US2535101A - Sulfonate base lubricating grease - Google Patents

Sulfonate base lubricating grease Download PDF

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US2535101A
US2535101A US15747A US1574748A US2535101A US 2535101 A US2535101 A US 2535101A US 15747 A US15747 A US 15747A US 1574748 A US1574748 A US 1574748A US 2535101 A US2535101 A US 2535101A
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molecular weight
sulfonate
oil
sulfonates
grease
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US15747A
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Lorne W Sproule
Warren C Pattenden
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Standard Oil Development Co
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Standard Oil Development Co
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    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M115/00—Lubricating compositions characterised by the thickener being a non-macromolecular organic compound other than a carboxylic acid or salt thereof
    • C10M115/10—Lubricating compositions characterised by the thickener being a non-macromolecular organic compound other than a carboxylic acid or salt thereof containing sulfur
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2219/00—Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions
    • C10M2219/04—Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions containing sulfur-to-oxygen bonds, i.e. sulfones, sulfoxides
    • C10M2219/044—Sulfonic acids, Derivatives thereof, e.g. neutral salts
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2219/00—Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions
    • C10M2219/04—Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions containing sulfur-to-oxygen bonds, i.e. sulfones, sulfoxides
    • C10M2219/046—Overbasedsulfonic acid salts
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2010/00—Metal present as such or in compounds
    • C10N2010/02—Groups 1 or 11
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2010/00—Metal present as such or in compounds
    • C10N2010/04—Groups 2 or 12
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2010/00—Metal present as such or in compounds
    • C10N2010/06—Groups 3 or 13

