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US2450221A - Shear-resistant grease - Google Patents

Shear-resistant grease Download PDF

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Publication number
US2450221A
US2450221A US611908A US61190845A US2450221A US 2450221 A US2450221 A US 2450221A US 611908 A US611908 A US 611908A US 61190845 A US61190845 A US 61190845A US 2450221 A US2450221 A US 2450221A
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grease
lubricating
soap
compounds
grams
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US611908A
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Harry V Ashburn
Robert S Barnett
Oney P Puryear
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Texaco Inc
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Texaco Inc
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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
    • C10M7/00Solid or semi-solid compositions essentially based on lubricating components other than mineral lubricating oils or fatty oils and their use as lubricants; Use as lubricants of single solid or semi-solid substances
    • 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
    • C10M3/00Liquid compositions essentially based on lubricating components other than mineral lubricating oils or fatty oils and their use as lubricants; Use as lubricants of single liquid substances
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/02Hydroxy compounds
    • C10M2207/021Hydroxy compounds having hydroxy groups bound to acyclic or cycloaliphatic carbon atoms
    • C10M2207/022Hydroxy compounds having hydroxy groups bound to acyclic or cycloaliphatic carbon atoms containing at least two hydroxy groups
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/10Carboxylix acids; Neutral salts thereof
    • C10M2207/12Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms
    • C10M2207/125Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms having hydrocarbon chains of eight up to twenty-nine carbon atoms, i.e. fatty acids
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/10Carboxylix acids; Neutral salts thereof
    • C10M2207/12Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms
    • C10M2207/129Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms having hydrocarbon chains of thirty or more carbon atoms
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/28Esters
    • C10M2207/282Esters of (cyclo)aliphatic oolycarboxylic acids
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/28Esters
    • C10M2207/34Esters having a hydrocarbon substituent of thirty or more carbon atoms, e.g. substituted succinic acid derivatives
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2209/00Organic macromolecular compounds containing oxygen as ingredients in lubricant compositions
    • C10M2209/10Macromolecular compoundss obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • C10M2209/103Polyethers, i.e. containing di- or higher polyoxyalkylene groups
    • C10M2209/104Polyethers, i.e. containing di- or higher polyoxyalkylene groups of alkylene oxides containing two carbon atoms only
    • 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
    • C10M2215/00Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant compositions
    • C10M2215/02Amines, e.g. polyalkylene polyamines; Quaternary amines
    • C10M2215/06Amines, e.g. polyalkylene polyamines; Quaternary amines having amino groups bound to carbon atoms of six-membered aromatic rings
    • C10M2215/064Di- and triaryl amines
    • C10M2215/065Phenyl-Naphthyl amines
    • 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
    • C10M2229/00Organic macromolecular compounds containing atoms of elements not provided for in groups C10M2205/00, C10M2209/00, C10M2213/00, C10M2217/00, C10M2221/00 or C10M2225/00 as ingredients in lubricant compositions
    • C10M2229/04Siloxanes with specific structure
    • C10M2229/041Siloxanes with specific structure containing aliphatic substituents
    • 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
    • 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
    • C10N2010/02Groups 1 or 11
    • 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
    • C10N2020/00Specified physical or chemical properties or characteristics, i.e. function, of component of lubricating compositions
    • C10N2020/01Physico-chemical properties
    • 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
    • C10N2040/02Bearings
    • 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 choice of the particular compounds used in the preparation of the synthetic grease depends upon the type of lubrication and the temperature range within which the grease is intended to be operated. In general, these compounds are adapted to specialized lubrication outside the conventional lubricating temperature ranges, such as ultra low temperature operation found .in refrigeration systems and arctic service lubrication, or to general purpose lubrication over a wide lubricating temperature range which was previously unattainable through the use of a single mineral lubricating oil due to their high viscosity change over such wide temperature ranges.
  • oleaginous compounds Inasmuch as the primary requisites of the oleaginous compounds are physical in nature, they cannot be conclusively defined in terms of their chemical structure. However, the majority of these compounds are polar compounds with oxygen as the principal type of polar constituent. Another general observation is that, in the compounds of a given chemical classification, those of comparatively high molecular weight possess the least change in viscosity per change in temperature.
