US2419325A - Lubricating composition - Google Patents

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US2419325A
US2419325A US628382A US62838245A US2419325A US 2419325 A US2419325 A US 2419325A US 628382 A US628382 A US 628382A US 62838245 A US62838245 A US 62838245A US 2419325 A US2419325 A US 2419325A
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phosphorus
pentasulphide
lubricating oil
reaction
reaction product
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John M Musselman
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Standard Oil Co
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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
    • C10M1/00Liquid compositions essentially based on mineral lubricating oils or fatty oils; Their use as lubricants
    • C10M1/08Liquid compositions essentially based on mineral lubricating oils or fatty oils; Their use as lubricants with additives
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/26Organic compounds containing phosphorus
    • C10L1/2691Compounds of uncertain formula; reaction of organic compounds (hydrocarbons acids, esters) with Px Sy, Px Sy Halz or sulfur and phosphorus containing compounds
    • 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

Definitions

  • the invention comprises the features hereinafter fully described, and particularly pointed out in the claims, the following description setting forth in detail certain illustrative embodiments of the invention, these being indicative however, of but a few of the various ways in which the principle of the invention may be employed.
  • Paramn wax is oxidized under pressure to yield in combination with the oxidation product.
  • the nature of the phosphorus in the reaction product is not known, but it does not appear to be present as a thiophosphate because the phosphorus content is materially-reduced upon reaction with an alkali in the manner described subsequently.
  • the reaction is carried out simply by mixing the reaction ingredients in theproportions stated at the temperature stated.
  • the pentasulphide is added in increments to a kettle containing the oxygenated hydrocarbon and the reaction mass is stirred. It is completed in 1 to 4 hours when the exothermic reaction subsides.
  • this is separated into saponiflable and non-saponifiable fractions, and the further procedure'is carried out with the saponifiable fraction, although where preferred the non-saponifiable diluent material may be left in.
  • Phosphorus 3o pentasulphide is reacted upon the oxidation product by heating to a temperature above thiophosphate formation, i. e., at least about 275 F. and preferably to around 300 F. An exothermic reaction takes place and it is generally not necessary to exceed a temperature above 425 F. It is particularly desirableto employ such an amount of phosphorus pentasulphide as requisite to supplant the oxygen of the compound with sulphur.
  • the amount of the phosphorus pentasulphide should be such that the sulphur therein is stoichiometrically sufiicient to replace all of the oxygen in the oxygenated hydrocarbon.
  • the amount of the sulphide to be used can be calculated readily, depending on the oxygenated hydrocarbon and its oxygen content. About 20 percent of phosphorus pentasulphide is satisfactory for an oxidized paraflin wax having about 7% oxygen. The amount generally falls within the range of 14 to per cent for oxygenated 5 By next subjecting the material to air-blowing. residual odors may be eliminated.
  • the material may be converted into a metal compound, and for instance from the saponification number of the material the required amount of lime for saponification is indicated and may be added. It is advisable that the product so formed be around 9-11 pH value.
  • the product has outstanding lubricating and stabilizing properties and ability to maintain metal surfaces in clean polished condition. If desired, only a part of the product of the reaction. product of the pentasulphide with the oxygenated hydrocarbon may be converted into the metal compound so as to form a mixture of the initial reaction product and the metal compound thereof.
  • the initial reaction product of the phosphorus sulphide and the oxygenated hydrocarbon, or the metal compound formed therefrom may be in-' corporated in a mineral lubricating oil in various amounts to improve the properties of the lubricating oil depending upon the particular purpose for which the oil is to be used. In general an amount of at least 0.1 per cent will be used. Inasmuch as the reaction products are lubricants themselves there is no upper limit but in general the amount will not exceed 10 per cent.
  • oxidized polymers of butylene or isobutylene and other olefins, naphthenic acids, or other oxygenated hydrocarbons derived by oxidizing petroleum hydrocarbons and containing oxygen capable of being displaced with sulphur by reaction with a sulphide of phosphorus may be carried out in the liquid or vapor phase, as in the case of the oxidation of paraflin wax discussed earlier, and in a manner well known in the art.