Definitions

  • the presentinvention relates to a sulfonate base lubricating grease and more particularly to a lubricating grease containing metallic sulionates of a character designed to impart high meltin point characteristics to lubricating grease compositions.
  • the present invention is based on the discovery that a very suitable lubricating grease may be prepared by using an appropriate quant ty of a relatively high molecular weight metal sulfonate in combination with a relatively small amount of a lower molecular weight and relatively oil-insoluble metal sulfonate.
  • the lower metal sulfonates and to some extent some of the higher sulfonates also, are quite water-soluble but the lower sulfonates are not appreciably soluble in mineral oil.
  • the present invention depends on the fact that a combination of high molecular weight and low molecular weight sulfonates dispersed in mineral oil produces a smooth, homogeneous, high melting point lubricating grease which cannot be obtained by the use of either type of sulfonate alone.
  • a lubricating grease was prepared by combining 20 parts by weight on a dry soap basis of oilsoluble calcium petroleum sulfonate having a molecular weight of about 740, 8 parts by weight of calcium ethane sulfonate with a molecular weight of about 258, and 72 parts of mineral lubricating oil of appropriate viscosity, for example 100 S. S. U. at 100 F. or 40 S. S. U. at 210 F.
  • the high molecular weight calcium sulfonate was prepared by calcium chloride treatment of sodium sulfonates recovered in the manufacture of white oils.
  • sulfonates are commonly obtained by treating the lubricating oil and heavier fractions of petroleum with strong, preferably fuming, sulfuric acid to form alkyl-aryl sulfonic acids.
  • the acids so formed are neutralized with an alkaline material, such as sodium hydroxide, to form the sulfonates.
  • the acids and the monovalent metal sulfonates of molecular weight substantially above 300 are generally oil-soluble. They may be recovered from the oil in which they are formed by selective solvent extraction, for example by extraction with isopropyl alcohol.
  • the particular high molecular weight sulfonate used was prepared from an emulsion consisting of a concentrate in oil and water of a sodium salt of sulfonic acid of molecular weight varying between 300 and 400. This emulsion was treated with calcium chloride and the sodium chloride resulting from double decomposition was washed out. The high molecular weight calcium sulfonate thus obtained was dissolved in part of the mineral oil and the low molecular weight sulfonate (calcium ethane sulfonate obtained by direct lime Example 1.
  • EXAMPLEZ Another example of a grease comprising higher and lower calcium suli'onates was prepared by combining 11 parts by weight of a calcium petroleum sulfonate of relatively high molecular weight with 6 parts of ethane sultonic acid (molecular weight 110) and 2.4 parts of lime in 80.6 parts of mineral oil.
  • the mineral oil used in this example had a viscosity of 320 S. S. U. at 100 F. and .a viscosity index of 40.
  • the alkylaryl sulfonic acid used in preparing the higher sulfonate had a molecular weight of approximately 350.
  • the mol ratio of high molecular weight sulfonic acid to low molecular weight sulfonic acid was 1 to 2 as indicated below in the table.
  • This composition had a good firm consistency as evidenced by its worked penetration of 310, and a high dropping point of 400+F.
  • EXAMPLE 3 Another sample was made by combining 16 parts by weight 01' the calcium petroleum suli'onate of Example 2 with 4.4 partspf ethane sulfonic acid, 1.8 parts of hydrated lime, and 17.8v parts of the same oil as was also used in Examle 2. 'he grease o thisexample was prepared in substantially the same manner as that of It will be noted that the mol ratio of the higher and lower sulfonates was approximately 1 to 1. The grease had a slightly softer penetration than that of Example 2, but was smooth and transparent in texture and had a dropping point in excess of 400 F.
  • EXAMPLE 4 A further example was prepared by using 16% by weight of calcium sulfonate prepared from a sulfonic acid having a molecular weight of about 450. To this were added in aqueous solution 3.8% by weight based on the final composition, of ethane sulfonic acid, and 1.6% of hydrated lime. The mineral oil content was 78.6%, the same oil being used as in Examples 2 and 3 above. In this composition the mol ratio of the higher and lower 'sulfonates was 1 to l. The excess alkalinity was considerably lower than in Examples 2 and 3. The grease was somewhat softer, having a worked penetration of 360 but it was smooth and transparent in appearance and had a dropping point in excess of 400 F.
  • compositions described above in Examples 2, 3 and 4 were prepared in the same general manner, that is by dissolving the high molecular weight sulfonates in part of the oil, adding the lower sulfonate in an aqueous solution, dehydrating by heating to a temperature in the neighborhood of 300 F. and thereafter adding the remainder of the mineral oil and cooling with stirring to temperature of around 200 F.
  • EXAMPLE 5 The composition was prepared consisting'oi 16% by weight of oil-soluble barium petroleum sulfonate prepared from the same relatively high molecular weight sulfonic acids as the calcium sulfonates of Examples 2 and 3 above. 4.2% of ethane sulfonic acid and 6.4% of barium hydroxideocta-hydrate were added being combined with 73.4% of mineral oil of 320 S. S. U. at 100 F. and a viscosity index of 40.
