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US2136391A - Lubricating composition - Google Patents

Lubricating composition Download PDF

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Publication number
US2136391A
US2136391A US673026A US67302633A US2136391A US 2136391 A US2136391 A US 2136391A US 673026 A US673026 A US 673026A US 67302633 A US67302633 A US 67302633A US 2136391 A US2136391 A US 2136391A
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United States
Prior art keywords
oil
lead
oils
compound
sulfur
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Expired - Lifetime
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US673026A
Inventor
Floyd L Miller
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Standard Oil Development Co
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Standard Oil Development Co
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Publication date
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Priority to US673026A priority Critical patent/US2136391A/en
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M135/00Lubricating compositions characterised by the additive being an organic non-macromolecular compound containing sulfur, selenium or tellurium
    • C10M135/02Sulfurised compounds
    • C10M135/06Esters, e.g. fats
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    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/132Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group
    • C07C29/136Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH
    • C07C29/147Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH of carboxylic acids or derivatives thereof
    • C07C29/149Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH of carboxylic acids or derivatives thereof with hydrogen or hydrogen-containing gases
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    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/10Preparation of carboxylic acids or their salts, halides or anhydrides by reaction with carbon monoxide
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    • C10M2201/00Inorganic compounds or elements as ingredients in lubricant compositions
    • C10M2201/04Elements
    • C10M2201/043Sulfur; Selenenium; Tellurium
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    • C10M2203/02Well-defined aliphatic compounds
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    • C10M2203/022Well-defined aliphatic compounds saturated
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • 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
    • C10N2040/00Specified use or application for which the lubricating composition is intended
    • C10N2040/10Running-in-oil ; Grinding
    • 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
    • C10N2040/14Electric or magnetic purposes
    • C10N2040/16Dielectric; Insulating oil or insulators
    • 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
    • C10N2040/14Electric or magnetic purposes
    • C10N2040/17Electric or magnetic purposes for electric contacts
    • 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
    • C10N2040/25Internal-combustion engines
    • 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
    • C10N2050/00Form in which the lubricant is applied to the material being lubricated
    • C10N2050/10Semi-solids; greasy

Definitions

  • the present invention relates to improvements v in lubricating oils' and more especially to oils of high quality and capable of withstanding high pressure and generally severe service.
  • the presentjcomposition will be fully described in the following specification.
  • the distillatestocks used are oils-of relatively low vis- "cosity index, such as oils derived from wax free; ,crudes which in general have viscosity. indices.
  • Heavy residual oils such as black oils, rich in tarryor asphaltic substances (which sometimes show higher viscosity lndices than 50) are used for leaded lubricants, but the high grade residuals-such as bright stocks or dewaxed' bright stocks are not available because of. their failure to hold the lead in a' stable form.
  • the present invention deals with the leaded compound produced from a high grade 011, for example, distiilates having a viscosity index above 60, or even above 80 or 90 and residuals free from asphalt havingyiscosity lndices above 80, 85, or even 90. It is thus possible by the pres- Applioation May 28, 1933, erial No. 673,026
  • the naphthenlc acids are of the type obtained either from Russian, Rumanian or certain American crudes, especially those obtained from California. These acids are obtained as mixtures and have average molecular 5 weights of about 250 or higher. They should be carefully refined so as to separate as completely as possible the oily non-acid constituents and in this condition they are light lemon-yellow in color.
  • the sulphonic acids are preferably those 10 obtained by the refining treatment of lubricating oils with fuming or other highly concentrated sulfuric acid. The acids are conveniently obtained as a by-product in-themanufacture of "white oil for medicinal and technical purposes and are the so-called Moho'gany acids which remain largely in the oil after the acid treatment.
  • the requisite amount of lead oxide, litharge is added to the acids and the temperature is raised to effect the. combination.-
  • the proportion of lead is, say, where the naphthenate is used. and. say,18% for the sulphonate, and it is preferred to make the lead compound from the oxide to other.
  • lead compounds such as the salts, 25
  • the lead compound may be made by reaction of sodium naphthenate or sodium sulphonate with lead ,nitrate or other suitable salt.
  • the compound is incorporated so in'the'oll without dimblllty by suitably raising the temperature while stirring vigorously.