  • oxidation products used in accordance with the inventions are liquids or solids, preferably having a boiling point above the temperature of the reaction with the sulphide so as to avoid the use of pressure during the reaction, and comprise mixtures of acids, alcohols, esters, aldehydes, ketones, lactones and similar oxygen containing hydrocarbon compounds. These mixtures are very complex and possess unique properties which are not inherent in any sing e constituent thereof.
  • the oxidation product may be separated into a aponiflable fraction as in the case of oxidized paraflin wax, or the non-saponifiable portion may be left in.
  • the neutralization or saponification of the product from the reaction of phosphorus pentasulphide and oxidized petroleum may be eflected also by other bases, such as aluminum, tin, zinc, lead, magnesium, barium, potassium, sodium, ammonia, amines, or a mixture of two or more of them, such as calcium and barium, aluminum and calcium, etc.
  • the testing engine was an Ethyl Gasoline Corporation test engine and it was operated in accordance with Procedure IV, namely, running at 1200 revolutions per minute, with sump temperature 300 F., and jacket temperature 212 F., and an iron catalyst in the amount of 0.1%, F203 as iron naphthenate.
  • the fuel was a high octane gasoline containing 3 cc. of lead tetraethyl per gallon.
  • the operating re- 4 metal compound the following example is also included:
  • reaction products of the invention are to be distinguished from reaction products obtained by reacting elemental sulphur and compounds yielding sulphur, such as sulphur halides, with oxygen containing compounds, since in such a reaction the oxygen is not replaced in the manner in which it is in accordance with the invention.
  • the reaction products of the invention are also to be distinguished from the use of other sulphides in smaller amounts less than that in which the sulphur of the sulphide is the stoichiometric equivalent of the oxygen to be replaced. All such reaction products are inferior to the reaction product of the invention and not the equivalent thereof.
  • a new lubricating oil composition of matter comprising a major portion of a lubricating oil and an amount of an additive sufficient to improve the stability of the lubricating oil, said additive comprising the metal compound of the reaction product of an oxygenated petroleum hydrocarbon boiling above the hereinafter named reaction temperature and an amount of phosphorus pentasulphide within the range of 14 to 30% and at least stoichiometrically sufficient to supplant the oxygen of the oxygenated petroleum hydrocarbon with sulphur, reacted at a temperature within the range of 275 to 425 F. to form a reaction product separable from a sludge sults beingcomprising the major part of the phosphorus in Same plus 3% San. plus 3% Same plus 37 S. A.
  • a new lubricating oil composition of matter comprising a major portion of a lubricating oil and an amount of an additive sufficient to improve the stability of the lubricating oil, said additive comprising the alkaline earth metal compound of the reaction product of an oxygenated petroleum hydrocarbon boiling above the hereinreaction product before its conversion into a 7 after named reaction temperature and an amount of phosphorus pentasulphide within the range of 14 to 80% and at least stoichiometrically suilicient to supplant the oxygen of the oxygenated petroleum hydrocarbon with sulphur. reacted at a temperature within the range oi 275 to 425 F. to form a reaction product separable from a sludge comprising the major part of the phosphorus in the pentasulphide, and subsequently converted into said alkaline earth metal compound.
  • a new lubricating oil composition of matter comprising a major portion of a lubricating oil and an amount of an additive suflicient to improve the stability of the lubricating oil, said additive comprising the metal compound reaction product of an oxidized parafiln wax and an amount of phosphorus pentasulphide within the range of 14 to 30% and at least stoichiometrically suflicient to supplant the oxygen of the oxidized parai'fln wax with sulphur, reacted at a temperature within the range of 275 to 425 F. to form a reaction product separable from a. sludge comprising the major part of the phosphorus in the pentasulphide, and subsequently converted into said metal compound.
  • a new lubricating oil composition of matter comprising a major portion of a lubricating oil and an amount of an additive sufiicient to improve the stability of the lubricating oil, said additive comprising the alkaline earth metal compound of the reaction product of an oxidized paraflln wax and about 20% phosphorus pentasulphide reacted at a temperature of about 300 F., said amount of phosphorus pentasulphide and said temperature resulting in a reaction product separable from a sludge comprising the major part of the phosphorus in the pentasulphide, and subsequently converted into the alkaline earth metal compound.