  • Example 5 had a considerably harder consistency than those of Examples 1 and 4 above. The dropping point, however, was lower, being approximately 260 F. The product was smooth and transparent.
  • a soda base grease wa prepared by using 25% of the oil soluble sodium sulfonate prepared from the same acids as Examples 2, 3 and 5 with 11% ethane sultonic acid, 5% sodium hydroxide and Tum 2 Formulae and properties of barium sulfonate and sodium sulfonate greases Formula, per cent by weight:
  • grease compositions prepared according to the present invention make use of the oil-soluble petroleum sulfonates of commerce.
  • These usually contain petroleum sulfonic acids ranging in molecular weight from 300 to 500 or slightly more. They are usually soluble in mineral oil, becoming very tacky and viscous at high concentrations.
  • the low molecular weight sulfonic acids such as ethane sulfonic acid, which has a molecular weight of 110, form metallic salts which will not dissolve in oil.
  • Methane sulfonic acid with a molecular weight of about 96, may be used for preparing the lower molecular weight sulfonate, and other homologues such as propane and butane sulfonate may be used. Mixtures of these and related acids may be used also.
  • the melting point of greases may be raised considerably and their structural stability is improved.
  • the foregoing examples show the use of the calcium, barium, and sodium sulfonates, but it will be understood that other sulfonates, such as zinc, aluminum, lithium, and the like may also be employed.
  • the quantity of sulfonate employed depends somewhat upon the viscosity of the mineral oil chosen. For a very light mineral oil, it is necessary to use larger quantities of sulfonates to get a suitable grease consistency. On the other hand, when heavy oils are employed, the sulfonate concentrations may be much lower. Thus, for a very heavy oil as little as 5% of the oil soluble sulfonate and about 3% of the non-oil soluble sulfonate will make a grease of reasonable good consistency. For a very light oil, several times as much may be required.
  • the sulfonate proportions will be between 5 and %7 0f the high molecular weight compound and from about 3 to 20% of the low molecular weight compound.
  • the high molecular weight sulfonates are preferably derived from sulfonic acids having an average molecular weight within the general range of about 300 to about 500. Acids having molecular weight of around 400 are particularly preferred.
  • the non-oil soluble sulfonates may be derived from the so-called black or green acids having an average molecular weight less than 300 and preferably between about 96 and 250. Ethane sulfonic acid is specifically preferred fo preparation of the oil insoluble sulionate ingredient.
  • Mineral oils used in such greases should preferably have a viscosity of at least S. S. U. at 100 F. and their viscosity may run as high as 1000 S. S. U. at 210 F.
  • additives which are commonly used in lubricating greases may be added to the foregoing compositions as will be evident to those skilled in the art.
  • Such additives may comprise the usual antioxidants, rust inhibitors, tackiness agents,
  • viscosity index improvers, extreme pressure Ill of mineral lubricating oil containing 5 to 25% byv weight, based on the total composition, of an oil soluble sulfonate having a sullonate radical molecular weight of more than 300 and not substantially greater than about 500, and 3 to 20% of a non-oil soluble sulfonate of a sulfonic acid having a molecular weight between 96 and 250, the combined sulfonates being effective to impart a grease-like consistenc to said oil.
  • a lubricating grease composition of high melting point consisting essentially of a mineral base lubricating oil of viscosity within the range of 60 S. S. U. at 100 F. to 1000 S. S. U. at 210 F., said oil containing 5 to 25%, by weight based on the final composition, of an oil soluble metal sulfonate having a sulfonate radical molecular weight of more than 300 and not substantially greater than about 500 and 3 to 20% of an oil insoluble metal alkyl sulfonate of a sulfonic acid having a molecular weight between 96 and 250.
  • composition as in claim 2 wherein said oil soluble sulfonate is an alkaline earth metal salt of sulfonic acids having an average molecular weight between about 300 and about 500.
  • composition as in claim 2 wherein said oil soluble sulionate is the calcium salt of petroleum sulfonic acids having an average molecular weight between about 300 and about 500.
  • composition as in claim 2 wherein said oil soluble sulionate is the barium salt of sulfonic acids having an average molecular weight between about 300 and about 500.
  • composition as in claim 2 wherein said oil soluble sulfonate is the sodium salt of sulfonic acids having an average molecular weight between about 300 and about 500.
  • composition as in claim 2 wherein said oil insoluble sulfonate is the sodium salt of sulfonic acid having an average molecular Weight between about 96 and 250.
  • a lubricating grease composition of high melting point consisting essentially of a mineral base lubricating oil of viscosity between 60 S. S. U. at 100 F. and 1000 S. S. U. at 210 F., 5 to 25% by weight, based on the ijnal composition, of substantially equimolar of the calcium salt of sulionic acid having an average molecular weight of between 300 and 400, and the calcium salt of ethane sulfonic acid, the combined quantities of sulfonates being sufficient to impart a grease like consistency to said oil.
  • composition according to claim 1 containing an excess of metal base beyond that required to neutralize the acids of said sulfonates.