  • the base stock preferred is, as stated above, an oil ofhigh viscosity index. of good color and otherwise well refined. Its viscodty may vary as considerably.- depending. upon the service to which the oil is destined. For some purposes the viscosity may be from or seconds Saybolt at 210 l"., to or 90, but for gear and transmission oils higher viscosities are desirable. say 40 above or at 210-F., and they may be as high as 200,250or more for particularly heavy ent method to produce stab1e,'1ight-colored,.”
  • naphthenic and sulfonic acids are the The leaded compound is ordinarily added in a proportion below about 10% of the oil. For ex- 48 ample, within the range of 545% or, expressed in terms of lead, for most purposes 24% gives satisfactory results.
  • oil-soluble substances rich in 60 sulfur may be added relatively small amounts of oil-soluble substances rich in 60 sulfur.
  • Various materials may be used for different purposes but synthetics are preferred since they can be produced with good color and odor.
  • the synthetics which are used are, of course, organic compounds solublein the oil, at least to such an extent as to furnish A to 5% of sulfur and they should be of high enough molecular as corrosive. This does not means that they cor- I rode bearings or gears to any appreciable extent but merely that they rapidly tarnish or discolor a bright stiip of copper which is allowed to stand in the liquid for several hours at 212 F. according to the A. S. T. M. corrosion test.
  • sulfurized animal, vegetable and marine oils are useful and they may be prepared by various methods, for example, reaction of elemental sulfur on the fatty oils.
  • Other suitable corrosive sulfur-bearing synthetics may be produced by the reaction of inorganic sulfur bearing compounds on halogenated aliphatic hydrocarbons.
  • the sulfides, polysulfides and hydro-sulfides of alkali and alkaline earth metals may be caused to react with chlorinated hydrocarbons, for example, paraflin wax, at temperatures of about 200 to 300 F. The sulfur appears to replace the chlorine at these temperatures and if suificient time is allowed, the substitution may be complete.
  • the oils produced by the above methods are.
  • Example 1 To a suitable base oil 10% of a leaded compound produced from naphthenic acid is added.
  • the leaded compound is produced by heating approximately 25 pounds of a lead oxide with 50 unds of naphthenic acids having an acid value of 223 and derived from a California crude.
  • To this compound is then added 3% of a synthetic containing corrosive sulfur.
  • the synthetic is produced by treating pine. oil with sulfur at a temperature of 200 C.
  • the inspection of the base oil (I), the blend before addition of the synthetic sulfur compound (II), and of the blend after such sulfur compound has been added (III) are given-below?
  • the base oil (I) showed a load bearing capacity of 5 wts. when tested on the well-known Mougey machine and 3 wts. on the Almen machine.
  • the leaded blend (ID gave bearing capacities of 8-10 wts. and 2 wts. respectively on the two machines,
  • Viscosity index ' was conducted in strict accordance with the and the blend containing the sulfur compound (III) showed values of 25 wts. and. 15 wts. (capacity loads) respectively. It will be noted that the lead-sulfur compound is especially effective on the Almen machine which shows the effect of 5 a rapidly applied load.
  • the blended oils are found to. be of high stability; for example, no settling is noticed after several weeks standing.
  • Example 2 In another similar composition a hydrogenated oil having a viscosity of 102 at 210 F. and a Viscosity Index of is incorporated with 10% of lead sulfonate and 5% of a corrosive synthetic produced by refiuxingparaflin, whichv had been chlorinated to the extent of 20%, with sodium polysulfide.
  • the synthetic contained about equal amounts of sulfur and chlorine.
  • the base oil comprises a synthetic hydrocarbon lubricating oil produced by aluminum chloride condensation of cracked paraifln wax. To this base 10% of lead naphthenate is added with 4% of sulfurized pine oil.
  • An improved lubricatingcomposition of high stability comprising as a base stock alubricatpound of an acid selected from the class of naphthenic and sulfom'c acids and an oil soluble substance rich in sulphur.
  • An improved lubricating composition comprising a major proportion of lubricating oil base characterized by a viscosity index above and containing in solution both a'lead compound soluble therein selected from the class of naphthenate and sulphonate and an oil soluble substance rich in corrosive sulphur.
  • composition according to claim 2 in which the lead compound comprises lead naphthenate and the sulphur rich material is a sulphurized vegetable oil.
