US3042613A - Preparation of lubricant additive and lubricant composition containing same - Google Patents

Preparation of lubricant additive and lubricant composition containing same Download PDF

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US3042613A
US3042613A US775118A US77511858A US3042613A US 3042613 A US3042613 A US 3042613A US 775118 A US775118 A US 775118A US 77511858 A US77511858 A US 77511858A US 3042613 A US3042613 A US 3042613A
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hydrocarbon
alkaline earth
product
reaction product
molecular weight
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Norman E Lemmon
Albert R Sabol
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Standard Oil Co
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Standard Oil Co
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Priority to BE584775D priority Critical patent/BE584775A/xx
Priority to NL245441D priority patent/NL245441A/xx
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Priority to US775118A priority patent/US3042613A/en
Priority to GB38573/59A priority patent/GB937933A/en
Priority to FR810344A priority patent/FR1241398A/fr
Priority to DEST15814A priority patent/DE1173256B/de
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F9/00Compounds containing elements of Groups 5 or 15 of the Periodic Table
    • C07F9/02Phosphorus compounds
    • C07F9/04Reaction products of phosphorus sulfur compounds with hydrocarbons
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M129/00Lubricating compositions characterised by the additive being an organic non-macromolecular compound containing oxygen
    • C10M129/02Lubricating compositions characterised by the additive being an organic non-macromolecular compound containing oxygen having a carbon chain of less than 30 atoms
    • C10M129/26Carboxylic acids; Salts thereof
    • C10M129/48Carboxylic acids; Salts thereof having carboxyl groups bound to a carbon atom of a six-membered aromatic ring
    • C10M129/52Carboxylic acids; Salts thereof having carboxyl groups bound to a carbon atom of a six-membered aromatic ring polycarboxylic
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M159/00Lubricating compositions characterised by the additive being of unknown or incompletely defined constitution
    • C10M159/12Reaction products
    • C10M159/123Reaction products obtained by phosphorus or phosphorus-containing compounds, e.g. P x S x with organic compounds
    • C10M159/126Reaction products obtained by phosphorus or phosphorus-containing compounds, e.g. P x S x with organic compounds with hydrocarbon polymers
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M163/00Lubricating compositions characterised by the additive being a mixture of a compound of unknown or incompletely defined constitution and a non-macromolecular compound, each of these compounds being essential
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2201/00Inorganic compounds or elements as ingredients in lubricant compositions
    • C10M2201/02Water
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2205/00Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions
    • C10M2205/02Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions containing acyclic monomers
    • C10M2205/026Butene
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2205/00Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions
    • C10M2205/22Alkylation reaction products with aromatic type compounds, e.g. Friedel-crafts
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/10Carboxylix acids; Neutral salts thereof
    • C10M2207/12Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms
    • C10M2207/121Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms having hydrocarbon chains of seven or less carbon atoms
    • C10M2207/123Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms having hydrocarbon chains of seven or less carbon atoms polycarboxylic
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/10Carboxylix acids; Neutral salts thereof
    • C10M2207/12Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms
    • C10M2207/125Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms having hydrocarbon chains of eight up to twenty-nine carbon atoms, i.e. fatty acids
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/10Carboxylix acids; Neutral salts thereof
    • C10M2207/12Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms
    • C10M2207/129Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms having hydrocarbon chains of thirty or more carbon atoms
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/10Carboxylix acids; Neutral salts thereof
    • C10M2207/14Carboxylix acids; Neutral salts thereof having carboxyl groups bound to carbon atoms of six-membered aromatic rings
    • C10M2207/142Carboxylix acids; Neutral salts thereof having carboxyl groups bound to carbon atoms of six-membered aromatic rings polycarboxylic
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/10Carboxylix acids; Neutral salts thereof
    • C10M2207/22Acids obtained from polymerised unsaturated acids
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2209/00Organic macromolecular compounds containing oxygen as ingredients in lubricant compositions
    • C10M2209/02Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • C10M2209/08Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing monomers having an unsaturated radical bound to a carboxyl radical, e.g. acrylate type
    • C10M2209/082Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing monomers having an unsaturated radical bound to a carboxyl radical, e.g. acrylate type monocarboxylic
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2209/00Organic macromolecular compounds containing oxygen as ingredients in lubricant compositions
    • C10M2209/02Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • C10M2209/08Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing monomers having an unsaturated radical bound to a carboxyl radical, e.g. acrylate type
    • C10M2209/084Acrylate; Methacrylate
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2223/00Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions
    • C10M2223/02Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions having no phosphorus-to-carbon bonds
    • C10M2223/04Phosphate esters
    • C10M2223/045Metal containing thio derivatives
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2223/00Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions
    • C10M2223/12Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions obtained by phosphorisation of organic compounds, e.g. with PxSy, PxSyHal or PxOy
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2225/00Organic macromolecular compounds containing phosphorus as ingredients in lubricant compositions
    • C10M2225/04Organic macromolecular compounds containing phosphorus as ingredients in lubricant compositions obtained by phosphorisation of macromolecualr compounds not containing phosphorus in the monomers
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2225/00Organic macromolecular compounds containing phosphorus as ingredients in lubricant compositions
    • C10M2225/04Organic macromolecular compounds containing phosphorus as ingredients in lubricant compositions obtained by phosphorisation of macromolecualr compounds not containing phosphorus in the monomers
    • C10M2225/041Hydrocarbon polymers
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2010/00Metal present as such or in compounds
    • C10N2010/04Groups 2 or 12
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2070/00Specific manufacturing methods for lubricant compositions
    • C10N2070/02Concentrating of additives

