US3102096A - Lubricating oil containing zinc carboxylate-coordinated zinc dithiophosphates - Google Patents

Lubricating oil containing zinc carboxylate-coordinated zinc dithiophosphates Download PDF

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US3102096A
US3102096A US76998A US7699860A US3102096A US 3102096 A US3102096 A US 3102096A US 76998 A US76998 A US 76998A US 7699860 A US7699860 A US 7699860A US 3102096 A US3102096 A US 3102096A
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zinc
dithiophosphate
coordinated
salt
bis
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US76998A
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Edwin M Nygaard
Edward A Oberright
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ExxonMobil Oil Corp
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Socony Mobil Oil Co Inc
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Priority to US76998A priority patent/US3102096A/en
Priority to GB43360/61A priority patent/GB959115A/en
Priority to DE19611444892 priority patent/DE1444892B1/en
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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
    • C07F9/06Phosphorus compounds without P—C bonds
    • C07F9/16Esters of thiophosphoric acids or thiophosphorous acids
    • C07F9/165Esters of thiophosphoric acids
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F3/00Compounds containing elements of Groups 2 or 12 of the Periodic Table
    • C07F3/003Compounds containing elements of Groups 2 or 12 of the Periodic Table without C-Metal linkages
    • 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
    • C10M137/00Lubricating compositions characterised by the additive being an organic non-macromolecular compound containing phosphorus
    • C10M137/02Lubricating compositions characterised by the additive being an organic non-macromolecular compound containing phosphorus having no phosphorus-to-carbon bond
    • C10M137/04Phosphate esters
    • C10M137/10Thio 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
    • C10M2201/00Inorganic compounds or elements as ingredients in lubricant compositions
    • C10M2201/06Metal compounds
    • C10M2201/065Sulfides; Selenides; Tellurides
    • 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
    • C10M2203/00Organic non-macromolecular hydrocarbon compounds and hydrocarbon fractions as ingredients in lubricant compositions
    • C10M2203/10Petroleum or coal fractions, e.g. tars, solvents, bitumen
    • 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
    • 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
    • C10M2207/122Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms having hydrocarbon chains of seven or less carbon atoms 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
    • 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
    • C10M2207/141Carboxylix acids; Neutral salts thereof having carboxyl groups bound to carbon atoms of six-membered aromatic rings 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
    • 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
    • C10M2207/144Carboxylix acids; Neutral salts thereof having carboxyl groups bound to carbon atoms of six-membered aromatic rings containing hydroxy groups
    • 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
    • C10M2207/14Carboxylix acids; Neutral salts thereof having carboxyl groups bound to carbon atoms of six-membered aromatic rings
    • C10M2207/146Carboxylix acids; Neutral salts thereof having carboxyl groups bound to carbon atoms of six-membered aromatic rings having carboxyl groups bound to carbon atoms of six-membeered aromatic rings having a hydrocarbon substituent of thirty or more carbon atoms
    • 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
    • C10M2207/16Naphthenic 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
    • 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
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2010/00Metal present as such or in compounds
    • C10N2010/04Groups 2 or 12
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2030/00Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/12Inhibition of corrosion, e.g. anti-rust agents or anti-corrosives
    • CCHEMISTRY; METALLURGY
    • 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

  • the invention relates to improved lubricating oil compositions. More specifically, it relates to lubricating oil compositions which are substantially non-corrosive to silver.
  • zinc bis(alkyl)dithiophosphates other than those derived 7 from neo-type alcohols, are not made non-corrosive to silver by reaction thereof with zinc carboxylates.
  • the manner in which the zinc dithiophosphate and zinc .carboxylate salts are combined in the reaction -of the invention is not known with certainty, it is theorized, without wishing to limit the invention in any way, that they are joined by coordinate bonds similar to those existing in complexes of the Werner-type.
  • the product salts are referred to herein as zinc carboxylate-coordinated zinc dithiophosphate salts.
  • the zinc carboxylate-coordinated zinc dithiophosphate salts contemplated by the invention have not been known heretofore and they are, therefore, believed to be new compositions of matter. Accordingly, it is the primary object of the invention to provide a new class of zinc dithiophosphate salts which are non-corrosive to silver, viz., zinc carboxylate-coordinated zinc dithiophosphate salts. A further object is to provide lubricating oil compositions containing these new coordinated salts. Other and further objects of the invention will be apparent from the following detailed description.
  • the zinc carboxylate-coordinated zinc dithiophosphate salts are produced by l) forming a reaction mixture of '(A) one mol 3,162,096 Patented Aug. 27, 1963 proportion of Zll'lC dithiophosphate, -(B) at least one mol proportion of zinc carboxylate, (C) water and (D) a hydrocarbon solvent and (2) heating the mixture to a temperature sufficient to distill off the water, whereby a solvent solution of the zinc carboxylate-coordinated zinc dithiophosphate salt, containing approximately one mol proportion of each of the reactant salts, is produced. The product mixture is then filtered to remove any unreacted salt.
  • a light hydrocarbon solvent such as xylene, toluene or a petroleum naphtha
  • the water distilled off as an azeotropic mixture with the solvent.
  • a lubricating oil may be added to the solvent mixture and the remainder of the solvent distilled off (or the solvent can be removed before the oil is added) whereby a lubricating oil concentrate of the product salt, suitable for blending with the base lubricating oil, is obtained.
  • normal zinc bis(aryl)dithiophosphates to which the invention is applicable are those containing aryl radicals, such as phenyl, naphthyl or the like, which radicals may have one or more (up to 5) alkyl groups of from one up to about 20 carbon atoms substituted thereon
  • aryl radicals such as phenyl, naphthyl or the like
  • radicals may have one or more (up to 5) alkyl groups of from one up to about 20 carbon atoms substituted thereon
  • normal zinc salts such as the following, are contemplated by the invention:
  • the normal zinc salts of bis(alkyl)- dithiophosphoric acids which ane improved by the invention are those derived from aliphatic alcohols having 2 neo or hindered carbon atom adjacent to the carbon atorr bearing the hydroxyl group. These alcohols conform tc the structure where R is alkyl. These alcohols and consequently the alkyl groups derived therefrom may contain from 5 up to about 20 carbon atoms.
  • suitable zinc dithiophosphate salts of this type are the following:
  • the zinc carboxylates with which the Zinc dithiophos phate salts may be coordinated in accordance with the in vention may be either aliphatic or aromatic in nature
  • the aliphatic Zinc carboxylates may be of the straight chained, branch-chained or cyclic type and may contair from 1 to about 20 carbon atoms.
  • thes salts are zinc acetate, Zinc formate, zinc butyrate, zir1 decanoate, zinc stearate, zinc oleate, zinc linoleate and th like.
  • Zinc naphthenate salts derived from petroleun oil naphthenic acids, are also highly suitable.