  • a new lubricating oil composition of matter comprising a, major portion of a lubricating oil and an amount of an additive suflicient to improve the stability of the lubricating oil, said adsupplant the oxygen of the oxidized paraflln was with sulphur, reacted at a temperature within the range of 275 to 425 F. to form a reaction product separable from a sludge comprising the mtaijor part of the phosphorus in the pentasulp de.
  • a new lubricating oil composition of matter comprising a major portion of a lubricating oil and an amount of an additive sufficient to improve the stability of the lubricating oil, said additive comprising the reaction product of an oxidized parafiin wax and about phosphorus pentasulphide, reacted at a temperature of about 300 F., said amount of phosphorus pentasulphide and said temperature resulting in a reaction product separable from a sludge comprising the major part of the phosphorus in the pentasulphide.
  • a new lubricating oil composition of matter comprising a major portion of a lubricating oil and an amount of an additive suiilcient to improve the stability of the lubricating oil, said additive comprising the reaction product of an oxygenated petroleum hydrocarbon boiling above the hereinafter named reaction temperature and an amount of phosphorus pentasulphide within the range of 14 to 30% and at least stoichiometrically suflicient to supplant the oxygen of the oxygenated petroleum hydrocarbon with sulphur, reacted at a temperature within the range of 275 to 425 F. to form a reaction product separable from a sludge comprising the major part of the phosphorus in the pentasulphide.
  • a new lubricating oil composition of matter comprising a major portion of a lubricating oil and an amount of an additive sufiicient to-improve the stability of the lubricating oil, said additive comprising the reaction product of an oxidized paraffln wax and an amount of the phosphorus pentasulphide within the range 01 14 to 30% and at least stoichiometrically suflicient to 9.
  • An additive effective in small amounts for improving the stability of a lubricating oil comprising the metal compound of the reaction product of an oxygenated petroleum hydrocarbon boiling .above the hereinafter named reaction temperature and an amount of phosphorus pentasulphide Within the range of 14 to 30%, and at least stoichiometrically suflicient to supplant the oxygen of the oxygenated petroleum hydrocarbon with sulphur, reacted at a temperature within the range of 275 to 425 F. to form a reaction product separable from a sludge comprising the major part of the phosphorus in the pentasulphide, and subsequently converted into said metal compound.
  • An additive efiective for improving the stability of a lubricating oil comprising the calcium compound of the reaction product of an oxidized parafiin Wax and about 20% phosphorus pentasulphide reacted at a temperature of about 300 F., said amount of phosphorus pentasulphide and said temperature resulting in a reaction product separable from a sludge comprising the major part of the phosphorus in the pentasulphide, and subsequently converted into said calcium compound.
  • An additive efiective for improving the stability of a lubricating oil comprising the reaction product of an oxygenated petroleum hydrocarbon boiling above the hereinafter named reaction temperature and an amount of phosphorus pentasulphide within the range of 14 to 30% and at least stoichiometrically suflicient to supplant the oxygen of the oxygenated petroleum hydrocarbon with sulphur, reacted at a temperature within the range of 275 to 425 F. to form a reaction product separable from a sludge comprising the major part of the phosphorus in the pentasulphide.
  • a new composition of matter suitable for use as an addition agent to improve the characted at a temperature within the range of 275 to 425 F. and with stolchiometrically sufllcient phosphorus pentasulphide to supplant oxygen of the oxygenated petroleum hydrocarbon with sulphur and to separate the major part of the 5 phosphorus from the reaction product.

Description

Faienteei Apr. 22, 1947 LUBRICATING COMPOSITION John M. Musselman, South Euclid, Ohio, assignor to The Standard Oil Company, Cleveland, Ohio, a corporation of Ohio No Drawing. Application November 13, 1945, Serial No. 628,382
13 Claims. (Cl. 252-32-7) It has been suggested to add oxidized petroleum acids to lubricating oil in an effort to increase the oiliness. While afiording some result in this direction, the oxidation acids have had the very serious drawback of greatly accelerating the breakdown of the oil, particularly if elevated temperatures were, involved. In accordance with the present invention it now becomes possible to at tain the desired advantages of oxidized petroleum material with in addition a remarkable stability and other properties not heretofore regarded as possible with such starting material.