  • the types of compounds which are recognized or have been proposed as synthetic oleaginous compounds include the aliphatic ethers, aromatic acid esters, aliphatic monoand di-carboxylic acid esters, phosphorus acid esters, and halogenated aromatic compounds.
  • esters for the purposes of the present invention and as illustrative of the synthetic oleaginous compounds contemplated by the invention, those compounds falling within the category of aliphatic dicarboxylic acid esters are preferred.
  • the compounds within this particular class are the esters of such acids as sebacic, adipic, pimelic, azelaic, alkenylsuccinic, alkylmaieic, etc.
  • the esters thereof are preferably the aliphatic esters and particularly the branched chain aliphatic esters.
  • the preferred oleaginous compounds are di-Z-ethylhexyl sebacate, di-sec-amyl seba- 'cate, di-z-ethylhexyl alkenylsuccinate, di-2- ethoxyethyl sebacate, di-2-(2'-methoxyethoxy) ethyl sebacate (di-methylcarbitol sebacate) di-2- (W-ethylbutoxy) ethyl sebacate, di-2-butoxyethyl azelate (di-butylcellosolve azelate), di-2-(2'- butoxyethoxy) ethyl alkenyl succinate (di-butylcarbitol alkenylsuccinate), trlethylidene sorbitol, di-2-butoxyethyl alkenyl succinate(di-butylcellosolve alkenylsuccinate),
  • oleaginous compounds may be used as the sole oil component of the greases or they may be blended with a mineral lubricating oil as desired.
  • soap component is to be formed in situ it is desirable to conduct the saponification in the presence of mineral oil which is inert to the reaction and then add the oleaginou compound. This would result in the combination of mineral oil and oleaginous compound as the oil component of the finished grease.
  • various addition agents may be incorporated with the ole aginous compounds to impart other desirable characteristics.
  • an extreme pressure agent may be incorporated to improve the anti-wear characteristics of the compound or an antioxidant may be incorporated to improve the antioxidant properties of the compound and/or the finished grease.
  • the metal soaps which have been found to contribute to the desirable attributes of the synthetic greases are those in which a soap-forming hydroxy fatw acid constitutes at least part of the acid component.
  • the soap-forming hydroxy fatty acids contemplated herein are those containing at least 12 carbon atoms in the molecue and one or more hydroxy] groups separated from the carboxyl group by at least one carbon atom, as well as mixtures thereof.
  • These hydroxy fatty acids may be obtained from natural sources, such as castor oil, or may be prepared by the classical synthetic methods, such as oxidation of unsaturated fatty acids or catalytic oxidation of petroleum oils and waxes with extraction and fractionation to the desired molecular range.
  • 12-hydroxy stearic acid and hydrogenated castor oil will be used as the representative types of hydroxy fatty acids and their glycerides.
  • the soap-forming hydroxy fatty acids may be used as the sole acidic component of the metal soaps or they may be blended or combined with the conventional fats or fatty acids in such proportions that at least 50% of the total acidic component is comprised of the hydroxy fatty acids.
  • the choice of fats or fatty acids and the specific proportion thereof which may be blended or combined with the hydroxy fatty acids depends upon the particular metallic constituent and the type of service for which the synthetic grease is intended. In general, any of the recognized fatty acid materials normally used in grease manufacture may be used providing they are essentially saturated in character.
  • acids include mixtures of fatty acid glycerides found in naturally-occurring fat and oils, together with fractionated components thereof.
  • the fatty acids may be a mixture of acids split These fats and fatty of! from these fats or prepared from hydrogenathin of fish oils, etc or the individual acids themse ves.
  • the metallic constituent of the soaps of hydroxy fatty acid may be any of the metals normally used in the production of thickening agents for lubricating oils, such as Na, Li, Ca, Ba, Al, etc., as well as mixtures thereof.
  • the choice of the metallic constituent is dependent upon the physical properties desired in the finished grease, such as dropping point, water resistance, texture, etc.
  • the metals preferred are the alkali metals, sodium and lithium.
  • the choice of the particular methods of manufacture applicable to the production of the synthetic greases of the invention will depend upon the type of oleaginous compound used and whether or not mineral oil is to be used as part of the oil component.
  • the conventional method of preparing synthetic greases is the gelling method in which the preformed metal soap and the oleaginou compound are heated to a homogeneous solution and rapidly cooled to form the grease gel.