Description

Patented Dec. 26, 1950 Lorne W.
Sarnta,
Spronle and Warren 0. Pattenden, Ontario, Canada, aaaignors to Standard 911 Development Company, a corporation of Delaware No Drawing. Application March 18, 1948, 1 Serial No. 15,747 I a cam (01. 252- 33) The presentinvention relates to a sulfonate base lubricating grease and more particularly to a lubricating grease containing metallic sulionates of a character designed to impart high meltin point characteristics to lubricating grease compositions.
It is well known in the prior art that certain types of lubricating greases, for example the lime soap base greases. have good lubricating characteristics at low temperatures but are not suitable for use at elevated temperatures, for example temperatures above 150 or 175 F. The lime soap greases prepared from fats or fatty acids which have'longbeen used for thickening lubricati oils in the preparation of grease type lubricants, normally require the presence of a small amount of water to insure mechanical stability. In the absence of such water, the soap and the lubricating oil separate at higher temperatures, for example 150 to 175 F., or more. This oil separation appears to be due to the evaporation of the water content at the higher temperature. the water normally serving to bond the soap into the oil in some manner and prevent separation in ordinary storage Or low temperature use.
The deficiencies in calcium base greases mentioned above have long been known and numerous attempts have been made in the prior art to replace the water with higher boiling compounds. For example, calcium salts of certain saturated carboxylic acids, such as acetic acid, have been added in minor proportions to calcium soap greases to prevent the separation of oil from the soap and also to raise the melting point of the composition. Such a composition is disclosed in U. S. Patent No. 2,197,263.
Conventional greases of the types mentione above consist largely of lubricating oil of appropriate grade thickened to a grease consistency with a fatty acid soap of a suitable metal, usually calcium, although the soaps of other metals are frequently employed. It has also been known in the prior art that certain of the so-called "mahogany" soaps, that is the metal salts of high molecular weight alkyl-aryl sulfonic acids derived from the manufacture of white oils in petroleum reflning, are useful in the manufacture of certain lubricating greases. Such materials, however, are generally oil soluble and thus have little thickening effect. As a result, they are ordinarily used in minor proportions along with conventional fatty acid soap type thickeners.
The present invention is based on the discovery that a very suitable lubricating grease may be prepared by using an appropriate quant ty of a relatively high molecular weight metal sulfonate in combination with a relatively small amount of a lower molecular weight and relatively oil-insoluble metal sulfonate. The lower metal sulfonates and to some extent some of the higher sulfonates also, are quite water-soluble but the lower sulfonates are not appreciably soluble in mineral oil.
The present invention depends on the fact that a combination of high molecular weight and low molecular weight sulfonates dispersed in mineral oil produces a smooth, homogeneous, high melting point lubricating grease which cannot be obtained by the use of either type of sulfonate alone.
It has been found that a grease employing a combination of high and low molecular weight sulfonates as a thickening agent has a dropping point very substantially higher than in the case of grease which is thickened with the calcium soaps of fatty acids. The following examples show the relative characteristics and properties of various samples exemplifying the present invention.
EXAMPLE 1 A lubricating grease was prepared by combining 20 parts by weight on a dry soap basis of oilsoluble calcium petroleum sulfonate having a molecular weight of about 740, 8 parts by weight of calcium ethane sulfonate with a molecular weight of about 258, and 72 parts of mineral lubricating oil of appropriate viscosity, for example 100 S. S. U. at 100 F. or 40 S. S. U. at 210 F. The high molecular weight calcium sulfonate was prepared by calcium chloride treatment of sodium sulfonates recovered in the manufacture of white oils.
These sulfonates, as is well-known in the art, are commonly obtained by treating the lubricating oil and heavier fractions of petroleum with strong, preferably fuming, sulfuric acid to form alkyl-aryl sulfonic acids. The acids so formed are neutralized with an alkaline material, such as sodium hydroxide, to form the sulfonates. The acids and the monovalent metal sulfonates of molecular weight substantially above 300 are generally oil-soluble. They may be recovered from the oil in which they are formed by selective solvent extraction, for example by extraction with isopropyl alcohol.
The particular high molecular weight sulfonate used was prepared from an emulsion consisting of a concentrate in oil and water of a sodium salt of sulfonic acid of molecular weight varying between 300 and 400. This emulsion was treated with calcium chloride and the sodium chloride resulting from double decomposition was washed out. The high molecular weight calcium sulfonate thus obtained was dissolved in part of the mineral oil and the low molecular weight sulfonate (calcium ethane sulfonate obtained by direct lime Example 1.
