiermittelzusammensetzung mit einer größeren Menge eines Öls mit Schmierviskosität, umfassend:
    (A) ein Metallsalz, ausgewählt aus der Gruppe bestehend aus Sulfonaten, Phenaten, Carboxylaten und deren Gemischen, und
    (B) eine wirksame Menge einer aliphatischen Carbonsäure oder deren Anhydrid, wobei der aliphatische Rest mindestens 20 Kohlenstoffatome enthält, und wobei die relativen Gewichtsmengen von (A) : (B) im Bereich von 5:1 bis 1:5 liegen.
  2. Die Verwendung nach Anspruch 1, wobei
    (A) ein Alkali- oder Erdalkalimetallphenat ist,
    (B) eine aliphatisch-substituierte Bernsteinsäure oder deren Anhydrid ist, wobei der aliphatische Rest 30 bis 400 Kohlenstoffatome enthält, und zusätzlich
    (C) ein Metallsalz von (C)(I) mindestens einer organischen Phosphorsäure oder eines Gemisches von (C)(I) mindestens einer Phosphorsäure und (C)(II) mindestens einer Monocarbonsäure oder Polycarbonsäure mit 2 bis 40 Kohlenstoffatomen und wobei die relativen Gewichtsmengen von (A) : (B) im Bereich von 5:1 bis 1:5 und von (A) : (C) im Bereich von 1:40 bis 2:1 liegen.
  3. Die Verwendung nach Anspruch 1 oder 2, wobei (A) ein überbasisches Metallsalz ist.
  4. Die Verwendung nach einem der Ansprüche 1 bis 3, wobei das Metallsalz (A) ein Alkalimetall-, Erdalkalimetall-, Kupfer- oder Zinksalz ist.
  5. Die Verwendung nach Anspruch 1 oder 2, wobei (A) ein Calciumphenat ist.
  6. Die Verwendung nach Anspruch 5, wobei (A) ein geschwefeltes Calciumphenat ist.
  7. Die Verwendung nach Anspruch 1, wobei (B) eine Polyolefin-substituierte Bernsteinsäure oder deren Anhydrid, Estersäure oder Lactonsäure ist.
  8. Die Verwendung nach Anspruch 7, wobei der Polyolefin-Substituent eine Polyethylengruppe, eine Polypropylengruppe, eine Polybutylengruppe oder deren Gemisch ist.
  9. Die Verwendung nach Anspruch 3, wobei (A) ein überbasisches Metallsalicylat ist.
  10. Die Verwendung nach einem der Ansprüche 1 bis 9, weiter umfassend ein Phoshit, ausgewählt aus der Gruppe bestehend aus Dialkylhydrogenphosphiten, Trialkylphosphiten und Triarylphosphiten.
  11. Die Verwendung nach einem der Ansprüche 2 bis 10, wobei die organische Phosphorsäure (C)(I) mindestens eine Säure der allgemeinen Formel I
    Figure 00780001
    ist, in der R1 und R2 gleich oder verschieden sind und jeder der Reste R1 und R2 ein Wasserstoffatom oder eine Gruppe auf Kohlenwasserstoffbasis ist, mit der Maßgabe, daß mindestens einer der Reste R1 und R2 eine Gruppe auf Kohlenwasserstoffbasis ist, und jeder Rest X unabhängig ein Schwefel- oder Sauerstoffatom bedeutet, und die Carbonsäure (C) (II) eine aliphatische oder alicyclische Carbonsäure mit 2 bis 40 Kohlenstoffatomen ist.
  12. Die Verwendung nach Anspruch 11, wobei die Phosphorsäure (C) (I) mindestens eine Dithiophosphorsäure der allgemeinen Formel
    Figure 00790001
    ist, in der jeder Rest R1 und R2 gleich oder verschieden ist und jeder Rest R1 und R2 unabhängig einen Alkylrest mit 3 bis 50 Kohlenstoffatomen bedeutet, und die Carbonsäure
    (C) (II) mindestens eine Carbonsäure der allgemeinen Formel R3COOH ist, in der R3 ein aliphatischer oder alicyclischer Rest auf Kohlenwasserstoffbasis mit 2 bis 40 Kohlenstoffatomen ist.
