US2734865A - Stabilized lubricating compositions - Google Patents

Stabilized lubricating compositions Download PDF

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US2734865A
US2734865A US2734865DA US2734865A US 2734865 A US2734865 A US 2734865A US 2734865D A US2734865D A US 2734865DA US 2734865 A US2734865 A US 2734865A
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    • 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
    • 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
    • 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
    • C10M2223/047Thioderivatives not containing metallic elements
    • 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
    • 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
    • C10N2010/00Metal present as such or in compounds
    • C10N2010/06Groups 3 or 13
    • 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
    • C10N2010/08Groups 4 or 14
    • 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
    • C10N2010/14Group 7
    • 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
    • C10N2010/16Groups 8, 9, or 10
    • 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
    • C10N2040/00Specified use or application for which the lubricating composition is intended
    • C10N2040/04Oil-bath; Gear-boxes; Automatic transmissions; Traction drives
    • 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
    • C10N2040/00Specified use or application for which the lubricating composition is intended
    • C10N2040/04Oil-bath; Gear-boxes; Automatic transmissions; Traction drives
    • C10N2040/042Oil-bath; Gear-boxes; Automatic transmissions; Traction drives for automatic transmissions
    • 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
    • C10N2040/00Specified use or application for which the lubricating composition is intended
    • C10N2040/04Oil-bath; Gear-boxes; Automatic transmissions; Traction drives
    • C10N2040/044Oil-bath; Gear-boxes; Automatic transmissions; Traction drives for manual transmissions
    • 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
    • C10N2040/00Specified use or application for which the lubricating composition is intended
    • C10N2040/04Oil-bath; Gear-boxes; Automatic transmissions; Traction drives
    • C10N2040/046Oil-bath; Gear-boxes; Automatic transmissions; Traction drives for traction drives
    • 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

  • This invention relates to lubricating oil additives; to lubricating oil compositions containing the same; and particularly to those oils of the type known as crankcase oils.
  • the improved lubricating oil compositions of the present invention are highly desirable for use in the crankcases of passenger automobiles, they are also especially valuable for heavy duty service in truck, bus, aeroplane, marine and diesel engines which operate for long periods of time at high temperatures.
  • the principal objects of the invention are to provide an improved lubricating oil of the heavy duty type which is heat stable, which is particularly resistant to sludge formation and oxidation, which is non-corrosive to alloy bearings and other metal parts under conditions of extreme service, and which is free from varnish formation and ring sticking tendencies.
  • hydrocarbon lubricating oil compositions having greatly improved detergent, anti-corrosive and antisludge forming properties may be prepared by the incorporation therein of minor amounts of various organic substituteddithiophosphates.V While the lubricating oil compositions containing these organic substituted dithiophosphates are extremely resistant to sludge formation under conditions of heavy duty service, we have found that, when preparing these lubricating oil compositions from ordinary classes of lubricating oils which are not highly refined, a certain amount of sludge will form when the oil is subjected to high temperatures in heavy duty service for, long periods of time in the presence of air or oxygen. With the more highly refined oils, howeve r, such as those treated bythe solvent refining process, the
  • R is a member of the group consisting of aryl, alkyl, aralkyl, cycloalkyl, aryloxyalkyl, acylaryl and alkoxyaryl radicals;
  • M is hydrogen or a salt-forming radical; and
  • n is the valence of M.
  • compounds of this class include the dialkyl dithiophosphates such as dibutyl dithiophosphate, dihexyl dithiophosphate, di n-octyl dithiophosphate, dicapryl dithiophosphate, dilauryl dithiophosphate, dioctadecyl dithiophosphate, etc.
  • diaryl dithiophosphates and the diaryl dithiophosphates in which the aryl group bears an alkyl, alkoxy or cycloaliphatic group are also useful such as for example diphenyl di thiophosphate, di-(2,4-diamyl phenyl) dithiophosphate, dikeryl diphenyl dithiophosphate (a product obtained by treating chlorinated kerosene with a phenol in the presence of aluminum chloride and then reacting with P235) and the various di-(wax substituted diaryl) dithiophosphates as described in detail in applicationSerial No.
  • alkyl group in the alkaryl radical to have 5 to 50 carbon atoms so that the compounds are more easily oil-soluble.
  • dicycloa1iphatic dithiophosphates such as those prepared by reacting cyclopentanol, cyclohexanol, cycloheptanol, and methyl, ethyl, propyl and amyl substituted cyclopentanol, cyclohexanol and cycloheptanol, etc. with P255.
  • di aryloxyalkyl dithiophosphates such as di-(2,4-diamylphenoxyethyl) dithiophosphate
  • diacylaryl dithiophosphates such as di-(lauroylphenyl) dithiophosphate
  • dialkoxyaryl dithiophosphates may also be added to lubricating oils to improve the oxidation stability of the oil.