Definitions

  • This invention relates to improvements in the preparation of lubricant additives, and more particularly pertains to the preparation of neutralized phosphorus sulfide-hydrocarbon reaction products having a high alkaline earth metal to phosphorus ratio which is compatible with fatty acid polymers with substantially no viscosity increase.
  • valve-lifters for smoother and more eflicient engine operation.
  • the lifter rise on the cam shaft converting the rotary motion of the cam into a reciprocating motion, which in turn opens and closes the valves.
  • the bottom of the valve-lifter is known as the cam follower.
  • the hydraulic part of the valve-lifter functions by means of a plunger on the inside of the valve lifter barrel, together with a ball-check and a spring.
  • larger valves, higher valve spring pressures and camshafts which produce more rapid valve opening and closing are employed.
  • camshaft and valve-lifter combinations of different metals create different requirements on the lubricant in that certain types of anti-wear additives may be effective with some cam-lifter metal combinations but ineffective with other metal combinations.
  • certain types of anti-wear additives may be effective with some cam-lifter metal combinations but ineffective with other metal combinations.
  • extremely small amounts of deposits such as varnish and/ or rusting may cause sticking of the valve-lifter. for good engine operation to provide a lubricant which will, in addition to inhibit Wear and/ or pitting also inhibit the formation of varnish and/or rusting in the valve-lifter.
  • Such cam follower pitting and/ or wear, and the sticking of hydraulic valve lifters can be effectively inhibited by using lubricating oils containing small amounts of an alkaline earth neutralized reaction product of a phosphorus sulfide and a hydrocarbon in combination with a fatty acid polymer such as polymeric linoleic acids, e.-g. linoleic and dimers, and mixtures of polymeric fatty acids; such as is described in US. 2,833,713 issued to N. E. Lemmon et al. May 6, 1958. While the additive combination of the Lemmon et al.
  • a fluid, free flowing lubricating oil additive concentrate consisting essentially of a neutralized alkaline earth-containing reaction product of a phosphorus sulfide and a hydrocarbon and a polymeric high molecular weight carboxylic acid, hereinafter defined, in the ratio of from about 20:1 to about 20:2 respectively is prepared by the process comprising reacting a phosphorus sulfide with a hydrocarbon, reacting the resultant reaction product with a sufiicient amount of a basic alkaline earth compound to give an alkaline earth-containing reaction product having an excess alkalinity of at least about 2 milligrams NaOH per gram of product, and usually from about 2 to about 20 milligrams NaOH per gram of product, treating the alkaline reaction product with CO at a temperature of from about F.
  • the alkalinity is determined by mixing five grams of the sample with ccs. of 95% ethyl alcohol and 200 ccs. naphtha and titrating with sodium hydroxide using phenolphthalein indicator. While not essential, it is preferred to conduct the C0 treatment in the presence of from about 0.1% to about 5% of water based on the alkaline additive.
  • the hydrocarbon is reacted with a phosphorus sulfide, such as P 8 P 8 P 8 or other phosphorus sulfides, and preferably phosphorus pentasulfide, P 5 as described in detail in US. 2,316,- 808, 2,316,082, and 2,316,088, each issued to Loane et al. on April 6, 1943.
  • a phosphorus sulfide such as P 8 P 8 P 8 or other phosphorus sulfides, and preferably phosphorus pentasulfide, P 5 as described in detail in US. 2,316,- 808, 2,316,082, and 2,316,088, each issued to Loane et al. on April 6, 1943.
  • the hydrocarbon constituent of this reaction is suitably a normally non-gaseous hydrocarbon having a molecular weight of at least about 150. While the by drocarbon constituent of this reaction can be any of the type hereinafter described, it is preferably a mono-olefin hydrocarbon polymer resulting from the polymerization of low molecular weight mono-olefinic hydrocarbons or isomono-olefinic hydrocarbons, such as propylene, butylcues, and amylenes or the copolymers obtained by the polymerization of hydrocarbon mixtures containing isomono-olefins and mono-olefins or mixtures of olefins in the presence of a catalyst, such as sulfuric acid, phosphoric acid, boron fluoride, aluminum chloride or other similar halide catalysts of the Friedel-Crafts type.
  • a catalyst such as sulfuric acid, phosphoric acid, boron fluoride, aluminum chloride or other similar halide catalyst
  • the polymers employed are preferably mono-olefin polymers or mixtures of mono-olefin polymers and isomono-olefin polymers having molecular weights ranging from about 150 to about 50,000 or more, and preferably from about 300 to about 10,000. Such polymers can be et al. April 6, 1943.
  • Essentially paraflinic hydrocarbons such as bright stock residuums, lubricating oil distillates, petrolatums, or paraffin waxes, may be used.
  • condensation products of any of the foregoing hydrocarbons usually through first halogenating the hydrocarbons, with aromatic hydrocarbons in the presence of anhydrous inorganic halides, such as aluminum chloride, zinc chloride, boron fluoride, and the like.