To the accomplishment of the foregoing and related ends, the invention, then, comprises the features hereinafter fully described, and particularly pointed out in the claims, the following description setting forth in detail certain illustrative embodiments of the invention, these being indicative however, of but a few of the various ways in which the principle of the invention may be employed.
The invention will be best understood by reference to an illustrative example: 7
Paramn wax is oxidized under pressure to yield in combination with the oxidation product. The
nature of the phosphorus in the reaction product is not known, but it does not appear to be present as a thiophosphate because the phosphorus content is materially-reduced upon reaction with an alkali in the manner described subsequently.
The reaction is carried out simply by mixing the reaction ingredients in theproportions stated at the temperature stated. Preferably the pentasulphide is added in increments to a kettle containing the oxygenated hydrocarbon and the reaction mass is stirred. It is completed in 1 to 4 hours when the exothermic reaction subsides.
an oxidation product comprising hydroxy acids.
Desirably, this is separated into saponiflable and non-saponifiable fractions, and the further procedure'is carried out with the saponifiable fraction, although where preferred the non-saponifiable diluent material may be left in. Phosphorus 3o pentasulphide is reacted upon the oxidation product by heating to a temperature above thiophosphate formation, i. e., at least about 275 F. and preferably to around 300 F. An exothermic reaction takes place and it is generally not necessary to exceed a temperature above 425 F. It is particularly desirableto employ such an amount of phosphorus pentasulphide as requisite to supplant the oxygen of the compound with sulphur. In other words the amount of the phosphorus pentasulphide should be such that the sulphur therein is stoichiometrically sufiicient to replace all of the oxygen in the oxygenated hydrocarbon. The amount of the sulphide to be usedcan be calculated readily, depending on the oxygenated hydrocarbon and its oxygen content. About 20 percent of phosphorus pentasulphide is satisfactory for an oxidized paraflin wax having about 7% oxygen. The amount generally falls within the range of 14 to per cent for oxygenated 5 By next subjecting the material to air-blowing. residual odors may be eliminated.
Then, if desired, the material may be converted into a metal compound, and for instance from the saponification number of the material the required amount of lime for saponification is indicated and may be added. It is advisable that the product so formed be around 9-11 pH value. The product has outstanding lubricating and stabilizing properties and ability to maintain metal surfaces in clean polished condition. If desired, only a part of the product of the reaction. product of the pentasulphide with the oxygenated hydrocarbon may be converted into the metal compound so as to form a mixture of the initial reaction product and the metal compound thereof.
The initial reaction product of the phosphorus sulphide and the oxygenated hydrocarbon, or the metal compound formed therefrom may be in-' corporated in a mineral lubricating oil in various amounts to improve the properties of the lubricating oil depending upon the particular purpose for which the oil is to be used. In general an amount of at least 0.1 per cent will be used. Inasmuch as the reaction products are lubricants themselves there is no upper limit but in general the amount will not exceed 10 per cent.
thereof, oxidized polymers of butylene or isobutylene and other olefins, naphthenic acids, or other oxygenated hydrocarbons derived by oxidizing petroleum hydrocarbons and containing oxygen capable of being displaced with sulphur by reaction with a sulphide of phosphorus. The oxidation may be carried out in the liquid or vapor phase, as in the case of the oxidation of paraflin wax discussed earlier, and in a manner well known in the art. (See chapter 36 of Ellis: The Chemistry of Petroleum Derivatives.) These oxidation products used in accordance with the inventions are liquids or solids, preferably having a boiling point above the temperature of the reaction with the sulphide so as to avoid the use of pressure during the reaction, and comprise mixtures of acids, alcohols, esters, aldehydes, ketones, lactones and similar oxygen containing hydrocarbon compounds. These mixtures are very complex and possess unique properties which are not inherent in any sing e constituent thereof. The oxidation product may be separated into a aponiflable fraction as in the case of oxidized paraflin wax, or the non-saponifiable portion may be left in.