  • This method of preparation possesses certain disadvantages in that it requires a preformed metal soap which in and of itself raises the cost of the grease because of the separate saponification step required and extensive milling equipment to work the grease gel to a homogeneous consistency.
  • other methods of manufacture conventional to the grease industry, may be used.
  • a particular advantage in the use of metal soaps of hydroxy fatty acids is the fact that the high temperatures required by the conventional gelling methods may be avoided and the preparation conducted at temperatures around 300 F. or at least those attained in a steam-heated kettle and the finished grease drawn from the kettle without requiring homogenization. Furthermore, saponification in situ is possible either in the presence of mineral oil or a synthetic oleaginous compound which i inert to the saponification reaction.
  • Example I A steam-heated kettle equipped with stirring mechanism was charged with 16.8 pounds of 10.4% lithium hydroxide solution and 9.0 pounds of water. Stirring was started at 35 R; P. M. and the lithium hydroxide solution heated to 180 F. 16.2 pounds of hydrogenated castor oil (Titer- 74.6 C., Sap. No.-183, hydroxyl value) and 22.6 pounds of a mildly refined mineral oil were then added. The kettle contents were held at F. for four hours and 5.52 pounds of triple pressed stearic acid were added. The temperature was then maintained at 186-190 F. for an additional hour and the kettle shut down over night. After standing over night stirring at 35 R. P. M. was begun and the saponification mixture dehydrated at 290312 F. for four hours. At this point the soap had a very light tan color. The heat was then reduced and 12.2 pounds of mineral oil were added. The physical tests on the mineral oil and synthetic oleaginous compound are as follows:
  • the foregoing synthetic grease was subjected to a dynamic shear test which was conducted in an apparatus consisting of a perforated piston reciprocating within a closed cylinder maintained at a constant temperature.
  • the grease was charged to the cylinder at a temperature of 225 F., and the fiston then reciprocated at 49 strokes per minute for a period of eight hours.
  • the grease was removed and miniature penetrations taken. These miniature penetrations were then compared with the miniature penetrations of the grease taken before the test to determine the eilect of the 750 grams of the grease base were charged to a kettle and heated with stirring at 234 F.
  • the subject rease was tested in a so-called grease-breakdown machine wherein a No. 204 anti-friction hearing was packed with the grease and mounted on a motor-driven shaft operating at 3450 R. P. M. and surrounded by a heating jacket, The test was started at room temperature and the bearing radually heated, while running at a constant speed, until the temperature reached 300' F. During the period of the test the lubricating performance was noted. At the conclusion of the test the grease was removed from the bearing and examined as to change in texture and consistency.
  • a lubricating grease comprising a liquid silicone polymer within the lubricating viscosity range as shearing action on the grease structure.
  • the resuits obtained on the subject grease showed an original miniature penetration of 89 and a final miniature penetration of 113.
  • a lubricating grease comprising a high molecular weight aliphatic dicarboxylic acid ester as the lubricating base, together with sufllcient
  • a grease base consisting of the lithium soaps of the combination of 75% hydrogenated castor oil and 25% triple-pressed stearic acid and mineral oil was prepared in accordance with the procedure of Example I. This grease base possessed the following calculated composition:
  • the lubricant base together with sumcient metal soap of a soap-forming hydroxy fatty acid or glyceride, and more specifically the grease of;
  • Example III 100 grams of lithium 12-hydroxy stearate and 900 grams of di-2-ethylhexyl sebacate were mixed and heated with stirring. At 350 F. the soap began to dissolve in the ester and at 390 F. was completely in solution. The solution was heated to 400 F. and poured in a thin layer on the bottom of a grease pan, taking care that no thick spots were formed. After cooling, a smooth, buttery gel was formed which showed no signs of separation. The ASTM control worked penetration of the grease gel was 240 at 77 F. The product possessed the following calculated composition:
  • Example IV The kettle was charged with 225 grams of hydrogenated castor oil, 200 grams of mineral oil whose characteristics are set forth in Example I, and 200 grams of water. The mixture was then heated with stirring to 210 F. 88.8 grams of a 45.9% sodium hydroxide solution were 1 then added over a period of one-half hour. At this point the saponiflcation mixture in the kettle was a white, soft dough. Stirring was continued for an additional hour at 186-192 F. and 75 grams of triple-pressed stearic acid added. After stirring for one and one-quarter hours the heat was turned on to dehydrate the soap base at 308 F. and a white, tough, fibrous base was formed. This base was held at 280-308 F. for one-half hour.