  • composition according to claim 2 in which the lead compound comprises lead naphthenate and the sulphur rich material comprises sulphurized pine oil.
  • composition according to claim 2 in'which the lead compound comprises lead sulphonate and the sulphur rich material is selected from the class of sulphurized animal, vegetable and marine oils.
  • composition according to claim 2 in which the, lead compound comprises lead sulphonate and the sulphur rich material is a sulphurized vegetable oil.
  • composition according to claim 2 in which the lead compound comprises lead sulphonate and the sulphur'rich material comprises sulphurized pine oil.
  • An improved lubricating oil comprising a major proportion of a base stock characterized by a viscosity index above and containing in solution both a soluble lead vcompound selected from the class of naphthenates and sulphonates and ar'ioil soluble substance rich in sulphur and selected from the group of sulphurized animal,
  • a base stock characterized by a viscosity index above and containing in solution both a soluble lead compound selected from the class of naphthenate and sulphonate, and an oil soluble substance rich in sulphur selected from the class of sulphurized animal, vegetable and marine oils.
  • composition according to claim 10 in which the lead compound is lead naphthenate and the sulphur compound comprises a sulphurized vegetable oil.
  • composition of matter according to claim 10 in which the lead compound is lead naphthenate and the sulphur compound is a sulphurized pine oil.
  • composition according to claim 2 in which said oil soluble substance rich in corrosive sulphur contains halogen.
  • composition according to claim 9 in which said sulphurized oil contains sulphur and chlorine in equal'quantities.
  • An improved lubricating composition of high stability comprising as a base stock a lubricating oil of high viscosity index containing in solution both a small quantity of a leaded compound of an acid selected from the class ofnaphthenic and sulfonic acids and a sulfurized iatty oil of the non-drying type.
  • An improved lubricating composition of high stability comprising as a base stock a lubri- V cating oilof high viscosity index containing in solution both a small quantity of ,a leaded compound of an acid selected from the'class of naphthenic and sulfonic acids and a sulfurized nondrying fatty oil of the corrosive type.
  • An improved lubricating oil composition of high stability comprising as a base stock a lubricating oil of high viscosity index containingv in solution both a small quantity of a lead compound of an acid selected from the class of naphthenicand sulfonic acids and sulfurized lard oil.

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

Description

Patented Nov. 15, 1938- Floyd L. Miller, Elizabeth, N. 1., asslgnor to Standard Oil Development Company; a corporation of Delaware 20 Claims.
The present invention relates to improvements v in lubricating oils' and more especially to oils of high quality and capable of withstanding high pressure and generally severe service. The presentjcomposition will be fully described in the following specification.
During the last several years leaded lubricating oils have'found general application but there are objections to the present compounds which limit their use considerably. One is the instability of the lead oleate which is generally used 'partic-' ularly in high grade base oils. The compound is not'freely soluble in high grade base oils, such as the distillates or bright stocks derived from wax. At ordinary temperatures and 1 bearing crudes. I
on-standing for a relatively short time the compound settles out of the oil in a thick sludge. For this reason the leaded compounds must be made up from relatively low'grade base oils. The distillatestocks used are oils-of relatively low vis- "cosity index, such as oils derived from wax free; ,crudes which in general have viscosity. indices.
below 50 on the scale devised by Davis and Dean,
Chem; and Met. Engineering 36-618 (1929). a
25 Heavy residual oils such as black oils, rich in tarryor asphaltic substances (which sometimes show higher viscosity lndices than 50) are used for leaded lubricants, but the high grade residuals-such as bright stocks or dewaxed' bright stocks are not available because of. their failure to hold the lead in a' stable form.
It. is highly'desirable to make use of the better.
grade of base oils, specifically the distillates' and residuals of waxy crudesfor leaded compounds in orderto obtain a better viscosity-temperature 7 curve and resistance to oxidation and sludge forination 'which is characteristic of these oils.