  • olefins suitable for the preparation of the herein described phosphorus sulfide reaction products are olefins having at least 20 carbon atoms in the molecule of which from about 13 carbon atoms to about 18 carbon atoms, and preferably at least 15 carbon atoms are in a long chain.
  • Such olefins can be obtained by the dehydrogenation of paraffins, such as by the cracking of paraflin waxes or by the dehalogenation of alkyl halides, preferably long chain alkyl halides, particularly halogenated parafiin waxes.
  • reaction products of a phosphorus sulfide with an aromatic hydrocarbon such as for example, benzene, naphthalene, toluene, xylene, diphenyl and the like or with an alkylated aromatic hydrocarbon, such as for example, benzene having an alkyl substituent having at least four carbon atoms, and preferably at least eight carbon atoms, such as long chain paraffin wax.
  • aromatic hydrocarbon such as for example, benzene, naphthalene, toluene, xylene, diphenyl and the like
  • an alkylated aromatic hydrocarbon such as for example, benzene having an alkyl substituent having at least four carbon atoms, and preferably at least eight carbon atoms, such as long chain paraffin wax.
  • the phosphorus sulfide-hydrocarbon reaction product is prepared by reacting the phosphorus sulfide, e.g. P 8 with the hydrocarbon at a temperature of from about 150 F. to about 600 F., preferably from about 300 F. to about 500 F., using from 1% to about 50%, preferably from about 5% to about 25% of phosphorus sulfide; the reaction is carried out in from about one to about ten hours. It is preferable to use an amount of the phosphorus sulfide that will completely react with the hydrocarbon so that no further purification is necessary; however, an excess of the phosphorus sulfide can be used, and the unreacted material separated by filtration.
  • the reaction if desired, can be carried out in the presence of a sulfurizing agent such as sulfur or a halide of sulfur as described in U.S. 2,316,087, issued to J. W. Gaynor, It is advantageous to maintain a non-oxidizing atmosphere, for example an atmosphere of nitrogen, in the reaction vessel.
  • a sulfurizing agent such as sulfur or a halide of sulfur as described in U.S. 2,316,087, issued to J. W. Gaynor
  • a non-oxidizing atmosphere for example an atmosphere of nitrogen
  • the reaction product obtained is then hydrolyzed at a temperature of from about 200 F. to about 500 F., preferably at a temperature of about 300 -F.-400 F. by suitable means, such as for example, by introducing steam through the reaction mass.
  • the hydrolyzed product, containing inorganic phosphorus acids formed during the hydrolysis, can be used as such in the subsequent neutralization stage; or it can be substantially freed of the inorganic phosphorus acids by contacting with an adsorbent material such as Attapulgus clay, fullers earth and the like at a temperature of 100 F.500 -F. as fully described and claimed in U.S. 2,688,612, issued to R. Watson September 7, 1954, or by extraction with phenol or an alkanol of 1 to 5 carbon atoms in admixture with water as described and claimed in Lemmon et al. U.S. Patent No. 2,843,579, issued July 15, 1958.
  • the hydrolyzed reaction product is reacted with a basic alkaline earth compound, such as an oxide or hydroxide of barium, calcium, strontium or magnesium to obtain in an oil, preferably an oil similar to the lubricating oil in which the additive is to be used.
  • a basic alkaline earth compound such as an oxide or hydroxide of barium, calcium, strontium or magnesium
  • the total amount of the basic alkaline earth compound present in the slurry should be from about 3 to about 15 parts per part of the phosphorus present in the phosphorus sulfide-hydrocarbon reaction product reactant.
  • Reaction with the basic alkaline earth compound is carried out at a temperature of from about 100 F. to about 500 F., preferably from about 120 F., to about 350. F.
  • the reaction is preflysts.
  • the hydrolyzed phosphorus sulfide-hydrocarbon reaction product after reaction with the basic alkaline earth compound normally contains an alkalinity of from about 2 to about 20 milligrams NaOH per gram of product.
  • the product so obtained can be used in the formulation of lubricating oil compositions in combination with many other additives. However, when the above hydrolyzed product is to be used in lubricating oil compositions in combination with a polymeric high molecular weight fatty acid undersirable gelling and/or thickening of the composition is encountered.
  • the alkaline earth containing hydrolyzed phosphorus sulfide-hydrocarbon reaction above described prior to being incorporated in the lubricant composition in combination with the polymeric fatty acid, is treated with CO at a temperature of from about F. to about 300 F. for a period of time sufficient to reduce the alkalinity of the alkaline earth-containing hydrolyzed phosphorus sulfide-hydrocarbon reaction product to a value of about zero milligrams NaOH per gram of product, by the above described procedure for measuring free alkalinity.
  • the polymeric carboxylic acid used is a polymeric high molecular weight unsaturated carboxylic acid having a molecular weight of at least about 300 and preferably 9 they may have a lesser or greater number of carbon atoms.