  • these various organic substituted dithiophosphates in'the form of their metal salts, preferably the alkaline earth metal salts.
  • the various metal salts which may be employed are those of the salt-forming radicals nickel, aluminum, cadmium, tin, zinc, magnesium, calcium, strontium, barium and others.
  • the various organic-substituted dithiophosphates described above are employed by us in our improved lubricating oil compositions, preferably in amounts ranging from 0.1 to 3% or more by weight and normally at a concentration of approximately 0.6%. Smaller amounts, 0.05 to 2.0% or more, of the heat stabilizer, that is, the oil soluble reaction products of phosphorus sulfides and oxygenwiththetallpit fatty acid-alcohol esters or mixtures may be employed with the dithiophosphates to enhance the heat stability thereof.
  • T the 1 dithiophosphates to; break down under: high temperatures, or the; higher its; concentration in the oil composition, then, the, more heat stabilizer should be employed;
  • The-amount of both; of these substituents in the oil. will also depend; to some extent upon; the purpose for which the oil isgintendedr For example, an oil intended'for extremely: heavy duty service should contain more of both the dithiophosphate; and the phosphorus sulfide. reaction product as comparedwith the amounts required by an oil intended for, ordinary usage.
  • the invention is particularly applicable to compositions comprising the organic substituted dithiophosphates, previously described, and to those reaction products of phosphorus sesquisulfide (P453); and the tall oil fatty acid-alcohol esters or mixtures.
  • tall oil fatty acids is intended to refer to and include those fatty acids normally found in tall oil as well as those fatty acids having very similar properties, asrequired for the specific purposes herein referred. to.
  • these acidsv contain 16 to 18 carbon atoms and may contain;on e, two ormore unsaturated bonds- Representative. acids of this group would include oleic acid, linoleic acid, linolenic acid, the, corresponding C16 unsaturated acids, stearicacid, palmitic acid, or mixtures of, the same- For-example, amixture of fatty acids derived from a;tall.oiludistillatiorl.v Process normally comprises. approximately-40;-60%. oleic: acid and, approximately 6040% linoleic acid with small quantities of other acids. Such a mixture; has;beenfound to bewell suitedfor the application; of the present inventive concept.
  • These tall oil fatty acids may be esterified with, various alcohols prior-to the reaction with phosphorus sulfide, in; the presence of an. oxygen containing; gas, or they may merely fcrm'a mixture withthese alcohols and then be; reacted with the phosphorus sulfide in they presence of the oxygen. containing, gas.
  • the alcohols suitable for usev with the above mentioned acids are.
  • the aliphatic monohydroxy alcohols such as octadecanol, oleyl alcohol, butanol, lauryl alcohol, tridecyl alcohol, cetyl alcohol, octyl alcohol, isopropanol, etc.
  • the polyhydroxy alcohols such asethylene glycol, propylene glycol
  • the alcohols containing, aromatic or cycloaliphatic substituents such as octylphenoxyethanol, dihydroabietyl alcohol
  • the sterols such as B-sitosterol; etc.
  • EXAMPLE 1 Materials used: Grams Octadecyl ester of Acintol FA #1 529 Butanol 100 Sodium hydroxide (in 25 ml. of'water) 16 Zinc chloride (in 25 ml. of water) 28 Phosphorus sesquisulfide 40 Zinc oxide 11 Barium hydroxide octahydrate 1 59
  • the preparation of the octadecyl ester of Acintol FA #1 was as follows: ('AcintolFA #1 is a mixture of tall oil fatty acids having from about 40 to about 60% oleic acid and from about 60 to about 40% linoleic acid and small percentages, approximately 35%, of other fatty acids).
  • Octadecanol "grams (1 mole) 268 Acintol FA #1 do 298 Toluene grams 500 Para toluene sulfonic acid do 4 The above materials were refluxed for three hours while removing the water which formed with a water trap. In this manner, 18 ml. or 1 mole of water was removed. After Washing with water, then with sodium carbonate, and againwith water, the volatilemaierials were. removed under vacuum at C. to give 529 grams of the desired ester.
  • the ester, butanol, and sodium hydroxide solution were refluxedj for1 /z1-2 hours; The zinc, chloride solution .wastherradded, to the mixture and refluxed for an additional /2. hour.
  • the phosphorus sesquisulfide was added.
  • a stream of air was blown into the reaction mixture.
  • An exothermic reaction developed and white fumes were evolved.
  • the reaction temperature was controlled by the-rate. of addition of air. After about one hour, the white fumes ceased, theexothermic reaction diminished, and air was passed through, themixture for an additional /2 hour, while holding the. temperature at 130-140 C.
  • Isopropyl ester of Acintol FA #1 (prepared in same'general manner as the ester used in Example 1 from isopropyl alcohol and Acintol FA #1) 444 Butanol 100 Sodium hydroxide (in 15 ml. of water) 13 Zinc chloride (in 25 ml. of water) 23 Phosphorus scsquisulfide 33 Zinc; oxide 9 Barium hydroxide octahydrate 132 The above materials were reacted in. the same general manner as set forth in Example 1.