treatment or ethane sultonic acid) was dissolved in water. The two solutions were then mixed and heated to a. temperature of about 300 F. with continued agitation until all water had been removed. Thereupon the remainder of the mineral oil was added with stirring and the grease composition was then cooled with continued stirring to a temperature of 200 F. At that temperature the grease was poured into containers.
EXAMPLEZ Another example of a grease comprising higher and lower calcium suli'onates was prepared by combining 11 parts by weight of a calcium petroleum sulfonate of relatively high molecular weight with 6 parts of ethane sultonic acid (molecular weight 110) and 2.4 parts of lime in 80.6 parts of mineral oil. The mineral oil used in this example had a viscosity of 320 S. S. U. at 100 F. and .a viscosity index of 40. The alkylaryl sulfonic acid used in preparing the higher sulfonate had a molecular weight of approximately 350. In this example the mol ratio of high molecular weight sulfonic acid to low molecular weight sulfonic acid was 1 to 2 as indicated below in the table. This composition had a good firm consistency as evidenced by its worked penetration of 310, and a high dropping point of 400+F.
EXAMPLE 3 Another sample was made by combining 16 parts by weight 01' the calcium petroleum suli'onate of Example 2 with 4.4 partspf ethane sulfonic acid, 1.8 parts of hydrated lime, and 17.8v parts of the same oil as was also used in Examle 2. 'he grease o thisexample was prepared in substantially the same manner as that of It will be noted that the mol ratio of the higher and lower sulfonates was approximately 1 to 1. The grease had a slightly softer penetration than that of Example 2, but was smooth and transparent in texture and had a dropping point in excess of 400 F.
EXAMPLE 4 A further example was prepared by using 16% by weight of calcium sulfonate prepared from a sulfonic acid having a molecular weight of about 450. To this were added in aqueous solution 3.8% by weight based on the final composition, of ethane sulfonic acid, and 1.6% of hydrated lime. The mineral oil content was 78.6%, the same oil being used as in Examples 2 and 3 above. In this composition the mol ratio of the higher and lower 'sulfonates was 1 to l. The excess alkalinity was considerably lower than in Examples 2 and 3. The grease was somewhat softer, having a worked penetration of 360 but it was smooth and transparent in appearance and had a dropping point in excess of 400 F.
The compositions described above in Examples 2, 3 and 4, were prepared in the same general manner, that is by dissolving the high molecular weight sulfonates in part of the oil, adding the lower sulfonate in an aqueous solution, dehydrating by heating to a temperature in the neighborhood of 300 F. and thereafter adding the remainder of the mineral oil and cooling with stirring to temperature of around 200 F.
The comparative formulas and properties of the calcium sulfonate greases of Examples 2, 3 and 4 are shown in the following table:
Turn 1 Formulae and properties of calcium sulfonate greases EL2 Ex.3 Ex.4
Formula. percent by weight:
Calcium Petroleum Sulionate ll 16 16 Ethane Bulfonic Acid 6 4. 4 3.8 Hydrated Lime. 2.4 1.8 1.6 Mineral 011 80.6 77.8 78.6 Mel. Wt. of Petroleum Bulfonic Add used in 350 350 450 preparation of Calcium Sultanate. Approx. Mol. Ratio of H. M. W. Sullonate to 1:2 1 1 1:1
M.'W. sulfonate. Inspections:
Per Cent Total Free Alkali (as Na0H) 0.6 0. 8 0. 1 Worked Penetration, 17 F 310 340 360 A. S. T. M. Dropping Point, F +400 +400 +4) Appearance 320 s. s. U. at F.;40V.I. 1 Smooth, s1. opaque. 1 Smooth, transparent.
Two further examples were prepared using the same mineral oil as in Examples 2, 3 and 4 by substituting other sulronates for the calcium sulfonates.
EXAMPLE 5 The composition was prepared consisting'oi 16% by weight of oil-soluble barium petroleum sulfonate prepared from the same relatively high molecular weight sulfonic acids as the calcium sulfonates of Examples 2 and 3 above. 4.2% of ethane sulfonic acid and 6.4% of barium hydroxideocta-hydrate were added being combined with 73.4% of mineral oil of 320 S. S. U. at 100 F. and a viscosity index of 40.
The greases of Example 5 had a considerably harder consistency than those of Examples 1 and 4 above. The dropping point, however, was lower, being approximately 260 F. The product was smooth and transparent.
EXAMPLES A soda base grease wa prepared by using 25% of the oil soluble sodium sulfonate prepared from the same acids as Examples 2, 3 and 5 with 11% ethane sultonic acid, 5% sodium hydroxide and Tum 2 Formulae and properties of barium sulfonate and sodium sulfonate greases Formula, per cent by weight:
Barium Petroleum sulfonate Sodium Petroleum Sultanate of high molecular Inspections:
Per cent Total Free Alkali (as NaOH) 1. Worked Penetration, 77 F 215 220 A. S. 'l. M. Dropping Point, "F 200 420 Appearance 3Z0 S. S. U. at 100 F.; 40 V. I. I Smooth, transparent. I Smooth, sl. tacky, transparent.
In general, grease compositions prepared according to the present invention make use of the oil-soluble petroleum sulfonates of commerce. These usually contain petroleum sulfonic acids ranging in molecular weight from 300 to 500 or slightly more. They are usually soluble in mineral oil, becoming very tacky and viscous at high concentrations. On the other hand, the low molecular weight sulfonic acids, such as ethane sulfonic acid, which has a molecular weight of 110, form metallic salts which will not dissolve in oil. Methane sulfonic acid, with a molecular weight of about 96, may be used for preparing the lower molecular weight sulfonate, and other homologues such as propane and butane sulfonate may be used. Mixtures of these and related acids may be used also.