  13. Die Verwendung nach einem der Ansprüche 2 bis 12, wobei das Verhältnis der Äquivalente von (C) (I) zu (C) (II) 0,5:1 bis 500:1 beträgt.
  14. Die Verwendung nach Anspruch 2, wobei das Metallsalz von (C) mindestens eines der Gruppe I-Metalle, Gruppe II-Metalle, Aluminium, Zinn, Kobalt, Molybdän, Blei, Mangan und Nickel ist.
  15. Die Verwendung nach Anspruch 14, wobei das Metallsalz von (C) ein Zinksalz ist.
  16. Die Verwendung nach Anspruch 2, wobei das Metallsalz (C) unter Reaktionsbedingungen mit mindestens einem Phosphit der allgemeinen Formel (R4O)3P zusammengebracht wird, wobei jeder Rest R4 unabhängig ein Wasserstoffatom oder ein Rest auf Kohlenwasserstoffbasis ist.
  17. Die Verwendung nach Anspruch 2, wobei das Additiv zusätzlich (D) mindestens ein basisches Alkali- oder Erdalkalimetallsalz einer organischen Sulfonsäure enthält.
  18. Die Verwendung nach einem der Ansprüche 1 bis 17, umfassend zusätzlich mindestens ein Mitglied, ausgewählt aus der Gruppe bestehend aus einer phenolischen antioxidierenden Verbindung, einem aschefreien Dispersant und einem Demulgator.
  19. Die Verwendung nach Anspruch 1 oder 2, wobei (A) in Mengen von etwa 0,01 bis 5 Gew.-% vorliegt.
  20. Die Verwendung nach einem der Ansprüche 1 bis 19, wobei das Additiv zusätzlich (E) eine stabilisierende Menge eines Triazols in einer Menge von weniger als 5 Gew.-% enthält.
  21. Die Verwendung einer Zusammensetzung zur Verbesserung der Feuchtfiltrierbarkeit in einer funktionellen Flüssigkeit mit einer größeren Menge eines Öls mit Schmierviskosität, umfassend:
    (A) ein Metallsalz der Gruppe I oder Gruppe II, ausgewählt aus der Gruppe bestehend aus Sulfonaten, Phenaten, Carboxylaten und deren Gemischen nach einem der Ansprüche 1 bis 6, und
    (B) eine wirksame Menge einer aliphatischen Carbonsäure oder deren Anhydrid, wobei der aliphatische Rest mindestens 20 Kohlenstoffatome enthält, nach einem der Ansprüche 1, 2, 7 und 8, und wobei die relativen Gewichtsmengen von (A) : (B) im Bereich von 5:1 bis 1:5 liegen.
  22. Verfahren zur Verbesserung der Feuchtfiltrierbarkeit eines Schmiermittels, das eine größere Menge eines Öls mit Schmierviskosität enthält, wobei man dem Öl als Additiv
    (A) ein Metallsalz, ausgewählt aus der Gruppe bestehend aus Sulfonaten, Phenaten, Carboxylaten und deren Gemischen, und
    (B) eine effektive Menge einer aliphatischen Carbonsäure oder deren Anhydrid zugibt, wobei der aliphatische Rest mindestens 20 Kohlenstoffatome enthält, und wobei die relativen Gewichtsmengen von (A) : (B) im Bereich von 5:1 bis 1:5 liegen.
  23. Verfahren nach Anspruch 22, wobei
    (A) ein Alkali- oder Erdalkalimetallphenat ist,
    (B) eine aliphatisch-substituierte Bernsteinsäure oder deren Anhydrid ist, wobei der aliphatische Rest 30 bis 400 Kohlenstoffatome enthält, und zusätzlich
    (C) ein Metallsalz von (C) (I) mindestens einer organischen Phosphorsäure oder deren Gemisch von (C) (I) mindestens einer Phosphorsäure und (C) (II) mindestens einer Monocarbonsäure oder Polycarbonsäure mit 2 bis 40 Kohlenstoffatomen, wobei die relativen Gewichtsmengen von (A) : (B) im Bereich von 5:1 bis 1:5 und von (A) : (C) von 1:40 bis 2:1 liegen.