.The present invention deals with the leaded compound produced from a high grade 011, for example, distiilates having a viscosity index above 60, or even above 80 or 90 and residuals free from asphalt havingyiscosity lndices above 80, 85, or even 90. It is thus possible by the pres- Applioation May 28, 1933, erial No. 673,026
'most desirable. The naphthenlc acids are of the type obtained either from Russian, Rumanian or certain American crudes, especially those obtained from California. These acids are obtained as mixtures and have average molecular 5 weights of about 250 or higher. They should be carefully refined so as to separate as completely as possible the oily non-acid constituents and in this condition they are light lemon-yellow in color. The sulphonic acids are preferably those 10 obtained by the refining treatment of lubricating oils with fuming or other highly concentrated sulfuric acid. The acids are conveniently obtained as a by-product in-themanufacture of "white oil for medicinal and technical purposes and are the so-called Moho'gany acids which remain largely in the oil after the acid treatment.
In-producing the leaded compounds of these acids the requisite amount of lead oxide, litharge, is added to the acids and the temperature is raised to effect the. combination.- The proportion of lead is, say, where the naphthenate is used. and. say,18% for the sulphonate, and it is preferred to make the lead compound from the oxide to other. lead compounds such as the salts, 25
although these latter can be used. For example, the lead compound may be made by reaction of sodium naphthenate or sodium sulphonate with lead ,nitrate or other suitable salt. When the compound has been produced it is incorporated so in'the'oll without dimblllty by suitably raising the temperature while stirring vigorously.
, The base stock preferred is, as stated above, an oil ofhigh viscosity index. of good color and otherwise well refined. Its viscodty may vary as considerably.- depending. upon the service to which the oil is destined. For some purposes the viscosity may be from or seconds Saybolt at 210 l"., to or 90, but for gear and transmission oils higher viscosities are desirable. say 40 above or at 210-F., and they may be as high as 200,250or more for particularly heavy ent method to produce stab1e,'1ight-colored,."
'45- clean, transparent oils containing lead in effective quantities from oils of Pennsylvania quality or" even better such as hydrogenated petroleum oils, high grade oils produced by solvent extraction processes. and even the synthetic oils produced by condensation of cracked or dehydrogenated wax and the like, either aloneor condensed with aromatic hydrocarbons. '7
. In orderto' make the -leaded compound soluble and stable, acids others than oleic are used; for
1.. example, naphthenic and sulfonic acids are the The leaded compound is ordinarily added in a proportion below about 10% of the oil. For ex- 48 ample, within the range of 545% or, expressed in terms of lead, for most purposes 24% gives satisfactory results.
To the above blend may be added relatively small amounts of oil-soluble substances rich in 60 sulfur. Various materials may be used for different purposes but synthetics are preferred since they can be produced with good color and odor. The synthetics which are used are, of course, organic compounds solublein the oil, at least to such an extent as to furnish A to 5% of sulfur and they should be of high enough molecular as corrosive. This does not means that they cor- I rode bearings or gears to any appreciable extent but merely that they rapidly tarnish or discolor a bright stiip of copper which is allowed to stand in the liquid for several hours at 212 F. according to the A. S. T. M. corrosion test.
For this purpose sulfurized animal, vegetable and marine oils are useful and they may be prepared by various methods, for example, reaction of elemental sulfur on the fatty oils. Other suitable corrosive sulfur-bearing synthetics may be produced by the reaction of inorganic sulfur bearing compounds on halogenated aliphatic hydrocarbons. For example, the sulfides, polysulfides and hydro-sulfides of alkali and alkaline earth metals may be caused to react with chlorinated hydrocarbons, for example, paraflin wax, at temperatures of about 200 to 300 F. The sulfur appears to replace the chlorine at these temperatures and if suificient time is allowed, the substitution may be complete. It is sometimes desirable, however, to replace the sulfur only par.- tially so that both sulfur and chlorine may be present together, say in equal quantities, or either one or the other may be in excess. The synthetic, by whatever method it may be produced, wedded. to the oil so as to provide sulfur in proportion of about to 5% by weight.