  • a lubricating grease composition comprising as the essential and at least major portion of the lubricating base a high molecular weight high boiling liquid aliphatic dicarboxylic acid ester within the lubricating oil viscosity rangeand possessing lubricating properties. and suflicient metal soap of a soap-forming fatty material selected from the group consisting of hydroxy fatty acids and hydroxy fatty acid glycerides to thicken said lubricating base, said grease composition being texture-stable under high shearing stress.
  • a lubricating grease composition comprising essentially a lubricating base consisting of at least a major proportion of an oil-soluble high molecular weight high boiling liquid aliphatic dicarboxylic acid ester within the lubricating oil viscosity range and possessing lubricating properties and not more than a minor proportion of mineral lubricating oil, sufllcient metal soap of a soap-forming fatty material containing at least 50% by weight on the basis of the fatty material of hydrogenated castor oil to thicken said lubricating base, glycerine, and a small amount or an oxidation inhibitor.
  • a lubricating grease composition comprising essentially a lubricating base consisting of a major proportion of di-z-ethylhexyl sebacate and a minor proportion of mineral lubricating oil, suiiicient metal soap of hydrogenated castor oil to thicken said lubricating base, glycerine, and a small proportion of an oxidation inhibitor.
  • said metal soap is a sodium soap
  • said oxidation inhibitor is phenyl alpha naphthylamine.

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

Description

Patented Sept. 1948 UNITED STATES PATENT l OFFICE SHEAR-RESISTANT GREASE Harry V. Ashburn, Glenham,Robert S. Barnett, Beacon, and Oney P. Puryear, Fishkill, N. Y., assignors-to The Texas Company, New York, N. Y., a corporation of Delaware No Drawing. Application August 21, 1945, Serial No. 611,908
8 Claims. 1
compounds offer a marked advantage over the mineral oils in that they possess a comparatively uniform viscosity over a wide temperature range and are not as susceptible to evaporation loss as a comparable viscosity mineral oil. These features areparticularlvdesirable and have been used to advantage in the production of greases used in sealed life-time bearing installations and low temperature greases used in aircraft controls and the like. However, one undesirable characteristic of these so-called synthetic greases is their lack of resistance to shear. Under conditions of operation where high shearing stresses are involved, such as in ball and roller-bearing lubrication, the structure of these greases gradually breaks down and their consistency falls off until they become liquid or semi-liquid. At this point the greases no longer adhere to the lubricating surfaces and bearing failures result.
In accordance with the present invention it has been found possible to produce a synthetic grease composition which possesses not only the desirable characteristics imparted by the oleaginous'compounds, but is also resistant to shear. The synthetic greases previously proposed and accepted by the industry have been prepared from the metal soaps of the conventional fatty acid sources, such as stearic acid and other soap-forming fatty acids or their glycerides. It has been discovered that the acid component of the metal soap is an important factor in the production of synthetic greases and that synthetic greases pro- 2 7 compounds or mixtures thereof which possess lubricating qualities and may be substituted in whole or in part for the conventional mineral lubricating oils. The choice of the particular compounds used in the preparation of the synthetic grease depends upon the type of lubrication and the temperature range within which the grease is intended to be operated. In general, these compounds are adapted to specialized lubrication outside the conventional lubricating temperature ranges, such as ultra low temperature operation found .in refrigeration systems and arctic service lubrication, or to general purpose lubrication over a wide lubricating temperature range which was previously unattainable through the use of a single mineral lubricating oil due to their high viscosity change over such wide temperature ranges.
As a general proposition, certain factors are prerequisite in the compounds falling within the category 'of synthetic oleaginous compounds. These compounds are necessarily chemically and physically stable liquids at the temperatures of operation and possess a minimum viscosity of 0.5 centistoke within the lubricating temperature range. Furthermore, the vapor pressure of these compounds in the lubricating temperature range are substantially negligible, although under conditions of flooded lubrication, where evaporation loss is not too critical, compounds of measurable vapor pressure may be used.