  • the product which was obtained was the P4S3:oxygenisopropyl ester of tall, oil fatty acid reaction product and had the following analysis:
  • EXAMPLE 3 Materials used: Grams Ethylene glycol diester of Acintol FA #1 (prepared from ethylene glycol and Acintol FA #1 in the same general manner as the ester prepared for Example 1) 534 Butanol 135 Sodium hydroxide (in ml. of water) 16 Zinc chloride (in ml. of water) 28 Phosphorus sesquisulfide Zinc oxide 11 Barium hydroxide octahydrate 160 The above materials were reacted together in the same general manner as in Example 1. The clear amber oilsoluble liquid was the Ptss-oxygen-ethylene glycol ester of tall oil fatty acids reaction product and had the following analysis:
  • EXAMPLE 5 Materials used: v Grams Oleyl stearate (prepared from oleyl alcohol and stearic acid in the same general manner as the ester prepared for Example 1) 497 Butanol. 75 Sodium hydroxide (in 15 m1. of Water) 12 Zinc chloride (in 25 ml. of water) 21 Phosphorus sesquisulfide 30 SAE #10 oil 497 Zinc oxide 8 Barium hydroxide octahydrate"; 124
  • EXAMPLE 7 Materials used: Grams Octadecanol 260 Acintol FA #1 286 Butanol I 100 Sodium hydroxide (in 20 m1. of water) 17 Zinc chloride (in 35 ml. of water) 29 Phosphorus sequisulfide 41 SAE #10 oil 546 Zinc oxide l1 Barium hydroxide octahydrate 16 4 The above materials were reacted together in the same general manner as in Example 6. The resulting dark brown oil-soluble liquid was the P4S3-oxygen reaction product of an octadecanol-tall oil fatty acid mixture and had the following analysis:
  • a lubricating oil composition comprising an organic substituted dithiophosphate and a heat stabilizer consisting of an oil soluble reaction product of phosphorus sulfide, and various esters or acid-alcohol mixtures, which composition is heat stable, is particularly resistant to sludge formation and'oxidation, is non-corrosive to alloy bearings and other metal parts under conditions of extreme service, and is free of varnish formation and ring sticking tendencies.
  • a hydrocarbon mineral-lubricating oil composition comprising a hydrocarbon mineral lubricating oil and, as. an antioxidant and anticorrosive agent having a tendency toward heat instability and the formation of sludge upon continued heating thereof at high temperatures; Gil -3.0% by weight of a dithiophosphate having the formula:
  • composition as defined in claim 1, wherein the tall oilfatty acids comprise 40-60% oleic acid and 60-40% linoleic acid.
  • composition as defined in claim 1, wherein the tall oil fatty acid comprises linoleic. acid.
  • composition as defined in claim 1, wherein the dithiophosphate is a polyvalent metal salt of dicapryldithiophosphate.
  • composition as defined in claim 1, wherein the polyvalent metal is zinc.
  • composition as defined in claim 1, wherein the polyvalent metal is barium.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Lubricants (AREA)

Description

STABILIZED LUBRICATFNG COMPOSITIONS James B. Peeso, Stamford, and Edwin 6. Hook, New
Canaan, Conn., assignors to American Qyanarnid Company, New York, N. Y., a corporation of Maine No Drawing. Application lune 24, 1952, Serial No. 295,346
Claims. (Cl. 252-32.7)
This invention relates to lubricating oil additives; to lubricating oil compositions containing the same; and particularly to those oils of the type known as crankcase oils. Although the improved lubricating oil compositions of the present invention are highly desirable for use in the crankcases of passenger automobiles, they are also especially valuable for heavy duty service in truck, bus, aeroplane, marine and diesel engines which operate for long periods of time at high temperatures.
The principal objects of the invention are to provide an improved lubricating oil of the heavy duty type which is heat stable, which is particularly resistant to sludge formation and oxidation, which is non-corrosive to alloy bearings and other metal parts under conditions of extreme service, and which is free from varnish formation and ring sticking tendencies.
When conventional lubricating oils are subjected to high operating temperatures for extended periods of time, as are encountered in heavy duty service, they show a tendency to oxidize or decompose with the formation of complex and objectionable oxidation and decomposition products. Under the high temperature conditions obtaining in the engine, these decomposition products polymerize to form lacquer-like deposits on or between the moving parts of the engine causing them to stick or to wear rapidly. Even larger quantities of polymerization products remain dispersed in the partly oxidized crankcase oil and are rapidly precipitated to form a sludge when the engine cools or when fresh oil is added to the engine. These precipitated sludges become caked on the heated metal surfaces and cut down the effective life of the engine.