  • the aro matic carboxylate salts include, for example, zinc ben zoate, zinc salicylate and such salts which also have one or more alkyl groups having from 1 to 20 carbon atom: each substituted on the aromatic ring thereof.
  • the mixture was dehydrated by refluxing for one and one-half hours. The temperature was then lowered to 130135 C. and 199.8 grams (0.9 mol) of phosphorus pentasulfide added, portionwise, over a period of one and one-half hours While maintaining the temperature at 130135 C. The mixture was then heated to reflux and refluxed for one hour (144l45 C.). The mixture was then cooled to approximately 90 C. and 150 cc. of distilled water added over a period of about one-half hour. The temperature was held at 8893 C. for two hours to form the normal zinc salt of bis('nonylphenyl)dithiophosphate. The mixture was then heated to reflux to azeotrope the water.
  • the product was then cooled to about 100 C. and filtered through Super-Cel (a diatomaceous earth filter aid).
  • the xylene was then removed at reduced pressure using a water-bath-as a source of heat.
  • the reaction mixture was then diluted with approximately 25%, by weight, of mineral oil (100 S.U.S. 100 F.), warmed on a waterbath and filtered through a bed of cuper-Cel.
  • the temperature was raised to reflux and the mixture refluxed for one hour (144147 C.).
  • the temperature was reduced to approximately 90 C. and 150 cc. of distilled water was added from the dropping funnel over a period of about 15 minutes.
  • the temperature was maintained at 9095 C. for two hours in order to form the normal zinc salt of bis(n0nylphenyl)- dithiophosphoric acid.
  • paraffinic mineral oil 100 S.U.S. 100 F.
  • xylene-free salt product containing about 25%, by weight, of oil.
  • the xylene was removed at reduced pressure using a waterbath as a source of heat.
  • the maximum azeotroping temperature was 116 C.
  • the product was then filtered through a bed of Super- Cel. The product was then removed at reduced pressure using a boiling water-bath as a source of heat.
  • the mixture was then refluxed to azeotrope the water.
  • the product was then filtered through Super- Cel.
  • the benzene was then removed at reduced pressure using a water-bath as a source of heat.
  • the mixture was stirred and refluxed at approximately 144 C. to remove all water from the system.
  • the temperature was reduced to approximately 130 C. and 34.3 grams (0.15 mol) of phosphorus pentasulfide was added over a period of 50 minutes at a reaction temperature of 130-135 C.
  • the temperature of the mixture was raised to reflux (Ml-142 C.) and refluxed for one hour.
  • the temperature was then reduced to approximately 90 C. and 88.0 grams (0.225 mol) of petroleum naphthenic acid was added, followed by 50 milliliters of distilled Water.
  • the mixture was stirred and heated for two hours at 9093 C.
  • the temperature was then raised to azeotrope the water (144 C.).
  • the mixture was then cooled and filtered through Super-Cal.
  • the filtrate was washed with 150 milliliters of fresh xylene.
  • the xylene was removed from the filtrate at reduced pressure using a water-bath as a source of heat.
  • the test method used was that developed by the Electro-Motive Division of General Motors Corporation, designated EMD Method No. LO. 201-47, for determining the corrosivity towards silver of a heavy duty lubricating oil.
  • the procedure consists in heating in an oil bath held at 325 F.i2 F., 300 milliliters of lubricating oil contained in a 600-milliliter beaker. The oil is stirred at 300 rpm.
  • a weighed section of a silver-plated wrist-pin bushing (approximate size 3" x 1" x A1"lead flashing removed from surface prior to test) is suspended in the oil so that it is immersed to approximately of its surface area.
  • the bushing section is removed from the oil, washed with carbon tetrachloride and dried.
  • the corrosion layer is then electrolytically removed after which the bushing is washed with water and alcohol and dried by wiping with a cloth and placing it in an oven held at F. for 10 minutes. After cooling in a desiccator, it is reweighed. If the weight loss is no greater than 5 milligrams, the oil is considered to have passed the test.
  • the lubricating oil used in the tests was a Mid-Continent solvent-refined, all paraflin distillate having an S.U.V. of 77 seconds at 210 F.
  • the percentage of additive used in the oil in each instance was adjusted to give the same percentage of zinc bound to sulfur (excludes the zinc bound to zinc carboxylate coordinating agent) as contained in 0.44% and 0.89%, by weight, respectively, of the normal zinc bis(4-methyl-2-pentyl)dithiophosphate additive (Example '5).
  • the test results are shown in Table I.
  • the coordinated salts contemplated by the invention contain approximately one mo of zinc carboxylate per mol of zinc dithiophosphate. 11 has been found that if less than approximately one moi of the zinc carboxylate is combined with the zinc dithiophosphate salt, the resulting coordinated salt will no? pass the silver corrosion test.
  • the amount of zinc carboxylate salt used in the reaction with the zinc dithiophos- 7 phate salt therefore, must be at least about one mol per mol of zinc dithiophosphate, the use of a moderate excess over this amount, say, from 10% to about 50%, being preferred in order to insure incorporation of the required one mol proportion thereof in the coordinated salt product.
  • the presence of water is essential to the coordination reaction, the minimum required amount being about 0.5 mol per mol of zinc dithiophosphate being reacted with the zinc carboxylate.
  • the reaction is greatly facilitated, however, by the use of much larger amounts, say, from 10 to about 50 mols of water per mol of zinc dithiophosphate being reacted.
  • the upper limit of the amount of water is not critical and the amount used is, therefore, governed largely by practical considerations.
  • the coordinated salt products of the invention may conveniently be prepared in the form of concentrated oil solutions thereof which solutions are readily blendable with base oils desired to be improved thereby.
  • concentration of the product salt in these solutions will depend, of course, on the amount of diluent oil used in the process. For commercial purposes this amount can be standardized to provide a specified level of concentration. Expressed on an oil-free basis, however, the amount of the coordinated salt to be utilized in lubricating oil will range from about 0.01% to about 10%, by Weight, the usual amount being from about 0.5% to about 5%.
  • the lubricating oil to which the salts of the invention are added may also contain other addition agents designed to improve the characteristics of the oil in various respects, such as detergents, pour point depressants, viscosity index improvers, extreme pressure agents, additional antioxidants, etc.