  24. Verfahren nach Anspruch 22 oder 23, wobei (A) ein überbasisches Metallsalz ist.
  25. Verfahren nach einem der Ansprüche 22 bis 24, wobei das Metallsalz (A) ein Alkalimetall-, Erdalkalimetall-, Kupfer- oder Zinksalz ist.
  26. Verfahren nach Anspruch 22 oder 23, wobei (A) ein Calciumphenat ist.
  27. Verfahren nach Anspruch 26, wobei (A) ein geschwefeltes Calciumphenat ist.
  28. Verfahren nach Anspruch 22, wobei (B) eine Polyolefin-substituierte Bernsteinsäure oder deren Anhydrid, Estersäure oder Lactonsäure ist.
  29. Verfahren nach Anspruch 28, wobei der Polyolefin-Substituent eine Polyethylengruppe, eine Polypropylengruppe, eine Polybutylengruppe oder deren Gemisch ist.
  30. Verfahren nach Anspruch 24, wobei (A) ein überbasisches Metallsalicylat ist.
  31. Verfahren nach einem der Ansprüche 22 bis 30, weiter umfassend ein Phosphit, ausgewählt aus der Gruppe bestehend aus Dialkylhydrogenphosphiten, Trialkylphosphiten und Triarylphosphiten.
  32. Verfahren nach einem der Ansprüche 23 bis 31, wobei die organische Phosphorsäure (C) (I) mindestens eine Säure der allgemeinen Formel I
    Figure 00820001
    ist, in der die Reste R1 und R2 gleich oder verschieden sind und jeder Rest R1 und R2 ein Wasserstoffatom oder ein Rest auf Kohlenwasserstoffbasis ist, mit der Maßgabe, daß mindestens einer der Reste R1 und R2 ein Rest auf Kohlenwasserstoffbasis ist, und jeder Rest X unabhängig ein Schwefel- oder Sauerstoffatom ist, und die Carbonsäure (C) (II) eine aliphatische oder alicyclische Carbonsäure mit 2 bis 40 Kohlenstoffatomen ist.
  33. Verfahren nach Anspruch 32, wobei die Phosphorsäure (C) (I) mindestens eine Dithiophosphorsäure der allgemeinen Formel
    Figure 00820002
    ist, in der jeder der Reste R1 und R2 gleich oder verschieden ist und jeder Rest R1 und R2 unabhängig ein Alkylrest mit 3 bis 50 Kohlenstoffatomen ist, und die Carbonsäure
    (C)(II) mindestens eine Carbonsäure der allgemeinen Formel R3COOH ist, in der R3 ein aliphatischer oder alicyclischer Rest auf Kohlenwasserstoffbasis mit 2 bis 40 Kohlenstoffatomen ist.
  34. Verfahren nach einem der Ansprüche 23 bis 33, wobei das Verhältnis der Äquivalente von (C) (I) zu (C) (II) 0,5:1 bis 500:1 beträgt.
  35. Verfahren nach Anspruch 23, wobei das Metallsalz von (C) mindestens eines der Gruppe I-Metalle, Gruppe II-Metalle, Aluminium, Zinn, Kobalt, Molybdän, Blei, Mangan und Nickel ist.
  36. Verfahren nach Anspruch 35, wobei das Metallsalz von (C) ein Zinksalz ist.
  37. Verfahren nach Anspruch 23, wobei das Metallsalz von unter Reaktionsbedingungen mit mindestens einem Phosphit der allgemeinen Formel (R4O)3P zusammengebracht wird, wobei jeder Rest R4 unabhängig ein Wasserstoffatom oder ein Rest auf Kohlenwasserstoffbasis ist.
  38. Verfahren nach Anspruch 23, wobei dem Öl zusätzlich (D) mindestens ein basisches Alkali- oder Erdalkalimetallsalz einer organischen Sulfonsäure zugesetzt wird.
  39. Verfahren nach einem der Ansprüche 22 bis 38, wobei dem Öl zusätzlich mindestens ein Mitglied, ausgewählt aus der Gruppe bestehend aus einer phenolischen antioxidierenden Verbindung, einem aschefreien Dispersant und einem Demulgator zugesetzt wird.