The neutralization or saponification of the product from the reaction of phosphorus pentasulphide and oxidized petroleum may be eflected also by other bases, such as aluminum, tin, zinc, lead, magnesium, barium, potassium, sodium, ammonia, amines, or a mixture of two or more of them, such as calcium and barium, aluminum and calcium, etc.
As illustrating the characteristics of the present compounds, comparisons in operating results with an untreated oil, an oil containing parafiin oxidation acid, an oil containing the calcium salt of paraffin oxidation acid, and an oil containing a compound in accordance with the present invention, may be noted: The testing engine was an Ethyl Gasoline Corporation test engine and it was operated in accordance with Procedure IV, namely, running at 1200 revolutions per minute, with sump temperature 300 F., and jacket temperature 212 F., and an iron catalyst in the amount of 0.1%, F203 as iron naphthenate. The fuel was a high octane gasoline containing 3 cc. of lead tetraethyl per gallon. The operating re- 4 metal compound, the following example is also included:
An oxidized parafdn wax, available under the name of "A101: 152" was reacted with 25% phosphorus penta'sulphide, which amount is that theoretically required to replace .the oxygen in this oxidized parailin wax. The reaction was carried out at 300 F. for one hour. The reaction product was separated from the sludge. The reaction product was found, upon analysis, to contain 1.87% phosphorus and 9.92% sulphur. It was tested in accordance with procedure IV explained earlier, with the following results, using the identical oil in each instance.
The reaction products of the invention are to be distinguished from reaction products obtained by reacting elemental sulphur and compounds yielding sulphur, such as sulphur halides, with oxygen containing compounds, since in such a reaction the oxygen is not replaced in the manner in which it is in accordance with the invention. The reaction products of the invention are also to be distinguished from the use of other sulphides in smaller amounts less than that in which the sulphur of the sulphide is the stoichiometric equivalent of the oxygen to be replaced. All such reaction products are inferior to the reaction product of the invention and not the equivalent thereof.
I claim:
1. A new lubricating oil composition of matter comprising a major portion of a lubricating oil and an amount of an additive sufficient to improve the stability of the lubricating oil, said additive comprising the metal compound of the reaction product of an oxygenated petroleum hydrocarbon boiling above the hereinafter named reaction temperature and an amount of phosphorus pentasulphide within the range of 14 to 30% and at least stoichiometrically sufficient to supplant the oxygen of the oxygenated petroleum hydrocarbon with sulphur, reacted at a temperature within the range of 275 to 425 F. to form a reaction product separable from a sludge sults beingcomprising the major part of the phosphorus in Same plus 3% San. plus 3% Same plus 37 S. A. E. 20 Midcalcium salt of oxidized paraicalcium salt of Continent Oil fin oxidizeiiid1 parafreaction product Hours Operation 20 20 2 60. Per cent Sludge- 5.0- 7.0- 8.0- 0.9. Acid number 2.5 2.0- 1.9- 0.6. Viscosity Inerpasa 150 270 228 94. Mg. lacquer per sq. dem. pistcn. .0. 85.0. 69.0.-. 0. Condition 0! Engine Light sludge Heavy sludge-.- Heavy sludge.-. No sludge.
For a continuous running test of twenty hours, it is thu seen that the original oil had a life of actually less than twenty hours for satisfactory lubrication, and that'the addition of oxidized paraflin or of the calcium salt of oxidized paramn did not materially aid, while the metal salt of the reaction product gave outstandingly good performance.
As illustrative of the properties of the initial the pentasulphide, and subsequently converted into said metal compound.
2. A new lubricating oil composition of matter comprising a major portion of a lubricating oil and an amount of an additive sufficient to improve the stability of the lubricating oil, said additive comprising the alkaline earth metal compound of the reaction product of an oxygenated petroleum hydrocarbon boiling above the hereinreaction product before its conversion into a 7 after named reaction temperature and an amount of phosphorus pentasulphide within the range of 14 to 80% and at least stoichiometrically suilicient to supplant the oxygen of the oxygenated petroleum hydrocarbon with sulphur. reacted at a temperature within the range oi 275 to 425 F. to form a reaction product separable from a sludge comprising the major part of the phosphorus in the pentasulphide, and subsequently converted into said alkaline earth metal compound.