  • a zinc carboxylatecoordinated zinc dithiophosphate salt composed of approximately one mol proportion of zinc carboxylate per mol proportion of zinc dithiophosphate, said coordinated salt being prepared by the method which comprises (1) forming a reaction mixture of one mol proportion of (A) a zinc dithiophosphate salt of the formula where R is a hydrocarbon radical selected from the group consisting of (a) aryl radicals, (b) alkyl-substituted aryl radicals having from one to 5 alkyl radicals substituted on the aryl nucleus thereof, each of said alkyl radicals having from one up to about 20 carbon atoms and (c) alkyl radicals containing from 5 to about 20 carbon atoms in which the carbon atom adjacent to the carbon atom attached to the oxygen atom in said formula is completely substituted with alkyl groups, (B) at least one mol proportion of a Zinc salt of a carboxylic acid selected from the group consisting of (a) alipha
  • a zinc acetatecoordinated zinc bis(nonylphenyl)dithiophosphate salt composed of approximately one mol proportion of zinc acetate per mol proportion of zinc bis(nonylphenyl)dithiophosphate, said coordinated salt being prepared by the method which comprises (1) forming a reaction mixture of (A) one mol proportion of normal bis(nonylphenyl)- dithiophosphate, (B) at least one mol proportion of zinc acetate, (C) water and (D) a hydrocarbon solvent; (2) heating the reaction mixture to distill oi the water and a portion of the hydrocarbon solvent as an azeotropic mixture; (3) filtering the reaction mixture to obtain a solvent solution of the zinc acetate-coordinated zinc bis- (nonylphenyl)dithiophosphate; and (4) distilling off the remainder of the solvent.
  • a Zinc acetate-coordinated zinc bis(2,2,4-trimethyl-l-pentyl)dithiophosphate salt composed of approximately one mol proportion of zinc acetate per mol proportion of zinc bis(2,2,4- trimethyl-l-pentyl)dithiophosphate, said coordinated salt being prepared by the method which comprises (1) forming a reaction mixture of (A) one mol proportion of normal bis(2,2,4-trimethyl-1-pentyl)dithiophosphate, (B) at least one mol proportion of zinc acetate, (C) water and (D) a hydrocarbon solvent; (2) heating the reaction mixture to distill off the water and a portion of the hydrocarbon solvent as an azeotropic mixture; (3) filtering the reaction mixture to obtain a solvent solution of the zinc acetate-coordinated zinc bis(2,2,4-trimethyl-1-pentyl)- dithiophosphate; and (4) distilling off the remainder of the solvent.
  • a zinc naphthenatecoordinated zinc bis(mixed phen0ls) dithiophosphate salt composed of approximately one mol proportion of zinc naphthenate per mol proportion of zinc bis(mixed phenols) dithiophosphate, said coordinated salt being prepared by the method which comprises (1) forming a reaction mixture of (A) one mol proportion of normal bis(mixed phenols)dithiophosphate, (B) at least one mol proportion of zinc naphthenate, (C) water and (D) a hydrocarbon solvent; (2) heating the reaction mixture to distill off the water and a portion of the hydrocarbon solvent as an azeotropic mixture; (3) filtering the reaction mixture to obtain a solvent solution of the zinc naphthenatecoordinated zinc bis(mixed phenols)dithiophosphate; and (4) distilling off the remainder of the solvent.
  • a lubricating oil containing a minor amount, from about 0.01% to about by weight, of a zinc acetatecoordimated zinc bis(nonylphenyl) dithiophosphate salt composed of approximately one mol proportion of zinc acetate per mol proportion of zinc bis(nonylphenyl)dithophosphate, said ooordinated salt being prepared by the method which comprises (1) forming a reaction mixture of (A) one mol proportion of normal bis(nonyl phenyDdithiophosph-ate, ('B) at least one mol proportion of zinc acetate, (C) water and (D) a hydrocarbon solvent; (2) heating the reaction mixture to distill ofi the Water and a portion of the hydrocarbon solvent as an azeotropic mixture; (3) filtering [the reaction mixture to obtain a solvent solution of the zinc acetate-coordinated bis(nonylphenyl)tdithiophosphate; and (4) distilling olf the remainder of the solvent

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Description

United States Patent LUBRICATING 01L CONTAINING ZINC CARBOX- YLATE-COORDINATED Z I N C DITHIOPHGS- PHATES I Edwin M. Nygaard and Edward A. Oberright, Woodbury, N.J., assignors to Socony Mobil Oil Company, Inc, a corporation of New York No Drawing. Filed Dec. 20, 1960, Ser. No. 76,998
8 Claims. (Cl. 25232.7)
The invention relates to improved lubricating oil compositions. More specifically, it relates to lubricating oil compositions which are substantially non-corrosive to silver.
As is well known, in certain types of diesel engines, such as those used by railroads, silver bushings are used as the bearing surfaces with steel wrist pins. As is also known, a serious problem encountered in the lubrication of these engines is that of inhibiting corrosion of the silver bearing surfaces. Thus, Well-known commercial antioxidants and bearing corrosion inhibitors, although highly satisfactory for use in lubricating oils for other types of engines, are not suitable for use in oils designed for the lubrication of engines containing silver bearings. For example, zinc salts of dithiophosphoric acids are widely used as antioxidants and bearing corrosion inhibitors in engine oils. However, experience has shown that when oils containing these salts are used in engines containing silver bearings, such as railnoad diesels, rather than inhibiting corrosion, they actually attack and corrode the silver bearing surfaces. ,A means of overcoming this deficiency in these otherwise highly useful additives has been extensively sought by the art. The present invention provides such a means.
In accordance with the present invention, it has now been found that the corrosiveness towards silver of certain zinc dithiophosphate salts can be overcome by reacting these salts with zinc carboxylates. More specifically, it has been found that two types of zinc dithiophosphate salts, viz., (1) normal zinc bis(aryl)dithiopl1osphates and (2) normal zinc bis(alkyl)dithiophosphates prepared from so-called neoor hindered-type alcohols, i.e., alcohols in which the carbon atom adjacent to the carbon atom attached to the hydroxyl group is completely substituted' with alkyl groups, when reacted with zinc carboxylate salts, as hereinafter described, are made noncorrosive (to silver. Conversely, it has been found that zinc bis(alkyl)dithiophosphates, other than those derived 7 from neo-type alcohols, are not made non-corrosive to silver by reaction thereof with zinc carboxylates. Although the manner in which the zinc dithiophosphate and zinc .carboxylate salts are combined in the reaction -of the invention is not known with certainty, it is theorized, without wishing to limit the invention in any way, that they are joined by coordinate bonds similar to those existing in complexes of the Werner-type. For convenience, therefore, the product salts are referred to herein as zinc carboxylate-coordinated zinc dithiophosphate salts.
As far as is known, the zinc carboxylate-coordinated zinc dithiophosphate salts contemplated by the invention have not been known heretofore and they are, therefore, believed to be new compositions of matter. Accordingly, it is the primary object of the invention to provide a new class of zinc dithiophosphate salts which are non-corrosive to silver, viz., zinc carboxylate-coordinated zinc dithiophosphate salts. A further object is to provide lubricating oil compositions containing these new coordinated salts. Other and further objects of the invention will be apparent from the following detailed description.