Inasmuch as the primary requisites of the oleaginous compounds are physical in nature, they cannot be conclusively defined in terms of their chemical structure. However, the majority of these compounds are polar compounds with oxygen as the principal type of polar constituent. Another general observation is that, in the compounds of a given chemical classification, those of comparatively high molecular weight possess the least change in viscosity per change in temperature. The types of compounds which are recognized or have been proposed as synthetic oleaginous compounds include the aliphatic ethers, aromatic acid esters, aliphatic monoand di-carboxylic acid esters, phosphorus acid esters, and halogenated aromatic compounds. For the purposes of the present invention and as illustrative of the synthetic oleaginous compounds contemplated by the invention, those compounds falling within the category of aliphatic dicarboxylic acid esters are preferred. The compounds within this particular class are the esters of such acids as sebacic, adipic, pimelic, azelaic, alkenylsuccinic, alkylmaieic, etc. The esters thereof are preferably the aliphatic esters and particularly the branched chain aliphatic esters. Specific examples of the preferred oleaginous compounds are di-Z-ethylhexyl sebacate, di-sec-amyl seba- 'cate, di-z-ethylhexyl alkenylsuccinate, di-2- ethoxyethyl sebacate, di-2-(2'-methoxyethoxy) ethyl sebacate (di-methylcarbitol sebacate) di-2- (W-ethylbutoxy) ethyl sebacate, di-2-butoxyethyl azelate (di-butylcellosolve azelate), di-2-(2'- butoxyethoxy) ethyl alkenyl succinate (di-butylcarbitol alkenylsuccinate), trlethylidene sorbitol, di-2-butoxyethyl alkenyl succinate(di-butylcellosolve alkenylsuccinate), etc.
These oleaginous compounds may be used as the sole oil component of the greases or they may be blended with a mineral lubricating oil as desired. In some instances where the soap component is to be formed in situ it is desirable to conduct the saponification in the presence of mineral oil which is inert to the reaction and then add the oleaginou compound. This would result in the combination of mineral oil and oleaginous compound as the oil component of the finished grease. Furthermore, various addition agents may be incorporated with the ole aginous compounds to impart other desirable characteristics. Thus, an extreme pressure agent may be incorporated to improve the anti-wear characteristics of the compound or an antioxidant may be incorporated to improve the antioxidant properties of the compound and/or the finished grease.
The metal soaps which have been found to contribute to the desirable attributes of the synthetic greases are those in which a soap-forming hydroxy fatw acid constitutes at least part of the acid component. The soap-forming hydroxy fatty acids contemplated herein are those containing at least 12 carbon atoms in the molecue and one or more hydroxy] groups separated from the carboxyl group by at least one carbon atom, as well as mixtures thereof. These hydroxy fatty acids may be obtained from natural sources, such as castor oil, or may be prepared by the classical synthetic methods, such as oxidation of unsaturated fatty acids or catalytic oxidation of petroleum oils and waxes with extraction and fractionation to the desired molecular range. In the practice of the invention, as described herein, 12-hydroxy stearic acid and hydrogenated castor oil will be used as the representative types of hydroxy fatty acids and their glycerides.
These acid are preferred because of their advantage of availability and cost which renders them competitive to the conventional fats and fatty acids.
The soap-forming hydroxy fatty acids may be used as the sole acidic component of the metal soaps or they may be blended or combined with the conventional fats or fatty acids in such proportions that at least 50% of the total acidic component is comprised of the hydroxy fatty acids. The choice of fats or fatty acids and the specific proportion thereof which may be blended or combined with the hydroxy fatty acids depends upon the particular metallic constituent and the type of service for which the synthetic grease is intended. In general, any of the recognized fatty acid materials normally used in grease manufacture may be used providing they are essentially saturated in character. acids include mixtures of fatty acid glycerides found in naturally-occurring fat and oils, together with fractionated components thereof. The fatty acids may be a mixture of acids split These fats and fatty of! from these fats or prepared from hydrogenathin of fish oils, etc or the individual acids themse ves.
The metallic constituent of the soaps of hydroxy fatty acid may be any of the metals normally used in the production of thickening agents for lubricating oils, such as Na, Li, Ca, Ba, Al, etc., as well as mixtures thereof. In many respects, the choice of the metallic constituent is dependent upon the physical properties desired in the finished grease, such as dropping point, water resistance, texture, etc. For the purpose of the present invention the metals preferred are the alkali metals, sodium and lithium.