In United States patent applications, Serial No. 401,960, filed July 11, 1941, and Serial No. 415,411, filled Octoer 17, 1941, now abandoned, it is disclosed that hydrocarbon lubricating oil compositions having greatly improved detergent, anti-corrosive and antisludge forming properties may be prepared by the incorporation therein of minor amounts of various organic substituteddithiophosphates.V While the lubricating oil compositions containing these organic substituted dithiophosphates are extremely resistant to sludge formation under conditions of heavy duty service, we have found that, when preparing these lubricating oil compositions from ordinary classes of lubricating oils which are not highly refined, a certain amount of sludge will form when the oil is subjected to high temperatures in heavy duty service for, long periods of time in the presence of air or oxygen. With the more highly refined oils, howeve r, such as those treated bythe solvent refining process, the
amount of sludge formed under such conditions is small.
Since it is desirable, however, to use a lower cost oil in trucks, buses, diesel engines, etc., which operate almost continuously at high temperatures, a further improvement in the heat stability of lubricating oils refined by conventional methods is desirable. Y
We have found that these organic substituted dithio phosphates whichareadded to lubricating oils refined by ordinary methods may be rendered more heat stable and more resistant to oxidation and decomposition and the lubricating oil compositions themselves may be made almost entirely resistant to sludge formation in heavy duty service for long periods of time at elevated temperatures by the incorporation therein of minor amounts of oil soluble reaction products of phosphorus sulfides and a member of the group consisting of either esters of tall oil fatty acids and alcohols or mixtures of such acids and alcohols, which reaction may be promoted by the presence of a free oxygen-containing gas.
The various dithiophosphates which we have found useful in improving lubricating oils and which may be employed to advantage with the oil-soluble reaction products of phosphorus sulfides are those having the general formula:
R-O s M I: 1
P R0/ s in which R is a member of the group consisting of aryl, alkyl, aralkyl, cycloalkyl, aryloxyalkyl, acylaryl and alkoxyaryl radicals; M is hydrogen or a salt-forming radical; and n is the valence of M. More specifically, compounds of this class include the dialkyl dithiophosphates such as dibutyl dithiophosphate, dihexyl dithiophosphate, di n-octyl dithiophosphate, dicapryl dithiophosphate, dilauryl dithiophosphate, dioctadecyl dithiophosphate, etc. We prefer to use those dialkyl dithiophosphates in which the alkyl group has from 5 to 30 carbon atoms since the longer alkyl chains tend to increase the solubility of the dithiophosphates in lubricating oils. The diaryl dithiophosphates and the diaryl dithiophosphates in which the aryl group bears an alkyl, alkoxy or cycloaliphatic group are also useful such as for example diphenyl di thiophosphate, di-(2,4-diamyl phenyl) dithiophosphate, dikeryl diphenyl dithiophosphate (a product obtained by treating chlorinated kerosene with a phenol in the presence of aluminum chloride and then reacting with P235) and the various di-(wax substituted diaryl) dithiophosphates as described in detail in applicationSerial No. 415,411, filed October 17, 1941, now abandoned. We also prefer the alkyl group in the alkaryl radical to have 5 to 50 carbon atoms so that the compounds are more easily oil-soluble. We may also employ the dicycloa1iphatic dithiophosphates such as those prepared by reacting cyclopentanol, cyclohexanol, cycloheptanol, and methyl, ethyl, propyl and amyl substituted cyclopentanol, cyclohexanol and cycloheptanol, etc. with P255. The di aryloxyalkyl dithiophosphates such as di-(2,4-diamylphenoxyethyl) dithiophosphate, the diacylaryl dithiophosphates such as di-(lauroylphenyl) dithiophosphate and the dialkoxyaryl dithiophosphates may also be added to lubricating oils to improve the oxidation stability of the oil.
We prefer to employ these various organic substituted dithiophosphates in'the form of their metal salts, preferably the alkaline earth metal salts. Among the various metal salts which may be employed are those of the salt-forming radicals nickel, aluminum, cadmium, tin, zinc, magnesium, calcium, strontium, barium and others.
The various organic-substituted dithiophosphates described above are employed by us in our improved lubricating oil compositions, preferably in amounts ranging from 0.1 to 3% or more by weight and normally at a concentration of approximately 0.6%. Smaller amounts, 0.05 to 2.0% or more, of the heat stabilizer, that is, the oil soluble reaction products of phosphorus sulfides and oxygenwiththetallpit fatty acid-alcohol esters or mixtures may be employed with the dithiophosphates to enhance the heat stability thereof. The greater the tendencyof T the 1 dithiophosphates: to; break down under: high temperatures, or the; higher its; concentration in the oil composition, then, the, more heat stabilizer should be employed; The-amount of both; of these substituents in the oil. will also depend; to some extent upon; the purpose for which the oil isgintendedr For example, an oil intended'for extremely: heavy duty service should contain more of both the dithiophosphate; and the phosphorus sulfide. reaction product as comparedwith the amounts required by an oil intended for, ordinary usage.