Broadly, in accordance with the invention, the zinc carboxylate-coordinated zinc dithiophosphate salts are produced by l) forming a reaction mixture of '(A) one mol 3,162,096 Patented Aug. 27, 1963 proportion of Zll'lC dithiophosphate, -(B) at least one mol proportion of zinc carboxylate, (C) water and (D) a hydrocarbon solvent and (2) heating the mixture to a temperature sufficient to distill off the water, whereby a solvent solution of the zinc carboxylate-coordinated zinc dithiophosphate salt, containing approximately one mol proportion of each of the reactant salts, is produced. The product mixture is then filtered to remove any unreacted salt. Preferably, a light hydrocarbon solvent, such as xylene, toluene or a petroleum naphtha, is used and the water distilled off as an azeotropic mixture with the solvent. After the water has been completely removed, a lubricating oil may be added to the solvent mixture and the remainder of the solvent distilled off (or the solvent can be removed before the oil is added) whereby a lubricating oil concentrate of the product salt, suitable for blending with the base lubricating oil, is obtained.
The normal zinc bis(aryl)dithiophosphates to which the invention is applicable are those containing aryl radicals, such as phenyl, naphthyl or the like, which radicals may have one or more (up to 5) alkyl groups of from one up to about 20 carbon atoms substituted thereon Thus, normal zinc salts, such as the following, are contemplated by the invention:
As afore-indicated, the normal zinc salts of bis(alkyl)- dithiophosphoric acids which ane improved by the invention are those derived from aliphatic alcohols having 2 neo or hindered carbon atom adjacent to the carbon atorr bearing the hydroxyl group. These alcohols conform tc the structure where R is alkyl. These alcohols and consequently the alkyl groups derived therefrom may contain from 5 up to about 20 carbon atoms. Examples of suitable zinc dithiophosphate salts of this type are the following:
Zinc bis(2,2-dimethyl-l-propy1)dithiophosphate Zinc bis(2,2,4-trimethyl-l-pentyl)dithiophosphate Zinc bis(2,2-dimethyl-1-decyl)dithiophosphate Zinc bis(2,2,4-trimethyl-l-hexadecyl) dithiophosphate The zinc carboxylates with which the Zinc dithiophos phate salts may be coordinated in accordance with the in vention may be either aliphatic or aromatic in nature The aliphatic Zinc carboxylates may be of the straight chained, branch-chained or cyclic type and may contair from 1 to about 20 carbon atoms. Examples of thes salts are zinc acetate, Zinc formate, zinc butyrate, zir1 decanoate, zinc stearate, zinc oleate, zinc linoleate and th like. Also, Zinc naphthenate salts, derived from petroleun oil naphthenic acids, are also highly suitable. The aro matic carboxylate salts include, for example, zinc ben zoate, zinc salicylate and such salts which also have one or more alkyl groups having from 1 to 20 carbon atom: each substituted on the aromatic ring thereof.
The invention will be more fully understood by ref erence to the following examples and test results illustrat ing typical preparations of the coordinated zinc dithio phosphate-zinc carboxylate salts and their effectivenes: in reducing silver corrosion as compared to the norma zinc dithiophosphate salts.
"7 :3 EXAMPLE 1 Preparation of Normal Zinc Salt of Bis(Nnylphenyl)- Ditlzioplzosphoric Acid Into a dry S-liter, 4-necked flask, equipped with a stirrer, thermometer, broad tube for introducing phosphorus pen-tasulfide and a distilling receiver hooked to a reflux condenser protected by a calcium chloride tube, there was charged 792 grams (3.6 mols) of nonylphenol, 161.1 grams (1.98 mols) of zinc oxide (i.e., 120% excess in order to insure complete conversion of dithiophosphoric acid to normal salt) and 1500 cc. of xylene. The mixture was dehydrated by refluxing for one and one-half hours. The temperature was then lowered to 130135 C. and 199.8 grams (0.9 mol) of phosphorus pentasulfide added, portionwise, over a period of one and one-half hours While maintaining the temperature at 130135 C. The mixture was then heated to reflux and refluxed for one hour (144l45 C.). The mixture was then cooled to approximately 90 C. and 150 cc. of distilled water added over a period of about one-half hour. The temperature was held at 8893 C. for two hours to form the normal zinc salt of bis('nonylphenyl)dithiophosphate. The mixture was then heated to reflux to azeotrope the water. The product was then cooled to about 100 C. and filtered through Super-Cel (a diatomaceous earth filter aid). The xylene was then removed at reduced pressure using a water-bath-as a source of heat. The reaction mixture was then diluted with approximately 25%, by weight, of mineral oil (100 S.U.S. 100 F.), warmed on a waterbath and filtered through a bed of cuper-Cel. The product oil solution analyzed as follows: zinc=5.0%, sulfur=7.3% and phosphorus=3.9%.
EXAMPLE 2 Preparation of Zinc Acetate Coordinated-Zinc Bis(N0nylphenyl)Dithiophlosphate Into a -liter, 4-necked flask equipped with a stirrer, thermometer and distilling receiver connected to a reflux condenser protected by a calcium chloride tube, there was charged 792 grams (3.6 mols) of nonylphenol, 161.1 grams (1.98 mols) of zinc oxide and 1500 cc. of xylene. The mixture was refluxed to dehydrate the apparatus and its contents. The temperature was reduced to 130 C. and 199.8 grams (0.9 mol) of P 3 was added over a period of one and one-quarter hours keeping the temperature at 130-135 C. The temperature was raised to reflux and the mixture refluxed for one hour (144147 C.). The temperature was reduced to approximately 90 C. and 150 cc. of distilled water was added from the dropping funnel over a period of about 15 minutes. The temperature was maintained at 9095 C. for two hours in order to form the normal zinc salt of bis(n0nylphenyl)- dithiophosphoric acid.
197.6 grams (0.9 mol) of Zn(C I-I O .2H O dissolved in 350 cc. of hot distilled water was next added to the reaction mixture. The temperature was then raised to azeotrope the Water, the final temperature being about 146 C. A total of 525 cc. of water was azeotroped. The product was then filtered through a bed of Super-Col.
An amount of paraffinic mineral oil (100 S.U.S. 100 F.) was then added to provide a xylene-free salt product containing about 25%, by weight, of oil. The xylene was removed at reduced pressure using a waterbath as a source of heat. The product analyzed as follows: zinc=8.85%, sulfur=5.73% and phosphorus=3.24%.