As indicated from the data above, by mixing the salts of high and low molecular weight sulionic acids, the melting point of greases may be raised considerably and their structural stability is improved. The foregoing examples show the use of the calcium, barium, and sodium sulfonates, but it will be understood that other sulfonates, such as zinc, aluminum, lithium, and the like may also be employed. In general, it is preferred that equal or substantially equal molar proportions of the higher and lower sulfonates be used but the invention contemplates the use of various ratios, for example from 1 proportion of high molecular weight sulfonates to 3 of the lower composition on the one hand, to 3 proportions of the high molecular weight compound with 1 proportion of the lower compound.
The quantity of sulfonate employed depends somewhat upon the viscosity of the mineral oil chosen. For a very light mineral oil, it is necessary to use larger quantities of sulfonates to get a suitable grease consistency. On the other hand, when heavy oils are employed, the sulfonate concentrations may be much lower. Thus, for a very heavy oil as little as 5% of the oil soluble sulfonate and about 3% of the non-oil soluble sulfonate will make a grease of reasonable good consistency. For a very light oil, several times as much may be required.
In general, the sulfonate proportions will be between 5 and %7 0f the high molecular weight compound and from about 3 to 20% of the low molecular weight compound. As suggested above the high molecular weight sulfonates are preferably derived from sulfonic acids having an average molecular weight within the general range of about 300 to about 500. Acids having molecular weight of around 400 are particularly preferred. The non-oil soluble sulfonates may be derived from the so-called black or green acids having an average molecular weight less than 300 and preferably between about 96 and 250. Ethane sulfonic acid is specifically preferred fo preparation of the oil insoluble sulionate ingredient. Mineral oils used in such greases should preferably have a viscosity of at least S. S. U. at 100 F. and their viscosity may run as high as 1000 S. S. U. at 210 F.
It will be understood that conventional additives which are commonly used in lubricating greases may be added to the foregoing compositions as will be evident to those skilled in the art. Such additives may comprise the usual antioxidants, rust inhibitors, tackiness agents,
viscosity index improvers, extreme pressure Ill) of mineral lubricating oil containing 5 to 25% byv weight, based on the total composition, of an oil soluble sulfonate having a sullonate radical molecular weight of more than 300 and not substantially greater than about 500, and 3 to 20% of a non-oil soluble sulfonate of a sulfonic acid having a molecular weight between 96 and 250, the combined sulfonates being effective to impart a grease-like consistenc to said oil.
2. A lubricating grease composition of high melting point consisting essentially of a mineral base lubricating oil of viscosity within the range of 60 S. S. U. at 100 F. to 1000 S. S. U. at 210 F., said oil containing 5 to 25%, by weight based on the final composition, of an oil soluble metal sulfonate having a sulfonate radical molecular weight of more than 300 and not substantially greater than about 500 and 3 to 20% of an oil insoluble metal alkyl sulfonate of a sulfonic acid having a molecular weight between 96 and 250.
3. Composition as in claim 2 wherein said oil soluble sulfonate is an alkaline earth metal salt of sulfonic acids having an average molecular weight between about 300 and about 500.
4. Composition as in claim 2 wherein said oil soluble sulionate is the calcium salt of petroleum sulfonic acids having an average molecular weight between about 300 and about 500.
5. Composition as in claim 2 wherein said oil soluble sulionate is the barium salt of sulfonic acids having an average molecular weight between about 300 and about 500.
6. Composition as in claim 2 wherein said oil soluble sulfonate is the sodium salt of sulfonic acids having an average molecular weight between about 300 and about 500.
7. Composition as in claim 2 wherein said oil insoluble sulfonate is the sodium salt of sulfonic acid having an average molecular Weight between about 96 and 250.
8. A lubricating grease composition of high melting point consisting essentially of a mineral base lubricating oil of viscosity between 60 S. S. U. at 100 F. and 1000 S. S. U. at 210 F., 5 to 25% by weight, based on the ijnal composition, of substantially equimolar of the calcium salt of sulionic acid having an average molecular weight of between 300 and 400, and the calcium salt of ethane sulfonic acid, the combined quantities of sulfonates being sufficient to impart a grease like consistency to said oil.
9. Composition according to claim 1 containing an excess of metal base beyond that required to neutralize the acids of said sulfonates.
LORNE W. SPROULE. WARREN C. PATTENDEN.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Number Name Date 2,111,907 Zimmer et a1 Mar. 22, 1938 2,113,754 Zimmer et al Apr. 12, 1938 2,265,791 Zimmer et a1 Dec. 9, 1941 2,352,811 Swensen July 4, 1944 2,358,939 Nelson et al Sept. 26, 1944 2,394,790 Liehe Feb. 12, 1946 2,398,075 Brunstrum et al Apr. 9, 1946 2,417,429 McLennan Mar. 18, 1947 2,445,936 Bertcook July 2'7, 1948