The general chemical reactionsand; the. preparation and nature of'the .oil soluble. reaction productsof phosphorus sulfides such as those ofphosphorussesquisulfide, phosphorus pentasulfide, etc., involvingthe, use of oxygen, are set forth in United; StatesP'atents-2,483,571, issued October 4, 1949, and 2,375,060, issued May.- 1, 1945, and reference thereto is incorporated herein.
The invention is particularly applicable to compositions comprising the organic substituted dithiophosphates, previously described, and to those reaction products of phosphorus sesquisulfide (P453); and the tall oil fatty acid-alcohol esters or mixtures.
As used herein, the term tall oil fatty acids is intended to refer to and include those fatty acids normally found in tall oil as well as those fatty acids having very similar properties, asrequired for the specific purposes herein referred. to. For the purposes of this invention, these acidsv contain 16 to 18 carbon atoms and may contain;on e, two ormore unsaturated bonds- Representative. acids of this group would include oleic acid, linoleic acid, linolenic acid, the, corresponding C16 unsaturated acids, stearicacid, palmitic acid, or mixtures of, the same- For-example, amixture of fatty acids derived from a;tall.oiludistillatiorl.v Process normally comprises. approximately-40;-60%. oleic: acid and, approximately 6040% linoleic acid with small quantities of other acids. Such a mixture; has;beenfound to bewell suitedfor the application; of the present inventive concept.
These tall oil fatty acids may be esterified with, various alcohols prior-to the reaction with phosphorus sulfide, in; the presence of an. oxygen containing; gas, or they may merely fcrm'a mixture withthese alcohols and then be; reacted with the phosphorus sulfide in they presence of the oxygen. containing, gas.
Among the alcohols suitable for usev with the above mentioned acids, either for esterification purposes or merely to form mixtures therewith, are. the aliphatic monohydroxy alcohols such as octadecanol, oleyl alcohol, butanol, lauryl alcohol, tridecyl alcohol, cetyl alcohol, octyl alcohol, isopropanol, etc.; the polyhydroxy alcohols such asethylene glycol, propylene glycol; the alcohols containing, aromatic or cycloaliphatic substituents such as octylphenoxyethanol, dihydroabietyl alcohol; the sterols such as B-sitosterol; etc.
The preparation of the oil soluble phosphorus sulfide reaction products of these esters or mixtures will be further described in greater detail by the following specificexamples, It should beunderstood, however, that, although these examples may set forth in particular dc tail some of the more specific featuresof the-invention, such is not to be construed as limitative thereof.
EXAMPLE 1 Materials used: Grams Octadecyl ester of Acintol FA #1 529 Butanol 100 Sodium hydroxide (in 25 ml. of'water) 16 Zinc chloride (in 25 ml. of water) 28 Phosphorus sesquisulfide 40 Zinc oxide 11 Barium hydroxide octahydrate 1 59 The preparation of the octadecyl ester of Acintol FA #1 was as follows: ('AcintolFA #1 is a mixture of tall oil fatty acids having from about 40 to about 60% oleic acid and from about 60 to about 40% linoleic acid and small percentages, approximately 35%, of other fatty acids).
Materials used:
Octadecanol "grams (1 mole) 268 Acintol FA #1 do 298 Toluene grams 500 Para toluene sulfonic acid do 4 The above materials were refluxed for three hours while removing the water which formed with a water trap. In this manner, 18 ml. or 1 mole of water was removed. After Washing with water, then with sodium carbonate, and againwith water, the volatilemaierials were. removed under vacuum at C. to give 529 grams of the desired ester.
The ester, butanol, and sodium hydroxide solution were refluxedj for1 /z1-2 hours; The zinc, chloride solution .wastherradded, to the mixture and refluxed for an additional /2. hour. After removing the, water andbutanol under. vacuumatlOO" C. the phosphorus sesquisulfide was added. Afterv heating this reaction mixture to 130 C.., a stream of air was blown into the reaction mixture. An exothermic reaction developed and white fumes were evolved. The reaction temperature was controlled by the-rate. of addition of air. After about one hour, the white fumes ceased, theexothermic reaction diminished, and air was passed through, themixture for an additional /2 hour, while holding the. temperature at 130-140 C. At this point, the. zincoxide and 10 ml. of water. were added andthe mixture; heated. for. about A. ofan hour at 90.10.0, C. The bariumyoctahydrate was thenadded and the reactiongradually heated. to 0, followed byblowing: with. air. at this temperature to remove the water. After the removal of, water was complete, 55 grams of Hy-flo. were, added and, the product filtered through a pre-coated; steam-jacketed vacuum filter. The resulting amber, oil-soluble liquid was the Pisa-oxygenoctadecylester oftalloil fatty acids reaction product and had the following analysis:
Isopropyl ester" of Acintol FA #1 (prepared in same'general manner as the ester used in Example 1 from isopropyl alcohol and Acintol FA #1) 444 Butanol 100 Sodium hydroxide (in 15 ml. of water) 13 Zinc chloride (in 25 ml. of water) 23 Phosphorus scsquisulfide 33 Zinc; oxide 9 Barium hydroxide octahydrate 132 The above materials were reacted in. the same general manner as set forth in Example 1.