EXAMPLE 3 Preparation of Zinc Bis(2,2,4-Trimethyl-1- Pentyl)Dithiophosphale Into a 2-liter, 4-necked flask equipped with a stirrer, thermometer, reflux condenser protected by a calcium chloride tube and a broad, closeable tube for periodically introducing P 5 was weighed 676 grams (5.2 mols) of 4 2,2,4-trirnethyl-1-pentanol. The P S 288.6 grams (1.3 mols), was added over a 38-minute period at a reaction temperature of 6878 C. The mixture was then stirred and heated for four hours at a temperature of 89-93 C. The whole was then filtered into a dropping funnel to remove unreacted P S In another 2-liter, 4-necked flask, equipped with a stirrer, thermometer, reflux condenser and the above-mentioned dropping funnel protected by a calcium chloride tube, were placed in turn 158.8 grams (1.95 mols) of zinc oxide and 465 cc. of distilled water. The dithiophosphoric acid was added from the dropping funnel over a period of two and three-quarter hours at a reaction temperature of 60-67 C. During this period cc. of benzene was added to thin the mixture. The mixture was then held at this temperature for one and one-half hours. The temperature was then raised to a maximum of 110 C. to azeotrope the water, 200 co. more of benzene being added to reduce the reflux temperature. The mixture was then filtered through Super-Gel. The benzene was removed at reduced pressure using a boiling water-bath as a source of heat. The product was a pale, viscous liquid. It analyzed as follows: zinc=8.9%, sulfur=15.7% and phosphorus=7.7
EXAMPLE 4 Preparation of Zinc Acetate-Coordinated Salt of Example 3 Into a 2-liter, 4-necked flask equipped with a stirrer, thermometer, a distilling receiver hooked to a reflux condenser and a dropping funnel protected by a calcium chloride tube, were placed in turn 102 grams (1.26 mols) of zinc oxide and 300 cc. of distilled water. To the stirred mixture was added 593 grams (1.68 mols) of the dithiophosphoric acid prepared as described in the first part of Example 3. The acid was added in about two hours at a reaction temperature of 6067 C. During the acid addition 100 cc. of benzene was added to thin the mixture. The mixture was stirred for an additional one and onehalf hours at 6263 C. 184 grams (0.84 mol) of zinc acetate dihydrate dissolved in 326 cc. of hot distilled water was then added. The temperature was then raised to azeotrope the water, 129 cc. of benzene being added to reduce the temperature during azeotroping (84106 C.). The whole was then filtered through Super-Cel. The benzene was then removed at reduced pressure using a boiling water-bath as a source of heat. The product was a pale, viscous liquid. It analyzed as follows: zinc=15.1%, sulfur=12.7% and phosphorus:6.6%.
EXAMPLE 5 This was a commercial additive-normal zinc bis(4- methyl-2-pentyl)dithiophosphate containing 15%, by Weight, of dilution oil. It showed the following analysis: zinc=9.5%, sulfur=17.4% and phosphorus=8.6%.
EXAMPLE 6 Preparation of Zinc Acetate-Coordinated Salt 0 Example 5 into a 2-liter, 4-necked flask, equipped with a stirrer, thermometer and a distillate receiver hooked to a reflux condenser was weighed grams of the additive of Example 5 [equivalent to 164.8 grams (0.25 mol) of zinc bis(4 methyl 2 pentyl)dithiophosphate on an oil-free basis]. This material was diluted with 400 cc. of toluene 65.9 grams (0.30 mol) of zinc acetate dihydrate, dissolved in 227 cc. of warm distilled water, was then added. The mixture was stirred and heated to azeotrope the water. The maximum azeotroping temperature was 116 C. The product was then filtered through a bed of Super- Cel. The product was then removed at reduced pressure using a boiling water-bath as a source of heat. The product was a fairly fluid, dark amber-colored liquid. It has the following analysis: zinc=12.8%, sulfur=16.6% and phosphorus=7.6%
5 EXAMPLE 7 Preparation of Zinc Acetate-Coordinated Salt of Zinc Bis(n-Octyl)Dithiophosphate Into a dry 500 cc. 4-necked flask equipped with a thermometer, stirrer, reflux condenser protected by a calcium chloride tube and a broad, closeable tube for introducing P 8 was weighed 78.0 grams (0.6 mol) of noctyl alcohol. The P 8 3333 grams (0.15 mol) was then added in small increments to the alcohol held at 6070 C. The temperature was then raised to 90 C. and held there for four hours. The product was then filtered into a dry dropping funnel.
Into a one-liter, 4-necked flask equipped with a stirrer, thermometer, dropping funnel containing the above-prepared dithiophosphoric acid and a distilling receiver hooked to a reflux condenser was weighed 18.3 grams (0.225 mol) of zinc oxide. 54 cc. of water was then added. The acid was added slowly to the stirred slurry of zinc oxide and water and the whole heated to 60 65 C. The thick mixture was thinned with 250 cc. of benzene. The temperature was then raised to 75 C. and held there for two hours. Zinc acetate dihydrate, 36.3 grams (0.16 mol), dissolved in 100 cc. of distilled water, was then added. The mixture was then refluxed to azeotrope the water. The product was then filtered through Super- Cel. The benzene was then removed at reduced pressure using a water-bath as a source of heat. The product was a fairly fluid, colorless liquid. It analyzed as follows: zinc=15.4%, sulfur=11.7% and phosphorus=6.3%.
EXAMPLE 8 Preparation of Zinc NaphthenateCoordinated Salt of Zinc B'is(Mixed Phenl)Dithioph0sphate Into a one-titer, 4-necked flask, equipped with a stirrer, thermometer and a distilling receiver hooked to a reflux condenser protected by a calcium chloride tube and a broad closeable tube for introducing P there was placed in turn 63.7 grams (0.6 mol) of a mixture of 40%, by weight, of phenol, 56%, by weight, of cresols and 4%, by weight, of xylenols, 250 milliliters of xylene and 40.5 grams (0.5 mol) of zinc oxide. The mixture was stirred and refluxed at approximately 144 C. to remove all water from the system. The temperature was reduced to approximately 130 C. and 34.3 grams (0.15 mol) of phosphorus pentasulfide was added over a period of 50 minutes at a reaction temperature of 130-135 C. The temperature of the mixture was raised to reflux (Ml-142 C.) and refluxed for one hour. The temperature was then reduced to approximately 90 C. and 88.0 grams (0.225 mol) of petroleum naphthenic acid was added, followed by 50 milliliters of distilled Water. The mixture was stirred and heated for two hours at 9093 C. The temperature was then raised to azeotrope the water (144 C.). The mixture was then cooled and filtered through Super-Cal. The filtrate was washed with 150 milliliters of fresh xylene. The xylene was removed from the filtrate at reduced pressure using a water-bath as a source of heat. The product was a very viscous da-rkabrown liquid. After being fluidized by the addition of 25% by weight, of mineral oil, (100 S.U.S. 100 F.), it showed the following analysis: zinc=9.9%, sulfur=6.3% and phosphorus: 3.3%.