Claims (1)

1. A GREASE COMPOSITION CONSISTING ESSENTIALLY OF MINERAL LUBRICATING OIL CONTAINING 5 TO 25% BY WEIGHT, BASED ON THE TOTAL COMPOSITION, OF AN OIL SOLUBLE SULFONATE HAVING A SULFONATE RADICAL MOLECULAR WEIGHT OF MORE THAN 300 AND NOT SUBSTANTIALLY GREATER THAN ABOUT 500, AND 3 TO 20% OF A NON-OIL SOLUBLE SULFONATE OF A SULFONIC ACID HAVING A MOLECULAR WEIGHT BETWEEN 96 AND 250, THE COMBINED SULFONATES BEING EFFECTIVE TO IMPART A GREASE-LIKE CONSISTENCY TO SAID OIL.
US15747A 1948-03-18 1948-03-18 Sulfonate base lubricating grease Expired - Lifetime US2535101A (en)

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FR977911D FR977911A (en) 1948-03-18
US15747A US2535101A (en) 1948-03-18 1948-03-18 Sulfonate base lubricating grease
GB31031/48A GB668078A (en) 1948-03-18 1948-11-30 Sulfonate base lubricating greases

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Cited By (22)

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US2620301A (en) * 1950-12-09 1952-12-02 Standard Oil Co Grease compositions
US2659695A (en) * 1951-01-06 1953-11-17 Sonneborn Sons Inc L Lubricating greases
DE949678C (en) * 1952-01-02 1956-09-27 Standard Oil Dev Co Grease
US2823182A (en) * 1950-10-28 1958-02-11 Standard Oil Co Grease compositions
US2854408A (en) * 1955-11-07 1958-09-30 Exxon Research Engineering Co Lubricating grease compositions containing aliphatic sulfonic acid soap
US2856362A (en) * 1956-04-24 1958-10-14 Exxon Research Engineering Co Lubricating compositions
US2913410A (en) * 1955-08-11 1959-11-17 Gulf Oil Corp Soluble oil
US2947694A (en) * 1955-10-06 1960-08-02 Phillips Petroleum Co Preparation of metal petroleum sulfonates
US2987477A (en) * 1958-12-29 1961-06-06 Texaco Inc Lubricating greases containing metal salts of nu-alkanoyl-sulfanilic acids
US3121687A (en) * 1958-06-30 1964-02-18 Sinclair Research Inc Lubricating oil compositions containing sulfonates
US4261840A (en) * 1979-04-17 1981-04-14 Phillips Petroleum Company Grease composition and preparation thereof
US4368130A (en) * 1979-04-17 1983-01-11 Phillips Petroleum Company Process of preparing grease composition
US9273265B2 (en) 2011-10-31 2016-03-01 Nch Corporation Calcium carbonate based sulfonate grease compositions and method of manufacture
US9458406B2 (en) 2011-10-31 2016-10-04 Nch Corporation Calcium hydroxyapatite based sulfonate grease compositions and method of manufacture
US9976101B2 (en) 2011-10-31 2018-05-22 Nch Corporation Method of manufacturing calcium sulfonate greases using delayed addition of non-aqueous converting agents
US9976102B2 (en) 2011-10-31 2018-05-22 Nch Corporation Composition and method of manufacturing calcium sulfonate greases using alkali metal hydroxide and delayed addition of non-aqueous converting agents
US10087388B2 (en) 2016-05-18 2018-10-02 Nch Corporation Composition and method of manufacturing calcium sulfonate and calcium magnesium sulfonate greases using a delay after addition of facilitating acid
US10087387B2 (en) 2016-05-18 2018-10-02 Nch Corporation Composition and method of manufacturing calcium magnesium sulfonate greases
US10087391B2 (en) 2016-05-18 2018-10-02 Nch Corporation Composition and method of manufacturing calcium magnesium sulfonate greases without a conventional non-aqueous converting agent
US10392577B2 (en) 2016-05-18 2019-08-27 Nch Corporation Composition and method of manufacturing overbased sulfonate modified lithium carboxylate grease
US10519393B2 (en) 2016-05-18 2019-12-31 Nch Corporation Composition and method of manufacturing calcium magnesium sulfonate greases
US11661563B2 (en) 2020-02-11 2023-05-30 Nch Corporation Composition and method of manufacturing and using extremely rheopectic sulfonate-based greases