The product which was obtained was the P4S3:oxygenisopropyl ester of tall, oil fatty acid reaction product and had the following analysis:
Percent Barium 6.4
Zinc 1.71 Phosphorus. 2.1 Sulfur" 1.9
EXAMPLE 3 Materials used: Grams Ethylene glycol diester of Acintol FA #1 (prepared from ethylene glycol and Acintol FA #1 in the same general manner as the ester prepared for Example 1) 534 Butanol 135 Sodium hydroxide (in ml. of water) 16 Zinc chloride (in ml. of water) 28 Phosphorus sesquisulfide Zinc oxide 11 Barium hydroxide octahydrate 160 The above materials were reacted together in the same general manner as in Example 1. The clear amber oilsoluble liquid was the Ptss-oxygen-ethylene glycol ester of tall oil fatty acids reaction product and had the following analysis:
Lauryl oleate (prepared from lauryl alcohol and oleic acid in the same general manner as the ester prepared for Example 1) 430 Butanol 100 Sodium hydroxide (in 20 ml. of water) 13 Zinc chloride (in 30 ml. of water) 23 Phosphorus sesquisulfide 33 Zinc oxide I 9 Barium hydroxide octahydrate 132 The above materials were reacted in the same general manner as in Example 1. The resulting oil soluble amber liquid was the Psss-oxygen-lauryl oleate reaction product and had the following analysis:
Percent Barium 9.14 Zinc 2.45 Phosphorus 2.53 Sulfur 1.48
EXAMPLE 5 Materials used: v Grams Oleyl stearate (prepared from oleyl alcohol and stearic acid in the same general manner as the ester prepared for Example 1) 497 Butanol. 75 Sodium hydroxide (in 15 m1. of Water) 12 Zinc chloride (in 25 ml. of water) 21 Phosphorus sesquisulfide 30 SAE #10 oil 497 Zinc oxide 8 Barium hydroxide octahydrate"; 124
v Percent Barium 4.7 Zinc 1.1 Phosphorus 1.2 Sulfur 0.8
6 EXAMPLE 6 Materials used:
Octadecanol grams (1 mole)" 268 Oleic acid do.. 282 Butanol grams Sodium hydroxide (in 20 ml. water) ..do.... 17 Zinc ch1oride (in 35 ml. of water) do 29 Phosphorus sesquisulfide do 41' Zinc nxide V q I do. 11 Barium hydroxide octahydrate do 550 SAE #10 oil do 550 The octadecanol, oleic acid, butanol and sodium hydroxide solution were refluxed for about one hour. The zinc chloride solution was then added and the reaction mixture heated to reflux for an additional /2 hour. The water and butanol were removed by heating to -120 C. under vacuum. The phosphorus sequisulfide was then added and after heating the reaction mixture to 135 C., a stream of air was blown into the reaction. The exotherm which developed was maintained at -140 C. by regulating the rate of addition of the air. At the conclusion of the exotherm, air blowing was continued for an additional A; hour While maintaining the temperature at 130-140 C. The oil, zinc oxide, and 11 ml. of water were added to this mixture, which was then heated to 100 C. for about one hour. The barium hydroxide octahydrate was then added and the temperature slowly raised to 120 C. The reaction was maintained at 120 C. while air was blown through the reaction mixture to remove the water. After the removal of water was complete, 75 grams of Hy-flo were added and the reaction mixture filtered through a steam-heated, precoated vacuum filter. The resulting dark amber oilsoluble liquid was the Pass-oxygen reaction product of an octadecanol-oleic acid mixture and had the following analysis:
- Percent Barium 4.97
Zinc 1.88
Phosphorus 1.5
Sulfur 0.9
EXAMPLE 7 Materials used: Grams Octadecanol 260 Acintol FA #1 286 Butanol I 100 Sodium hydroxide (in 20 m1. of water) 17 Zinc chloride (in 35 ml. of water) 29 Phosphorus sequisulfide 41 SAE #10 oil 546 Zinc oxide l1 Barium hydroxide octahydrate 16 4 The above materials were reacted together in the same general manner as in Example 6. The resulting dark brown oil-soluble liquid was the P4S3-oxygen reaction product of an octadecanol-tall oil fatty acid mixture and had the following analysis:
The above materials were reacted together in the same Percent Barium 9.6 Zinc" 3.8 Phosphorus 2.9 Sulfur 1.0
The excellent compatibility and solubility of these oil soluble reaction products of phosphorus sulfides in hydrocarbon lubricating oil compositions containing the dithiophosphates leads to another important advantage, namely, the'ease with which these compoundsare blended with the oil compositions; This step is further simplified by our practice of very simply dissolving them in the lubricating oils upto the extent of 50% or higher concentrations for storage and" shipping; purposes. In this'way the blender of the ultimate composition need only pour the additive composition into the stock lubricating oil with suitable stirring in order to obtain the desired lubricant.