SILVER CORROSION TEST The non-corrosiveness towards silver of the zinc carboxylate-coordinated zinc dithiophosphate salts of the invention as compared to the uncoordinated zinc dithiophosphate salts is illustrated by the following series of tests conducted on the additives :of the foregoing Examples 1-8.
The test method used was that developed by the Electro-Motive Division of General Motors Corporation, designated EMD Method No. LO. 201-47, for determining the corrosivity towards silver of a heavy duty lubricating oil. In brief, the procedure consists in heating in an oil bath held at 325 F.i2 F., 300 milliliters of lubricating oil contained in a 600-milliliter beaker. The oil is stirred at 300 rpm. When the test oil is up to temperature, a weighed section of a silver-plated wrist-pin bushing (approximate size 3" x 1" x A1"lead flashing removed from surface prior to test) is suspended in the oil so that it is immersed to approximately of its surface area. At the end of 72 hours the bushing section is removed from the oil, washed with carbon tetrachloride and dried. The corrosion layer is then electrolytically removed after which the bushing is washed with water and alcohol and dried by wiping with a cloth and placing it in an oven held at F. for 10 minutes. After cooling in a desiccator, it is reweighed. If the weight loss is no greater than 5 milligrams, the oil is considered to have passed the test.
The lubricating oil used in the tests was a Mid-Continent solvent-refined, all paraflin distillate having an S.U.V. of 77 seconds at 210 F. In order to provide a proper comparison between the additives, the percentage of additive used in the oil in each instance was adjusted to give the same percentage of zinc bound to sulfur (excludes the zinc bound to zinc carboxylate coordinating agent) as contained in 0.44% and 0.89%, by weight, respectively, of the normal zinc bis(4-methyl-2-pentyl)dithiophosphate additive (Example '5). The test results are shown in Table I.
Table 1 Silver Corrosion 325 F.
Additive Used Wt, Silver Percent Loss,
None 1.5 Zine bis(nonylphenyl)dithiophosphate (Example 1)- 1. 04 19. E Do 2. 07 43.1 Zinc acetate-coordinated salt of Example 1 (Example 2) 0.95 0.5 Do 1.90 1.3 Zinc blS (2,2,4-trimetl1yl-1-pentyl)dithiophosphate (Example 3) 0. 47 18. 1 Do 0.94 48.1 Z1110 acetate-coordinated salt of Example 3 (Ex ample 4) 0.62 1. E Do 1.24 2.1 Zinc b1s(4-methyl-2-pentyl)dithiophosphate (Example 5) 0. 44 19. l D0 0.89 38.9 Zine acetate-coordinated salt of Example 5 (Example 6) 0.48 25.2 D0 0.96 65.4 Zinc acetate-coordinated salt of zinc bis(n'octyl) dithiophosphate (Example 7) 0. 55 9. l Do 1.10 36.2 Zmc naphthenate-coordinated salt of zinc bis (mfixed phenol)dithiophosphate (Example 8) 0.85 1.! o 1. 69 3.(
Referring to Table I, it is seen that all three of the uncoordinated salts (Examples 1, 3 and 5) are highly corrosive to silver. It is seen, however, that whereas the zinc bis(aryl)dithiophosphates and the zinc bis(alkyl)dithiophosphates derived from hindered-type aliphatic alcohols are made non-corrosive to silver by forming the co ordination salts thereof in accordance with the inventior (compare Examples 1 and 3 with Examples 2 and 4, respectively; also, note Example 8), the zinc bis(alkyl)dithiophosphate derived from non-hindered type aliphatic alcohols are not made non-corrosive by the formation 01 the coordination salts thereof. (Compare Examples 5 and 6; also, note Example 7.)
'As shown by analysis, the coordinated salts contemplated by the invention contain approximately one mo of zinc carboxylate per mol of zinc dithiophosphate. 11 has been found that if less than approximately one moi of the zinc carboxylate is combined with the zinc dithiophosphate salt, the resulting coordinated salt will no? pass the silver corrosion test. The amount of zinc carboxylate salt used in the reaction with the zinc dithiophos- 7 phate salt, therefore, must be at least about one mol per mol of zinc dithiophosphate, the use of a moderate excess over this amount, say, from 10% to about 50%, being preferred in order to insure incorporation of the required one mol proportion thereof in the coordinated salt product.
Also, as brought out herein, the presence of water is essential to the coordination reaction, the minimum required amount being about 0.5 mol per mol of zinc dithiophosphate being reacted with the zinc carboxylate. The reaction is greatly facilitated, however, by the use of much larger amounts, say, from 10 to about 50 mols of water per mol of zinc dithiophosphate being reacted. Actually, the upper limit of the amount of water is not critical and the amount used is, therefore, governed largely by practical considerations.
As shown in the examples presented herein, the coordinated salt products of the invention may conveniently be prepared in the form of concentrated oil solutions thereof which solutions are readily blendable with base oils desired to be improved thereby. The concentration of the product salt in these solutions will depend, of course, on the amount of diluent oil used in the process. For commercial purposes this amount can be standardized to provide a specified level of concentration. Expressed on an oil-free basis, however, the amount of the coordinated salt to be utilized in lubricating oil will range from about 0.01% to about 10%, by Weight, the usual amount being from about 0.5% to about 5%.
The lubricating oil to which the salts of the invention are added may also contain other addition agents designed to improve the characteristics of the oil in various respects, such as detergents, pour point depressants, viscosity index improvers, extreme pressure agents, additional antioxidants, etc.
Although the present invention has been described herein by means of certain specific embodiments and illustrative examples, it is not intended that the scope thereof be limited in any Way thereby but only as indicated in the following claims.
What is claimed is:
1. As a new composition of matter, a zinc carboxylatecoordinated zinc dithiophosphate salt composed of approximately one mol proportion of zinc carboxylate per mol proportion of zinc dithiophosphate, said coordinated salt being prepared by the method which comprises (1) forming a reaction mixture of one mol proportion of (A) a zinc dithiophosphate salt of the formula where R is a hydrocarbon radical selected from the group consisting of (a) aryl radicals, (b) alkyl-substituted aryl radicals having from one to 5 alkyl radicals substituted on the aryl nucleus thereof, each of said alkyl radicals having from one up to about 20 carbon atoms and (c) alkyl radicals containing from 5 to about 20 carbon atoms in which the carbon atom adjacent to the carbon atom attached to the oxygen atom in said formula is completely substituted with alkyl groups, (B) at least one mol proportion of a Zinc salt of a carboxylic acid selected from the group consisting of (a) aliphatic carboxylic acids having from one to about 20 aliphatic car-' bon atoms and (b) aryl carboxylic acids and alkylsubstituted aryl carboxylic acids having from one up to alkyl groups substituted on the aryl nucleus thereof, each of said alkyl groups containing from one to about 20 carbon atoms, (C) water and (D) a hydrocarbon solvent; (2) heating the reaction mixture to remove the water therefrom by distillation; and (3) filtering the reaction mixture to obtain a solvent solution of the zinc carboxylate-coordinated zinc dithiophosphate salt.