The oils produced by the above methods are.
extremely stable and show no tendency to separate a lead sludge. They may be of extremely high viscosity index, depending upon the base stock, and even with high viscosity index the high degree of stability persists. They may be of light color if well refined ingredients are used in their preparation and the composition containing the lea .ed compound and corrosive sulfur is of particular: advantage since it is capable of withstanding extremely high bearing pressures under conditions of a rapidly applied load. As
examples of the present compounds the following may be considered:
Example 1.--To a suitable base oil 10% of a leaded compound produced from naphthenic acid is added. The leaded compound is produced by heating approximately 25 pounds of a lead oxide with 50 unds of naphthenic acids having an acid value of 223 and derived from a California crude. To this compound is then added 3% of a synthetic containing corrosive sulfur. The synthetic is produced by treating pine. oil with sulfur at a temperature of 200 C. The inspection of the base oil (I), the blend before addition of the synthetic sulfur compound (II), and of the blend after such sulfur compound has been added (III) are given-below? The base oil (I) showed a load bearing capacity of 5 wts. when tested on the well-known Mougey machine and 3 wts. on the Almen machine. The leaded blend (ID gave bearing capacities of 8-10 wts. and 2 wts. respectively on the two machines,
' Viscosity index 'were conducted in strict accordance with the and the blend containing the sulfur compound (III) showed values of 25 wts. and. 15 wts. (capacity loads) respectively. It will be noted that the lead-sulfur compound is especially effective on the Almen machine which shows the effect of 5 a rapidly applied load.
The blended oils are found to. be of high stability; for example, no settling is noticed after several weeks standing.
Similar results were obtained using a sulfurized compound produced from lard oil by the action of sulfuryl chloride.
Example 2.-In another similar composition a hydrogenated oil having a viscosity of 102 at 210 F. and a Viscosity Index of is incorporated with 10% of lead sulfonate and 5% of a corrosive synthetic produced by refiuxingparaflin, whichv had been chlorinated to the extent of 20%, with sodium polysulfide. The synthetic contained about equal amounts of sulfur and chlorine. The inspection of the base oil (I) and the final product (II) are as follows:-
Gravity- Viscosity at 210 F Viscosity at F Pour int Cnlnr Percent sulfur"; 30
In load bearing tests the base oil successfully stood a bearing. pressure of 5 wts. on the Mougey machine and3 wts. on the Almen machine, respectively, while the blend showed increased values of 25 wts. and 15 wts. respectively.
Example 3.-As a third example, the base oil comprises a synthetic hydrocarbon lubricating oil produced by aluminum chloride condensation of cracked paraifln wax. To this base 10% of lead naphthenate is added with 4% of sulfurized pine oil.
The inspection of the base oil (I) and the blend (II) are as follows:
0 Percent sulfur In the above examples reference has been made to Mougey and Almen tests. These have been described in detail in Nat. Pt. News, Nov. 11, 1931, p. 47, and Nov. 16, 1932, p. 39,- and the tests ticular leaded compound nor to any particular base'stock or in fact to any particularsubs'tance of sulfur, but only to the following claims. in which it is desired to claim allnovelty inherent in the invention. 76
I claim: 1. An improved lubricatingcomposition of high stability,'comprising as a base stock alubricatpound of an acid selected from the class of naphthenic and sulfom'c acids and an oil soluble substance rich in sulphur.
2. An improved lubricating composition comprising a major proportion of lubricating oil base characterized by a viscosity index above and containing in solution both a'lead compound soluble therein selected from the class of naphthenate and sulphonate and an oil soluble substance rich in corrosive sulphur.
3. Composition according to claim 2 in which the lead compound comprises lead naphthenate and the sulphur rich material is selected from the class of sulphurized animal, vegetable and marine oils.
4. Composition according to claim 2 in which the lead compound comprises lead naphthenate and the sulphur rich material is a sulphurized vegetable oil.
,5. Composition according to claim 2 in which the lead compound comprises lead naphthenate and the sulphur rich material comprises sulphurized pine oil.
6. Composition according to claim 2 in'which the lead compound comprises lead sulphonate and the sulphur rich material is selected from the class of sulphurized animal, vegetable and marine oils.
7. Composition according to claim 2 in which the, lead compound comprises lead sulphonate and the sulphur rich material is a sulphurized vegetable oil.
- 8. Composition according to claim 2 in which the lead compound comprises lead sulphonate and the sulphur'rich material comprises sulphurized pine oil.
9. An improved lubricating oil comprising a major proportion of a base stock characterized by a viscosity index above and containing in solution both a soluble lead vcompound selected from the class of naphthenates and sulphonates and ar'ioil soluble substance rich in sulphur and selected from the group of sulphurized animal,
' vegetable and marine oils of the corrosive type.
major proportion of a base stock characterized by a viscosity index above and containing in solution both a soluble lead compound selected from the class of naphthenate and sulphonate, and an oil soluble substance rich in sulphur selected from the class of sulphurized animal, vegetable and marine oils.