The invention will be further described in more specifi'cdetail by reference'to and discussion of the following results obtained from heat stability tests which were run on various oil compositions selected to best illustrate the inventive concept.
These tests consisted of the following procedure: a 200 gram sample of the selected oil composition was placed in a 400 ml. short form, Pyrex beaker and set in a partially ventilated oven which was maintained at 250 F.; the test sample was observed at regular intervals during a 125 hour period. After 125 hours, the sample was removed from the oven and allowed to stand and cool for 24 hours. The sample was then observed for hazing, precipitation and/orgelling; Precipitating and/or gelling were considered as failures; a small amount of precipitationor sedimentation, however, could be tolerated; hazing, although not a crucial factor, was an indication of heat instability.
Thefollowing results werenoted onblends using a solvent refined Mid-Continent base oil, S. A. E.
slight sediment. Opaque, black. Clear, some darkening,
sll]g)ht precipitate.
From aconsideration of Table 1, it will be realized that the oil composition, without any zinc dihexyldithiophosphate inhibitor and without any Risa-oxygen reaction product of octadecanol-fatty acid ester remained clear, although there was some darkening accompanied by the formation-ofa slight sediment. Thesaddition'of 0.6% zinc dihexyldithiophosphate, alone, when tested, as above,
rendered the oil blend; opaque and. black as an indication of the relative heat instability thereof. However, it is to be. notedthat the addition of as littleas 0.05 of the heatstabilizer stabilized the. blend sufliciently so that it did not become opaque or black upon exposure to high temperatures for the test period. and was classified as clear and merely containing a small precipitate.
Similar results are to be noted from a consideration of Table 2, wherein again a small amount (0.05%) of a, heat stabilizer comprising aphosphorus sulfide reaction product of a mixture of'octadecanol and tall oil fatty acids'was'sufiicientto' overcome the-heat instability of the zinc dihexyl'dithiophosphate; Increased amounts of the heat stabilizer correspondingly improved the appearance of. the oil blend and its-heat stability.
From the foregoing, it will be seen that we have pro.- vided a lubricating oil composition comprising an organic substituted dithiophosphate and a heat stabilizer consisting of an oil soluble reaction product of phosphorus sulfide, and various esters or acid-alcohol mixtures, which composition is heat stable, is particularly resistant to sludge formation and'oxidation, is non-corrosive to alloy bearings and other metal parts under conditions of extreme service, and is free of varnish formation and ring sticking tendencies.
Although we have described but a few specific preparations of such reaction .productsof phosphorus sulfides and have: referred briefly to the results of specific tests of such compounds. in lubricating oil, compositions containing dithiophosphates, we. consider the. same not to be limited thereto. It is understoorlthat suitable. changes, variations and modifications may be made without departing from the spirit and scope. of the invention.
What we claim is:
1. A hydrocarbon mineral-lubricating oil composition comprising a hydrocarbon mineral lubricating oil and, as. an antioxidant and anticorrosive agent having a tendency toward heat instability and the formation of sludge upon continued heating thereof at high temperatures; Gil -3.0% by weight of a dithiophosphate having the formula:
R-O s in which R is an alkyl radical containing from 5 to 30 carbon atoms; M is a polyvalent metal from the group consisting of nickel, aluminum, cadmium, tin, zinc, magnesium, calcium, strontium and barium; and n is: the valence of M said oil also containing as a heat stabilizer for said dithiophosphate 0.052% by weight of an oil soluble, neutralized reaction product of a phosphorus sulfideand a member of the group consisting of tall oil fatty acids-alcohol esters and tall oil. fatty acid-alcohol mixtures.
2. The composition as defined in claim 1, wherein the tall oil fatty acidscomprise unsaturated monocarboxylic acids having 16' to18 carbon atoms.
3. The composition as defined in claim 1, wherein the tall oilfatty acids comprise 40-60% oleic acid and 60-40% linoleic acid.
4. The composition as definedin claim 1, wherein the tall oil fattyacid. comprises oleic. acid;
5. The composition as defined in claim 1, wherein the tall oil fatty acid comprises linoleic. acid.
6.. The. composition as defined in claim 1, wherein the alcohol .is. octadecanol.