2. As a new composition of matter, a zinc acetatecoordinated zinc bis(nonylphenyl)dithiophosphate salt composed of approximately one mol proportion of zinc acetate per mol proportion of zinc bis(nonylphenyl)dithiophosphate, said coordinated salt being prepared by the method which comprises (1) forming a reaction mixture of (A) one mol proportion of normal bis(nonylphenyl)- dithiophosphate, (B) at least one mol proportion of zinc acetate, (C) water and (D) a hydrocarbon solvent; (2) heating the reaction mixture to distill oi the water and a portion of the hydrocarbon solvent as an azeotropic mixture; (3) filtering the reaction mixture to obtain a solvent solution of the zinc acetate-coordinated zinc bis- (nonylphenyl)dithiophosphate; and (4) distilling off the remainder of the solvent.
3. As a new composition of matter, a Zinc acetate-coordinated zinc bis(2,2,4-trimethyl-l-pentyl)dithiophosphate salt composed of approximately one mol proportion of zinc acetate per mol proportion of zinc bis(2,2,4- trimethyl-l-pentyl)dithiophosphate, said coordinated salt being prepared by the method which comprises (1) forming a reaction mixture of (A) one mol proportion of normal bis(2,2,4-trimethyl-1-pentyl)dithiophosphate, (B) at least one mol proportion of zinc acetate, (C) water and (D) a hydrocarbon solvent; (2) heating the reaction mixture to distill off the water and a portion of the hydrocarbon solvent as an azeotropic mixture; (3) filtering the reaction mixture to obtain a solvent solution of the zinc acetate-coordinated zinc bis(2,2,4-trimethyl-1-pentyl)- dithiophosphate; and (4) distilling off the remainder of the solvent.
4. As a new composition of matter, a zinc naphthenatecoordinated zinc bis(mixed phen0ls) dithiophosphate salt composed of approximately one mol proportion of zinc naphthenate per mol proportion of zinc bis(mixed phenols) dithiophosphate, said coordinated salt being prepared by the method which comprises (1) forming a reaction mixture of (A) one mol proportion of normal bis(mixed phenols)dithiophosphate, (B) at least one mol proportion of zinc naphthenate, (C) water and (D) a hydrocarbon solvent; (2) heating the reaction mixture to distill off the water and a portion of the hydrocarbon solvent as an azeotropic mixture; (3) filtering the reaction mixture to obtain a solvent solution of the zinc naphthenatecoordinated zinc bis(mixed phenols)dithiophosphate; and (4) distilling off the remainder of the solvent.
5. A lubricating oil containing a minor amount, from about 0.01% to about 10%, by weight, of a zinc carboxylate-cooirdinated Zinc dithiophosphate salt composed of approximately one mol proportion of zinc carboxylate per mol proportion of zinc dithiophosphate, said coordinated salt being prepared by the method which comprises (1) forming a reaction mixture of one mol proportion of (A) a zinc dithiophosphate salt of the formula where R is a hydrocarbon radical selected from the group consisting of (a) aryl radicals, (b) alkyl-substituted aryl radicals having from one to 5 alkyl radicals substituted on the aryl nucleus thereof, each of said alkyl radicals having from one up to about 20 carbon atoms and (c) alkyl radicals containing from 5 to about 20 carbon atoms in which the carbon atom adjacent to the carbon atom attached to the oxygen atom in said formula is completely slrbstituted with alkyl groups, (B) at least one mol proportion of a zinc salt of a carboxylic acid selected from the group consisting of (a) aliphatic carboxylic acids having from one to about 20 aliphatic carbon atoms, (b) aryl carboxylic acids and (c) alkyl-substituted aryl carboxylic acids having from one up to 5 alkyl groups substituted on the aryl nucleus mhereof, each of said alkyl groups containing from one to about 20 carbon atoms, (C) water and (D) a hydrocarbon solvent; (2) heating the reaction mixture to distill ofif the Water and a portion of the hydrocarbon solvent as an azeotropic mixture; (3) filtering the reaction mixture to obtain a 9 solvent solution of the zinc. oarboxylate-ooordinated zinc dithiophosphate salt; and (4) distilling olf the remainder of the solvent.
6. A lubricating oil containing a minor amount, from about 0.01% to about by weight, of a zinc acetatecoordimated zinc bis(nonylphenyl) dithiophosphate salt composed of approximately one mol proportion of zinc acetate per mol proportion of zinc bis(nonylphenyl)dithophosphate, said ooordinated salt being prepared by the method which comprises (1) forming a reaction mixture of (A) one mol proportion of normal =bis(nonyl phenyDdithiophosph-ate, ('B) at least one mol proportion of zinc acetate, (C) water and (D) a hydrocarbon solvent; (2) heating the reaction mixture to distill ofi the Water and a portion of the hydrocarbon solvent as an azeotropic mixture; (3) filtering [the reaction mixture to obtain a solvent solution of the zinc acetate-coordinated bis(nonylphenyl)tdithiophosphate; and (4) distilling olf the remainder of the solvent.
7. A lubricating oil containing a minor amount, from about 0.01% to about 10%, by weight, of a zinc acetatecoordinated zinc .bis(2,2,4-trimethyl-1-pentyl)dithiophosphate salt composed of approximately one mol proportion of zinc aoetate per mol proportion of zinc 'bis(2,2,4-trimethyl-1-pentyl)dithiophosphate, said coordinated salt being prepared by the method which comprises (1) fonming a reaction mixture of (A) one mol proportion of normal bis(2,2,4-t1imethy1-1-pentyl)dithiophosphate, (B) at least one mol proportion of zinc acetate, (C) water and (D) a hydrocarbon solvent; (2) heating the reaction mixture to distill oi? the water and a portion of the laydrocarbon solvent as an azeotropic mixture; (3) filtering the reaction mixture to obtain a solvent solution of the 10 zinc acetate-coordinated zinc bis(2,2,4 trimethyl-lpentyDdithiophosphate; and (4) distilling oi the remainder oi the solvent.
8. A lubricating oil containing a minor amount, from about 0.01% to about 10%, by weight, of a zinc naphthenate-coordinated zinc bis(mixed phenols) dithiophosph-ate salt composed of approximately one mol proportion of zinc naphthenate per mol proportion of zinc bis(mixed phenols)dithiophosphate, said coordinated salt being prepared by the method which comprises (1) forming a reaction mixture of (A) one mol proportion of normal bis (mixed phenols)dithiophosphate, (B) at least one mol proportion of zinc naphthenate, (C) Water and (D) a hydrocarbon solvent; 2) heating the reaction mixture to distill oil? the Water and a portion of the hydrocarbon solvent as an azeotropic mixture; (3) filtering the reaction mixture to obtain a solvent solution of the zinc naphthenate-coordinated zinc bistnu'xed phenols)dithiophosphate; and (4) distilling off the remainder of the solvent.