  • the neutral fatty acids are those such as linoleic, linolenic, ricinoleic (which upon heating forms linoleic acid), linoleaidic, elaidolinolenic, eleostearic, arachidonic, eicosatrienaic, cetoleic, docosatrienoic and the like.
  • the free fatty acids can be polymerized either thermally or with the assistance of cata-
  • a method of thermally polymerizing free fatty acids (see U.S. 2,482,761) consists of hydrolyzing a fat or an oil, adding a small portion of water, and heating in a pressure vessel until substantially all of the diand tri-unsaturated fatty acids present polymerize. The resultant product is then heated at a reduced pressure to distil off vaporizable constituents, leaving behind the polymerized unsaturated fatty acids.
  • the polymerization reaction is carried out at a temperature of about 300 to 360 C. for about three to eight hours at a pressure varying between 75 and 500 p.s.i.g.
  • the polymerization product may consist of monomers, dimers, trimers, and higher polymers of the unsaturated fatty acids.
  • the various fats or oils which may be hydrolyzed to produce the free fatty acids used in the above thermal polymerization are those such as sardine oil, linseed oil, soybean oil, castor oil, peanut oil, palm oil, olive oil, cottonseed oil, sunflower seed oil, and the like.
  • Another method of preparing the polymerized fatty acids consists of subjecting fats and oils such as have been listed supra (without previous hydrolysis) to a thermal or catalytic polymerization to cause polymerization of the esters of the unsaturated carboxylic acids to the dimers, trimers, and higher polymerization products thereof, followed by hydrolysis to yield the corresponding polymers of the acids.
  • a large source of the polymerized unsaturated fatty acids are those residual acids obtained by methanolysis (see US. 2,450,940) of the semi-drying or drying type oils such as castor oil, soybean oil and others listed supra, polymerizing the methyl esters, removing unpolymerized compounds, saponifying the residual esters and freeing polymerized acids therefrom.
  • the products of catalytic polymerization of semidrying oils such as the BF;, polymerization products of soybean oil, cottonseed oil, or the like, also produce polymers suitable for use in the invention.
  • a useful, commercially available dimeric carboxylic acid is commercially available from Emery Industries, Inc. under the tradename Emery 955-Dimer Acid. Since the commercial product is produced by dimerization of linoleic acid, it is usually referred to as dilinoleic acid.
  • the mixture of high molecular weight unsaturated carboxylic acids comprises monomers, dimers, trimers and higher polymers in the ratio of from about 45% to about 55 of a monomers and dimers fraction having a molecular weight in the range of from about 300 to 600, and from about 45% to about 55% of a trimers and higher polymer fraction having a molecular weight in excess of 600.
  • the carboxylic acid'polymers result in part from a thermal polymerization of fatty acid type constituents of the castor oil, and in part from other reactions, such as the inter-molecular esterification, of such acid to form high molecular weight products.
  • the acid mixture which is mainly a mixture of polymeric long chain polybasic carboxylic acids, is further charactenzed by the following specifications:
  • E. TREATMENT OF PRODUCT A 3-1 Product A, 50% diluted with an SAE-SW mineral oil base, was stirred with 1.5 mols of 13210 per mol of phosphorus at about 75 F. to obtain thorough mixing, and to the mixture were added 0.8 mol water per mol of BaO and 7 mols of methanol per mol of BaO, and the entire mixture heated under reflux conditions for 3 hours at 158-l60 F. The refluxed mixture was then heated to about 400 F. to remove water and methanol and then clay filtered.
  • the recovered filtrate a barium containing reaction product of the P S -polybutene, had an alkalinity of about 14 milligrams NaOH per gram of product, a barium content of 7.9% and a phosphorus content of 1.3%.
  • reaction products of the phosphorus sulfide and the polybutene, or other hydrocarbons containing other alkaline earth metals can be obtained. While it is preferable to conduct the reaction with the basic alkaline earth compound, e.g. BaO, in the presence of an alkanol, e.g. methanol, and water, as shown in the above examples, this is not essential and the reaction can be carried out in the absence of the alkanol and water.
  • the basic alkaline earth compound e.g. BaO
  • an alkanol e.g. methanol
  • the product D-SO, supra which is essentially a mixture of high molecular weight unsaturated fatty acids comprising monomers, dimers, trimers, and higher polymers in the ratio of from about 45% to about 55% of a monomers and dimers fraction having a molecular weight in the range of from about 300 to about 600, and from about 55% to about 45% of a trimers and higher polymers fraction having a molecular weight in excess of about 600, and an essentially dimerized linoleic acid referred to as Dimer Acid and comprising 85% of a dilineoleic acid, about 12% of trilinoleic acid and about 3% linoleic acid.
  • SI Merely flows at RT. 1 Milligrams NaOH per gram product.