7. The-composition as: defined in claim 1, wherein the alcohol is..ethylene, glycol.
8. The composition as defined in claim 1, wherein the phosphorus sulfide is phosphorus sesquisulfide.
9. The composition as defined in claim 1, wherein the dithiophosphateis" a polyva-lent metal salt of dihexyldithiophosphate:
10. The" composition as" defined in claim 1, wherein 9 the dithiophosphate is a polyvalent metal salt of dilauryldithiophosphate.
11. The composition as defined in claim 1, wherein the dithiophosphate is a polyvalent metal salt of dicapryldithiophosphate.
12. The composition as defined in claim 1, wherein the polyvalent metal is zinc.
13. The composition as defined in claim 1, wherein the polyvalent metal is barium.
14. The composition as defined in claim 1 wherein the antioxidant and anticorrosive agent is zinc dihexyldithiophosphate and the heat stabilizer is a neutralized Pisa-oxygen reaction product of octadecanol-tall oil fatty acid ester.
5 acid mixture.
References Cited in the file of this patent UNITED STATES PATENTS 10 2,252,984 Rutherford et a1 Aug. 19, 1941 2,345,156 Roberts Mar. 28, 1944 2,483,571 Brennan et a1. Oct. 4, 1949

Claims (1)

1. A HYDROCARBON MINERAL LUBRICATING OIL COMPOSITION COMPRISING A HYDROCARBON MINERAL LUBRICATING OIL AND AS AN ANTIOXIDANT AND ANTICORROSIVE AGENT HAVING A TENDENCY TOWARD HEAT INSTABILITY AND THE FORMATION OF SLUDGE UPON CONTINUED HEATING THEREOF AT HIGH TEMPERATURES, 0.1-3.0% BY WEIGHT OF A DITHIOPHOSPHATE HAVING THE FORMULA:
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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1096528B (en) * 1959-08-03 1961-01-05 Standard Oil Co Hydrocarbon lubricating oil
US2990297A (en) * 1959-12-21 1961-06-27 California Research Corp Flameroofing of wood and article
US3159578A (en) * 1960-02-26 1964-12-01 Shell Oil Co Organic functional fluids and polymeric amine salt additives therefor
US3211648A (en) * 1963-03-11 1965-10-12 Lubrizol Corp Lubricants containing metal hydrocarbon-oxy-alkyl and hydrocarbon-oxyaryl phosphorothioate-epoxide reaction products
US3213022A (en) * 1963-03-11 1965-10-19 Lubrizol Corp Lubricants containing metal phosphorodithioate-epoxide reaction products
US3362907A (en) * 1964-03-06 1968-01-09 Australia Res Lab Liquid developer with sharp cut-off response
US3375197A (en) * 1964-07-30 1968-03-26 Gen Electric Refrigeration system lubrication
DE2108780A1 (en) * 1971-02-24 1972-10-26 Optimol-Ölwerke GmbH, 8000 München Lubricant or lubricant concentrate
US4822505A (en) * 1987-07-31 1989-04-18 Exxon Research And Engineering Company Load-carrying grease

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2252984A (en) * 1939-05-06 1941-08-19 Standard Oil Co Compounded hydrocarbon oil
US2345156A (en) * 1941-01-15 1944-03-28 Texas Co Lubricating oil
US2483571A (en) * 1945-12-20 1949-10-04 Pure Oil Co Reaction of organic substances with phosphorous sesquisulfide

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2252984A (en) * 1939-05-06 1941-08-19 Standard Oil Co Compounded hydrocarbon oil
US2345156A (en) * 1941-01-15 1944-03-28 Texas Co Lubricating oil
US2483571A (en) * 1945-12-20 1949-10-04 Pure Oil Co Reaction of organic substances with phosphorous sesquisulfide

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1096528B (en) * 1959-08-03 1961-01-05 Standard Oil Co Hydrocarbon lubricating oil
US2990297A (en) * 1959-12-21 1961-06-27 California Research Corp Flameroofing of wood and article
US3159578A (en) * 1960-02-26 1964-12-01 Shell Oil Co Organic functional fluids and polymeric amine salt additives therefor
US3211648A (en) * 1963-03-11 1965-10-12 Lubrizol Corp Lubricants containing metal hydrocarbon-oxy-alkyl and hydrocarbon-oxyaryl phosphorothioate-epoxide reaction products
US3213022A (en) * 1963-03-11 1965-10-19 Lubrizol Corp Lubricants containing metal phosphorodithioate-epoxide reaction products
US3362907A (en) * 1964-03-06 1968-01-09 Australia Res Lab Liquid developer with sharp cut-off response
US3375197A (en) * 1964-07-30 1968-03-26 Gen Electric Refrigeration system lubrication
DE2108780A1 (en) * 1971-02-24 1972-10-26 Optimol-Ölwerke GmbH, 8000 München Lubricant or lubricant concentrate
US4822505A (en) * 1987-07-31 1989-04-18 Exxon Research And Engineering Company Load-carrying grease

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