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US2111907A (en) * 1934-08-03 1938-03-22 Standard Oil Dev Co Grease composition
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US2111907A (en) * 1934-08-03 1938-03-22 Standard Oil Dev Co Grease composition
US2113754A (en) * 1935-06-06 1938-04-12 Standard Oil Dev Co Lubricating composition
US2265791A (en) * 1939-04-06 1941-12-09 Standard Oil Dev Co Grease composition and method for making same
US2358939A (en) * 1940-11-08 1944-09-26 Texas Co Lubricants
US2352811A (en) * 1941-06-27 1944-07-04 Standard Oil Co Lubricant
US2394790A (en) * 1942-05-29 1946-02-12 Standard Oil Co Greases
US2398075A (en) * 1943-07-21 1946-04-09 Standard Oil Co Grease manufacture
US2417429A (en) * 1945-04-16 1947-03-18 Union Oil Co Complex basic soap greases
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Cited By (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2823182A (en) * 1950-10-28 1958-02-11 Standard Oil Co Grease compositions
US2620301A (en) * 1950-12-09 1952-12-02 Standard Oil Co Grease compositions
US2659695A (en) * 1951-01-06 1953-11-17 Sonneborn Sons Inc L Lubricating greases
DE949678C (en) * 1952-01-02 1956-09-27 Standard Oil Dev Co Grease
US2913410A (en) * 1955-08-11 1959-11-17 Gulf Oil Corp Soluble oil
US2947694A (en) * 1955-10-06 1960-08-02 Phillips Petroleum Co Preparation of metal petroleum sulfonates
US2854408A (en) * 1955-11-07 1958-09-30 Exxon Research Engineering Co Lubricating grease compositions containing aliphatic sulfonic acid soap
US2856362A (en) * 1956-04-24 1958-10-14 Exxon Research Engineering Co Lubricating compositions
US3121687A (en) * 1958-06-30 1964-02-18 Sinclair Research Inc Lubricating oil compositions containing sulfonates
US2987477A (en) * 1958-12-29 1961-06-06 Texaco Inc Lubricating greases containing metal salts of nu-alkanoyl-sulfanilic acids
US4261840A (en) * 1979-04-17 1981-04-14 Phillips Petroleum Company Grease composition and preparation thereof
US4368130A (en) * 1979-04-17 1983-01-11 Phillips Petroleum Company Process of preparing grease composition
US9273265B2 (en) 2011-10-31 2016-03-01 Nch Corporation Calcium carbonate based sulfonate grease compositions and method of manufacture
US9458406B2 (en) 2011-10-31 2016-10-04 Nch Corporation Calcium hydroxyapatite based sulfonate grease compositions and method of manufacture
US9976101B2 (en) 2011-10-31 2018-05-22 Nch Corporation Method of manufacturing calcium sulfonate greases using delayed addition of non-aqueous converting agents
US9976102B2 (en) 2011-10-31 2018-05-22 Nch Corporation Composition and method of manufacturing calcium sulfonate greases using alkali metal hydroxide and delayed addition of non-aqueous converting agents
US10316266B2 (en) 2011-10-31 2019-06-11 Nch Corporation Calcium hydroxyapatite based calcium sulfonate grease compositions and method of manufacture
US11072756B2 (en) 2011-10-31 2021-07-27 Nch Corporation Calcium hydroxyapatite based calcium sulfonate grease compositions and method of manufacture
US10087388B2 (en) 2016-05-18 2018-10-02 Nch Corporation Composition and method of manufacturing calcium sulfonate and calcium magnesium sulfonate greases using a delay after addition of facilitating acid
US10087387B2 (en) 2016-05-18 2018-10-02 Nch Corporation Composition and method of manufacturing calcium magnesium sulfonate greases
US10087391B2 (en) 2016-05-18 2018-10-02 Nch Corporation Composition and method of manufacturing calcium magnesium sulfonate greases without a conventional non-aqueous converting agent
US10392577B2 (en) 2016-05-18 2019-08-27 Nch Corporation Composition and method of manufacturing overbased sulfonate modified lithium carboxylate grease
US10519393B2 (en) 2016-05-18 2019-12-31 Nch Corporation Composition and method of manufacturing calcium magnesium sulfonate greases
US11168277B2 (en) 2016-05-18 2021-11-09 Nch Corporation Composition and method of manufacturing calcium magnesium sulfonate greases
US11661563B2 (en) 2020-02-11 2023-05-30 Nch Corporation Composition and method of manufacturing and using extremely rheopectic sulfonate-based greases

Also Published As

Publication number Publication date
GB668078A (en) 1952-03-12
FR977911A (en) 1951-04-06

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