  • alkaline earth-containing phosphorus sulfide hydrocarbon reaction products treated with carbon dioxide in accordance with the present invention when admixed with polymeric high molecular weight fatty acids are fluid at room temperatures, whereas in the absence of such carbon dioxide treatment the mixtures are solid at room temperatures.
  • the combination of the alkaline earth-containing phosphorus sulfide-hydrocarbon reaction product prepared in accordance with the present invention, and the polymeric high molecular weight polybasic carboxylic acid, herein defined are useful additives for hydrocarbon lubricating oil compositions, for example, lubricating oils for internal combustion engines.
  • lubricating oil composition for internal combustion engines from about 1 to about 20% of the alkaline earth-containing phosphorus sulfide-hydrocarbon reaction product and from about 0.1 to about 1.0% of the polymeric acid are used.
  • Such lubricants can contain small amounts of other additives usually employed in such compositions, such as for example metal salts of dialkyldithiophosphates, e.g.
  • V.I. improvers e.g. high molecular Weight polybutenes, methacrylate polymers, etc.
  • pour point depressors e.g. condensation products of chlorinated paraflin wax and naphthalene, anti-Wear agents, etc.
  • Hydrocarbon oil compositions containing the combination of the carbon dioxide-treated alkaline earth-containing phosphorus sulfide reaction product, the polymeric high molecular weight polybasic carboxylic acid and a small amount of water exhibit improved rust preventive properties.
  • the amount of water in the finished composition is preferably in the range of from about 0.1% to 1.0%; the water may be present in the carbon dioxide treated product when such treatment is conducted in the presence of water, or the water can be added after the carbon dioxide treatment.
  • the data in Table II demonstrate the improvement in rust prevention properties 0b- In the above accelerated rust test, a 5 x 7 cm. steel panel is cleaned by sand blasting and the cleaned panel dipped in the above blend of oil, naphtha and additive for one minute. The dipped panel is allowed to drain at room temperature for 30 minutes and then immersed in distilled water at F. The panel is considered to fail when about 0.1% of the total area develops rust spots or stains.
  • additive combination for hydrocarbon lubricating oils, which additive combination consists essentially of a polymeric high molecular Weight unsaturated polybasic carboxylic acid and an alkaline earth-containing phosphorus sulfide-hydrocarbon reaction product obtained by reacting a normally nongaseous hydrocarbon with a phosphorus sulfide at a temperature of from about F. to about 600 F., hydrolyzing the resultant phosphorus sulfide-hydrocarbon reaction product at a temperature of from about 200 F.
  • polymeric high molecular Weight unsaturated carboxylic acid is a mixture comprising essentially monomers, dimers, trimers and higher fatty acid polymers in the ratio of from about 45% to about 55% of a monomer and dimer fraction having a molecular weight in the range of from about 300 to about 600, and from about 55% to about 45 of a trimer and higher polymer fraction having a molecular weight in excess of about 600.
  • non-gaseous hydrocarbon is an olefin hydrocarbon having a molecular weight of at least about 150.
  • a normally fluid lubricant composition comprising a major proportion of a hydrocarbon lubricating oil, from about 0.05% to about 1.0% of a polymeric high molecular weight unsaturated polybasic carboxylic acid and from about 1% to about 20% of an alkaline earth-containing phosphorus sulfide-hydrocarbon reaction product obtained by the method of claim 1.
  • a normally fluid lubricant composition having rust preventive properties comprising a major proportion of a hydrocarbon lubricating oil from about 0.05% to about 1.0% of a polymeric high molecular weight unsaturated polybasic carboxylic acid from about 0.1% to about 1.0% water and from about 1% to about 20% of an alkaline earth-containing phosphorus sulfide-hydrocarbon reac tion product obtained by the method of claim 1.
  • additive combination for hydrocarbon lubricating oils, which additive combination consists essentially of a polymeric high molecular weight unsaturated polybasic carboxylic acid and bariumcontaining phosphorus sulfide-polybutene reaction product obtained by reacting a polybutene with P 8 at a temperature of from about F. to about 600 F., hydrolyzing the resultant P S -polybutene reaction product at a temperature of from about 200 F.
  • a normally fluid lubricant composition comprising a major proportion of a hydrocarbon lubricating oil, from about 0.05 to about 1.0% of a polymeric high molecular weight unsaturated polybasic carboxylic acid and from about 1% to about 20% of an alkaline earthcontaining phosphorus sulfide-hydrocarbon reaction product obtained by the method of claim 10.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Biochemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • Molecular Biology (AREA)
  • Lubricants (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
US775118A 1958-11-20 1958-11-20 Preparation of lubricant additive and lubricant composition containing same Expired - Lifetime US3042613A (en)