3. A new lubricating oil composition of matter comprising a major portion of a lubricating oil and an amount of an additive suflicient to improve the stability of the lubricating oil, said additive comprising the metal compound reaction product of an oxidized parafiln wax and an amount of phosphorus pentasulphide within the range of 14 to 30% and at least stoichiometrically suflicient to supplant the oxygen of the oxidized parai'fln wax with sulphur, reacted at a temperature within the range of 275 to 425 F. to form a reaction product separable from a. sludge comprising the major part of the phosphorus in the pentasulphide, and subsequently converted into said metal compound.
4. A new lubricating oil composition of matter comprising a major portion of a lubricating oil and an amount of an additive sufiicient to improve the stability of the lubricating oil, said additive comprising the alkaline earth metal compound of the reaction product of an oxidized paraflln wax and about 20% phosphorus pentasulphide reacted at a temperature of about 300 F., said amount of phosphorus pentasulphide and said temperature resulting in a reaction product separable from a sludge comprising the major part of the phosphorus in the pentasulphide, and subsequently converted into the alkaline earth metal compound.
5. A new lubricating oil composition of matter comprising a, major portion of a lubricating oil and an amount of an additive suflicient to improve the stability of the lubricating oil, said adsupplant the oxygen of the oxidized paraflln was with sulphur, reacted at a temperature within the range of 275 to 425 F. to form a reaction product separable from a sludge comprising the mtaijor part of the phosphorus in the pentasulp de.
8. A new lubricating oil composition of matter comprising a major portion of a lubricating oil and an amount of an additive sufficient to improve the stability of the lubricating oil, said additive comprising the reaction product of an oxidized parafiin wax and about phosphorus pentasulphide, reacted at a temperature of about 300 F., said amount of phosphorus pentasulphide and said temperature resulting in a reaction product separable from a sludge comprising the major part of the phosphorus in the pentasulphide.
ditive comprising the calcium compound of the reaction product of an oxidized paraffin wax and about 20% phosphorus pentasulphide, reacted at a temperature of about 300 F., said amount of phosphorus pentasulphide and said temperature resulting in a reaction product separable from a sludge comprising the major part of the phosphorus in the pentasulphide; and subsequently converted into the calcium compound.
6. A new lubricating oil composition of matter comprising a major portion of a lubricating oil and an amount of an additive suiilcient to improve the stability of the lubricating oil, said additive comprising the reaction product of an oxygenated petroleum hydrocarbon boiling above the hereinafter named reaction temperature and an amount of phosphorus pentasulphide within the range of 14 to 30% and at least stoichiometrically suflicient to supplant the oxygen of the oxygenated petroleum hydrocarbon with sulphur, reacted at a temperature within the range of 275 to 425 F. to form a reaction product separable from a sludge comprising the major part of the phosphorus in the pentasulphide.
'7. A new lubricating oil composition of matter comprising a major portion of a lubricating oil and an amount of an additive sufiicient to-improve the stability of the lubricating oil, said additive comprising the reaction product of an oxidized paraffln wax and an amount of the phosphorus pentasulphide within the range 01 14 to 30% and at least stoichiometrically suflicient to 9. An additive effective in small amounts for improving the stability of a lubricating oil, comprising the metal compound of the reaction product of an oxygenated petroleum hydrocarbon boiling .above the hereinafter named reaction temperature and an amount of phosphorus pentasulphide Within the range of 14 to 30%, and at least stoichiometrically suflicient to supplant the oxygen of the oxygenated petroleum hydrocarbon with sulphur, reacted at a temperature within the range of 275 to 425 F. to form a reaction product separable from a sludge comprising the major part of the phosphorus in the pentasulphide, and subsequently converted into said metal compound.