  40. Verfahren nach Anspruch 22 oder 23, wobei (A) in einer Menge von 0,01 bis 5 Gew.-% vorliegt.
  41. Verfahren nach einem der Ansprüche 1 bis 19, wobei dem Öl zusätzlich (E) eine stabilisierende Menge eines Triazols in einer Menge von weniger als 5 Gew.-% zugesetzt wird.
  42. Verfahren zur Verbesserung der Feuchtfiltrierbarkeit einer funktionellen Flüssigkeit mit einer größeren Menge eines Öls mit Schmierviskosität, umfassend das Zusetzen zum Öl als Additiv
    (A) ein Gruppe I- oder Gruppe II-Metallsalz, ausgewählt aus der Gruppe bestehend aus Sulfonaten, Phenaten, Carboxylaten und deren Gemischen nach einem der Ansprüche 22 bis 27 und
    (B) eine wirksame Menge einer aliphatischen Carbonsäure oder deren Anhydrid, wobei der aliphatische Rest mindestens 20 Kohlenstoffatome enthält, nach einem der Ansprüche 22, 23, 28 und 29, wobei die relativen Gewichtsmengen von (A) : (B) im Bereich von 5:1 bis 1:5 liegen.
EP92915925A 1991-07-31 1992-07-15 Verwendung einer Additivzusammensetzung zur Verbesserung der Filtrierbarkeit von mit Wasser kontaminierten Schmiermittelzusammensetzungen Revoked EP0551466B1 (de)

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US73901791A 1991-07-31 1991-07-31
US739017 1991-07-31
PCT/US1992/005928 WO1993003121A1 (en) 1991-07-31 1992-07-15 Improved lubricating compositions and additives useful therein

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US5380448A (en) * 1994-02-07 1995-01-10 Ethyl Petrolium Additives, Inc. Process for metal salts of hydrocarbyl dithiophosphoric acid
GB9416838D0 (en) 1994-08-19 1994-10-12 Bp Chemicals Additives Overbased metal salts, their preparation and use
US5726133A (en) * 1996-02-27 1998-03-10 Exxon Research And Engineering Company Low ash natural gas engine oil and additive system
FR2762006B1 (fr) * 1997-04-11 2003-09-12 Chevron Res & Tech Utilisation de surfactants de haut poids moleculaire comme agents ameliorant la filtrabilite dans des lubrifiants hydrauliques
EP1078977B1 (de) * 1999-07-30 2010-01-27 Afton Chemical Limited Schmiermittelzusammensetzungen
US7435709B2 (en) * 2005-09-01 2008-10-14 Chevron Oronite Company Llc Linear alkylphenol derived detergent substantially free of endocrine disruptive chemicals
CN101479366A (zh) 2006-04-24 2009-07-08 卢布里佐尔公司 星形聚合物润滑组合物
US9771540B2 (en) 2009-01-20 2017-09-26 Exxonmobil Research And Engineering Company Hydraulic oil compositions with improved hydraulic motor efficiency
JP2012515833A (ja) 2009-01-20 2012-07-12 ザ ルブリゾル コーポレイション 改善された摩耗性能を有する流体組成物
CN103038323B (zh) 2010-06-02 2015-09-16 路博润公司 含胺官能化添加剂的润滑组合物

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MX162168A (es) * 1981-09-14 1991-04-04 Lubrizol Corp Composicion lubricante mejorada para reducir el consumo de combustible
US4502970A (en) * 1982-06-08 1985-03-05 Exxon Research & Engineering Co. Lubricating oil composition
US4466894A (en) * 1983-04-20 1984-08-21 The Lubrizol Corporation Phosphorus-containing metal salts/sulfurized phenate compositions/aromatic substituted triazoles, concentrates, and functional fluids containing same
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CA2088768A1 (en) 1993-02-01
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JPH06502682A (ja) 1994-03-24
AU658218B2 (en) 1995-04-06
MX9204467A (es) 1994-06-30
AU2339692A (en) 1993-03-02
ES2119816T3 (es) 1998-10-16

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