11. Composition according to claim 10 in which the lead compound is lead naphthenate and the sulphur compound comprises a sulphurized vegetable oil.
12. Composition of matter according to claim 10 in which the lead compound is lead naphthenate and the sulphur compound is a sulphurized pine oil.
13. Composition according to claim 2 in which said oil soluble substance rich in corrosive sulphur contains halogen.
14. Composition according to claim 9 in whic said sulphurized oil contains chlorine. r
15. Composition according to claim 9 in which said sulphurized oil contains sulphur and chlorine in equal'quantities.
16. A composition according to claim 2 in which the proportion of lead is from about 2% to 3% and of sulfur is from about /2 to 5%.
17. A composition according to claim 2 in which the proportion-of lead is from about 0.9% to 4.5% and of sulfur is from about to 5%.
18. An improved lubricating composition of high stability, comprising as a base stock a lubricating oil of high viscosity index containing in solution both a small quantity of a leaded compound of an acid selected from the class ofnaphthenic and sulfonic acids and a sulfurized iatty oil of the non-drying type.
19. An improved lubricating composition of high stability comprising as a base stock a lubri- V cating oilof high viscosity index containing in solution both a small quantity of ,a leaded compound of an acid selected from the'class of naphthenic and sulfonic acids and a sulfurized nondrying fatty oil of the corrosive type.-
20. An improved lubricating oil composition of high stability comprising as a base stock a lubricating oil of high viscosity index containingv in solution both a small quantity of a lead compound of an acid selected from the class of naphthenicand sulfonic acids and sulfurized lard oil.
' FLOYD L. MEIER.
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Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2418894A (en) * 1944-12-09 1947-04-15 Standard Oil Dev Co Compounded lubricating oil
US2419584A (en) * 1945-01-18 1947-04-29 Socony Vacuum Oil Co Inc Mineral oil composition
US2433646A (en) * 1943-03-15 1947-12-30 Sun Oil Co Soluble oil and process of producing same
US2501732A (en) * 1946-10-14 1950-03-28 Union Oil Co Modified lubricating oil
US2501731A (en) * 1946-10-14 1950-03-28 Union Oil Co Modified lubricating oil
US2701237A (en) * 1950-09-26 1955-02-01 Harry Sokol Extreme pressure lubricant
US2711395A (en) * 1953-11-25 1955-06-21 Sinclair Refining Co Cutting oil composition
US2785130A (en) * 1953-12-21 1957-03-12 Texas Co Extreme pressure lubricant
US3200072A (en) * 1961-12-26 1965-08-10 Pure Oil Co Extreme pressure lubricant containing alkyd resins derived from complex acids
US3250711A (en) * 1964-03-06 1966-05-10 Shell Oil Co Gear lubricant
US3303129A (en) * 1965-07-26 1967-02-07 Atlantic Refining Co Method for breaking in aluminum cylinders of an internal combustion engine

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2433646A (en) * 1943-03-15 1947-12-30 Sun Oil Co Soluble oil and process of producing same
US2418894A (en) * 1944-12-09 1947-04-15 Standard Oil Dev Co Compounded lubricating oil
US2419584A (en) * 1945-01-18 1947-04-29 Socony Vacuum Oil Co Inc Mineral oil composition
US2501732A (en) * 1946-10-14 1950-03-28 Union Oil Co Modified lubricating oil
US2501731A (en) * 1946-10-14 1950-03-28 Union Oil Co Modified lubricating oil
US2701237A (en) * 1950-09-26 1955-02-01 Harry Sokol Extreme pressure lubricant
US2711395A (en) * 1953-11-25 1955-06-21 Sinclair Refining Co Cutting oil composition
US2785130A (en) * 1953-12-21 1957-03-12 Texas Co Extreme pressure lubricant
US3200072A (en) * 1961-12-26 1965-08-10 Pure Oil Co Extreme pressure lubricant containing alkyd resins derived from complex acids
US3250711A (en) * 1964-03-06 1966-05-10 Shell Oil Co Gear lubricant
US3303129A (en) * 1965-07-26 1967-02-07 Atlantic Refining Co Method for breaking in aluminum cylinders of an internal combustion engine

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