10. An additive effective for improving the stability of a lubricating oil, comprising the alkaline earth metal compound of the reaction product of an oxygenated petroleum hydrocarbon boiling above the hereinafter named reaction temperature and an amount of phosphorus pentasulphide within rthe range of 14 to 30% and at least stoichiometrically sufficient to supplant the oxygen of the oxygenated petroleum hydrocarbon with sulphur, reacted at a temperature with-=- in the range of 275 to 425 F. to form a reaction product separable from a sludge comprising the major. part of the phosphorus in the pentasulphide, and subsequently converted into said alkaline earth metal compound.
11; An additive efiective for improving the stability of a lubricating oil, comprising the calcium compound of the reaction product of an oxidized parafiin Wax and about 20% phosphorus pentasulphide reacted at a temperature of about 300 F., said amount of phosphorus pentasulphide and said temperature resulting in a reaction product separable from a sludge comprising the major part of the phosphorus in the pentasulphide, and subsequently converted into said calcium compound.
12. An additive efiective for improving the stability of a lubricating oil, comprising the reaction product of an oxygenated petroleum hydrocarbon boiling above the hereinafter named reaction temperature and an amount of phosphorus pentasulphide within the range of 14 to 30% and at least stoichiometrically suflicient to supplant the oxygen of the oxygenated petroleum hydrocarbon with sulphur, reacted at a temperature within the range of 275 to 425 F. to form a reaction product separable from a sludge comprising the major part of the phosphorus in the pentasulphide.
13. A new composition of matter, suitable for use as an addition agent to improve the characted at a temperature within the range of 275 to 425 F. and with stolchiometrically sufllcient phosphorus pentasulphide to supplant oxygen of the oxygenated petroleum hydrocarbon with sulphur and to separate the major part of the 5 phosphorus from the reaction product.
JOHN M. MUSSELMAN.
REFERENCES The following references are of record in the 10 file of this patent:
UNITED STATES PATENTS Number Name Date 1,987,397 Gallsworthy Jan. 8, 1935 15 Number
US628382A 1945-11-13 1945-11-13 Lubricating composition Expired - Lifetime US2419325A (en)

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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2511630A (en) * 1947-02-04 1950-06-13 Shell Dev Liquid hydrocarbon lubricant, an additive therefor, and a process of making the additive
US2562904A (en) * 1946-08-27 1951-08-07 Michael W Freeman Lubricating oil composition
US2689827A (en) * 1952-02-15 1954-09-21 American Cyanamid Co Lubricating oil composition containing the neutralized reaction product of a phosphorus sulfide and sugar cane oil
US2830949A (en) * 1955-12-23 1958-04-15 Socony Mobil Oil Co Inc Phosphorus- and sulfur-containing complex metal salts of oxidized hydrocarbons and oil compositions thereof
US2864846A (en) * 1954-12-03 1958-12-16 Phillips Petroleum Co Process for producing lubricating oil additives
US2939841A (en) * 1956-06-15 1960-06-07 Union Oil Co High v. i. detergent lubricating oils
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* Cited by examiner, † Cited by third party
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US2562904A (en) * 1946-08-27 1951-08-07 Michael W Freeman Lubricating oil composition
US2511630A (en) * 1947-02-04 1950-06-13 Shell Dev Liquid hydrocarbon lubricant, an additive therefor, and a process of making the additive
US2689827A (en) * 1952-02-15 1954-09-21 American Cyanamid Co Lubricating oil composition containing the neutralized reaction product of a phosphorus sulfide and sugar cane oil
US2864846A (en) * 1954-12-03 1958-12-16 Phillips Petroleum Co Process for producing lubricating oil additives
US2830949A (en) * 1955-12-23 1958-04-15 Socony Mobil Oil Co Inc Phosphorus- and sulfur-containing complex metal salts of oxidized hydrocarbons and oil compositions thereof
US2939841A (en) * 1956-06-15 1960-06-07 Union Oil Co High v. i. detergent lubricating oils
US4298483A (en) * 1979-12-17 1981-11-03 Mobil Oil Corporation Metal forming lubricants
US20050209115A1 (en) * 2002-04-26 2005-09-22 Hirotsugu Kinoshita Grease composition
US8183191B2 (en) * 2002-04-26 2012-05-22 Nippon Oil Corporation Grease composition

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