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BE584775D BE584775A (xx) 1958-11-20
NL245441D NL245441A (xx) 1958-11-20
US775118A US3042613A (en) 1958-11-20 1958-11-20 Preparation of lubricant additive and lubricant composition containing same
GB38573/59A GB937933A (en) 1958-11-20 1959-11-13 Lubricant additives and lubricant compositions containing them
FR810344A FR1241398A (fr) 1958-11-20 1959-11-17 Procédé de préparation d'un additif pour lubrifiants et compositions lubrifiantes contenant cet additif
DEST15814A DE1173256B (de) 1958-11-20 1959-11-19 Verfahren zur Herstellung von Derivaten metallhaltiger hydrolysierter phosphor-geschwefelter Kohlenwasserstoffe

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4244828A (en) * 1978-11-13 1981-01-13 Texaco Inc. Lubricating oil composition
US5449470A (en) * 1991-04-19 1995-09-12 The Lubrizol Corporation Overbased alkali salts and methods for making same
US5486300A (en) * 1991-04-19 1996-01-23 The Lubrizol Corporation Lubricating compositions
US5490945A (en) * 1991-04-19 1996-02-13 The Lubrizol Corporation Lubricating compositions and concentrates
US5562864A (en) * 1991-04-19 1996-10-08 The Lubrizol Corporation Lubricating compositions and concentrates
US5614480A (en) * 1991-04-19 1997-03-25 The Lubrizol Corporation Lubricating compositions and concentrates