References Cited in the file of this patent UNITED STATES PATENTS 2,726,208 Karll et al. Dec. 6, 1955 2,790,766 Otto Apr. 20, 1957 FOREIGN PATENTS 550,586 Canada Dec. 24, 1957 OTHER REFERENCES Kosolapoif: Organophosphorus Compounds, John Wiley & Sons, N.Y., 1950, pp. 220-241.

Claims (1)

1. AS A NEW COMPOSITION OF MATTER, A ZINC CARBOXYLATECOORDINATED ZINC DITHIOPHOSPHATE SALT COMPOSED OF APPROXIMATELY ONE MOL PROPORTION OF ZINC CARBOXYLATE PER MOL PROPORTION OF ZINC DITHIPHOSPHATE, SAID COORDINATED SALT BEING PREPARED BY THE METHOD WHICH COMPRISES (1) FORMING A REACTION MIXTURE OF ONE MOL PROPORTION OF (A) A ZINC DITHIOPHOSPHATE SALT OF THE FORMULA
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Cited By (12)

* Cited by examiner, † Cited by third party
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US3290347A (en) * 1963-02-28 1966-12-06 Exxon Research Engineering Co Preparation of polyvalent metal salts of diorgano dithiophosphoric acids
US3328335A (en) * 1964-08-31 1967-06-27 Mobil Oil Corp Lubricating oils containing complex zinc salts
DE1255658B (en) * 1965-07-01 1967-12-07 Lubrizol Corp Process for the production of heat and oxidation resistant metal salts of phosphoric acid compounds
US3396183A (en) * 1964-04-29 1968-08-06 Exxon Research Engineering Co One step preparation of metal organo dithiophosphates
US3414598A (en) * 1964-08-24 1968-12-03 Mobil Oil Corp Method of preparing zinc carboxylate coordinated complexes of aromatic zinc dithiophosphates
US3523081A (en) * 1967-02-01 1970-08-04 Mobil Oil Corp High metal content additives for fluid compositions
US4288335A (en) * 1979-03-09 1981-09-08 Orogil Novel metallic dithiophosphates and their use as additives for lubricating oils
US4293430A (en) * 1979-03-09 1981-10-06 Orogil Sulfurized metallic dithiophosphates and their use as additives for lubricating oils
WO1989009812A1 (en) * 1988-04-11 1989-10-19 The Lubrizol Corporation Lubricating oil additives
US5356552A (en) * 1993-03-09 1994-10-18 Chevron Research And Technology Company, A Division Of Chevron U.S.A. Inc. Chlorine-free lubricating oils having modified high molecular weight succinimides
US6294506B1 (en) 1993-03-09 2001-09-25 Chevron Chemical Company Lubricating oils having carbonated sulfurized metal alkyl phenates and carbonated metal alkyl aryl sulfonates
EP4353805A1 (en) 2022-10-11 2024-04-17 Infineum International Limited Lubricant composition containing metal alkanoate

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DE2108780C2 (en) * 1971-02-24 1985-10-17 Optimol-Ölwerke GmbH, 8000 München Lubricant or lubricant concentrate
GB1568647A (en) * 1977-03-18 1980-06-04 Shell Int Research Dthiophosphoric acid diesters and salts thereof
US4308154A (en) * 1979-05-31 1981-12-29 The Lubrizol Corporation Mixed metal salts and lubricants and functional fluids containing them
IN152910B (en) * 1979-05-31 1984-04-28 Lubrizol Corp
US4263150A (en) * 1979-06-11 1981-04-21 The Lubrizol Corporation Phosphite treatment of phosphorus acid salts and compositions produced thereby

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US2726208A (en) * 1954-10-15 1955-12-06 Standard Oil Co Non-corrosive lubricant composition
US2790766A (en) * 1955-10-20 1957-04-30 Socony Mobil Oil Co Inc Complex metal salts of phosphoric acid esters and mineral oil compositions containing the same
CA550586A (en) * 1957-12-24 O. Clayton James Oxidation-inhibited, silver non-corrosive lubricants

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CA550586A (en) * 1957-12-24 O. Clayton James Oxidation-inhibited, silver non-corrosive lubricants
US2726208A (en) * 1954-10-15 1955-12-06 Standard Oil Co Non-corrosive lubricant composition
US2790766A (en) * 1955-10-20 1957-04-30 Socony Mobil Oil Co Inc Complex metal salts of phosphoric acid esters and mineral oil compositions containing the same

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3290347A (en) * 1963-02-28 1966-12-06 Exxon Research Engineering Co Preparation of polyvalent metal salts of diorgano dithiophosphoric acids
US3396183A (en) * 1964-04-29 1968-08-06 Exxon Research Engineering Co One step preparation of metal organo dithiophosphates
US3414598A (en) * 1964-08-24 1968-12-03 Mobil Oil Corp Method of preparing zinc carboxylate coordinated complexes of aromatic zinc dithiophosphates
US3328335A (en) * 1964-08-31 1967-06-27 Mobil Oil Corp Lubricating oils containing complex zinc salts
DE1255658B (en) * 1965-07-01 1967-12-07 Lubrizol Corp Process for the production of heat and oxidation resistant metal salts of phosphoric acid compounds
US3523081A (en) * 1967-02-01 1970-08-04 Mobil Oil Corp High metal content additives for fluid compositions
US4288335A (en) * 1979-03-09 1981-09-08 Orogil Novel metallic dithiophosphates and their use as additives for lubricating oils
US4293430A (en) * 1979-03-09 1981-10-06 Orogil Sulfurized metallic dithiophosphates and their use as additives for lubricating oils
WO1989009812A1 (en) * 1988-04-11 1989-10-19 The Lubrizol Corporation Lubricating oil additives
US5356552A (en) * 1993-03-09 1994-10-18 Chevron Research And Technology Company, A Division Of Chevron U.S.A. Inc. Chlorine-free lubricating oils having modified high molecular weight succinimides
US6294506B1 (en) 1993-03-09 2001-09-25 Chevron Chemical Company Lubricating oils having carbonated sulfurized metal alkyl phenates and carbonated metal alkyl aryl sulfonates
EP4353805A1 (en) 2022-10-11 2024-04-17 Infineum International Limited Lubricant composition containing metal alkanoate

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DE1444892B1 (en) 1970-03-05
GB959115A (en) 1964-05-27
FR1310171A (en) 1963-03-06

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