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2048934B (en) * 1979-05-08 1983-08-03 Nippon Kokan Kk Lubricating oil compositions and methods of manufacturing and supplying them

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US2762774A (en) * 1953-04-21 1956-09-11 Exxon Research Engineering Co Pour depressant-detergent additive combination
US2767209A (en) * 1952-11-03 1956-10-16 Lubrizol Corp Complexes of dissimilar metals and methods of making same
GB785196A (en) * 1955-04-22 1957-10-23 Bataafsche Petroleum Process for the preparation of oil-soluble basic monovalent metal salts of organic acids
US2833713A (en) * 1955-04-18 1958-05-06 Standard Oil Co Corrosion inhibited motor oils
US2841552A (en) * 1955-06-30 1958-07-01 Standard Oil Co Lubricating oil composition
US2906709A (en) * 1956-05-31 1959-09-29 Standard Oil Co Lubricant additive of high metal content

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US2316082A (en) * 1941-03-24 1943-04-06 Standard Oil Co Lubricant

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2767209A (en) * 1952-11-03 1956-10-16 Lubrizol Corp Complexes of dissimilar metals and methods of making same
US2762774A (en) * 1953-04-21 1956-09-11 Exxon Research Engineering Co Pour depressant-detergent additive combination
US2833713A (en) * 1955-04-18 1958-05-06 Standard Oil Co Corrosion inhibited motor oils
GB785196A (en) * 1955-04-22 1957-10-23 Bataafsche Petroleum Process for the preparation of oil-soluble basic monovalent metal salts of organic acids
US2841552A (en) * 1955-06-30 1958-07-01 Standard Oil Co Lubricating oil composition
US2906709A (en) * 1956-05-31 1959-09-29 Standard Oil Co Lubricant additive of high metal content

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4244828A (en) * 1978-11-13 1981-01-13 Texaco Inc. Lubricating oil composition
US5449470A (en) * 1991-04-19 1995-09-12 The Lubrizol Corporation Overbased alkali salts and methods for making same
US5486300A (en) * 1991-04-19 1996-01-23 The Lubrizol Corporation Lubricating compositions
US5490945A (en) * 1991-04-19 1996-02-13 The Lubrizol Corporation Lubricating compositions and concentrates
US5562864A (en) * 1991-04-19 1996-10-08 The Lubrizol Corporation Lubricating compositions and concentrates
US5614480A (en) * 1991-04-19 1997-03-25 The Lubrizol Corporation Lubricating compositions and concentrates

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GB937933A (en) 1963-09-25
FR1241398A (fr) 1960-09-16
NL245441A (xx)
BE584775A (xx)
DE1173256B (de) 1964-07-02

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