The choice of the particular methods of manufacture applicable to the production of the synthetic greases of the invention will depend upon the type of oleaginous compound used and whether or not mineral oil is to be used as part of the oil component. The conventional method of preparing synthetic greases is the gelling method in which the preformed metal soap and the oleaginou compound are heated to a homogeneous solution and rapidly cooled to form the grease gel. This method of preparation possesses certain disadvantages in that it requires a preformed metal soap which in and of itself raises the cost of the grease because of the separate saponification step required and extensive milling equipment to work the grease gel to a homogeneous consistency. However, in preparing the greases of the invention other methods of manufacture, conventional to the grease industry, may be used. A particular advantage in the use of metal soaps of hydroxy fatty acids is the fact that the high temperatures required by the conventional gelling methods may be avoided and the preparation conducted at temperatures around 300 F. or at least those attained in a steam-heated kettle and the finished grease drawn from the kettle without requiring homogenization. Furthermore, saponification in situ is possible either in the presence of mineral oil or a synthetic oleaginous compound which i inert to the saponification reaction.
The following examples are presented as illustrating the preparation of representative synthetic greases falling within the scope of the present invention. It is to be understood, however, that these examples are merely illustrative and not definitive of the invention and as such may be modified within the scope of the invention as previously defined in accordance with the skill of the art.
Example I A steam-heated kettle equipped with stirring mechanism was charged with 16.8 pounds of 10.4% lithium hydroxide solution and 9.0 pounds of water. Stirring was started at 35 R; P. M. and the lithium hydroxide solution heated to 180 F. 16.2 pounds of hydrogenated castor oil (Titer- 74.6 C., Sap. No.-183, hydroxyl value) and 22.6 pounds of a mildly refined mineral oil were then added. The kettle contents were held at F. for four hours and 5.52 pounds of triple pressed stearic acid were added. The temperature was then maintained at 186-190 F. for an additional hour and the kettle shut down over night. After standing over night stirring at 35 R. P. M. was begun and the saponification mixture dehydrated at 290312 F. for four hours. At this point the soap had a very light tan color. The heat was then reduced and 12.2 pounds of mineral oil were added. The physical tests on the mineral oil and synthetic oleaginous compound are as follows:
At 236 F. 160 grams of triple-pressed stearic acid were added to render the grease slightly acidic. 26 pounds of di-Z-ethylhexyl sebacate were then added slowly. At approximately 190 F. 36.60 pounds of additional di-2-ethylhexyl sebacate were added and during theaddition of the ester. 196.3 grams of phenyl alpha naphthylamine were added simultaneously. At this point the grease contained approximately ,soap and possessed an ASTM penetration at 77 F. of 301-303 unworked and 317-324 worked. 5 pounds of a blend of 28% mineral oil and 72% sebacate ester and 23 grams of phenyl alpha naphthylamine were then added. The grease was finally drawn at a temperature of 166 F. and pumped through three 60 mesh screens. The product was a light cream-colored buttery grease having the following calculated composition:
' Per cent Lithium soap (75% hydroxy stearic acid,
25% stearic acid) 13.6 Glycerine 1.0 Mineral oil 23.8 Di-Z-ethylhexyl sebacate 60.9 Phenyl alpha naphthylamine 0.5 Free fatty acid 0.2
The foregoing synthetic grease was subjected to a dynamic shear test which was conducted in an apparatus consisting of a perforated piston reciprocating within a closed cylinder maintained at a constant temperature. In the test the grease was charged to the cylinder at a temperature of 225 F., and the fiston then reciprocated at 49 strokes per minute for a period of eight hours. At the conclusion of the run the grease was removed and miniature penetrations taken. These miniature penetrations were then compared with the miniature penetrations of the grease taken before the test to determine the eilect of the 750 grams of the grease base were charged to a kettle and heated with stirring at 234 F. The heat was then reduced and 1020 grams of a dimethyl silicone polymer possessing a flash point above 600 F., with a kinematic viscosity of 82 cs. at 100 F. and 32 cs. at 210 F. were slowly added over a period of six and one-half hours. At this point the temperature was 147 F. and the ASTM control penetration at 77 was 203-210 un- .Percent Lithium soap 12.8 'Glycerine 0.9 Mineral oil- 13.4 Dimethyl silicone polymer 72.9
The subject rease was tested in a so-called grease-breakdown machine wherein a No. 204 anti-friction hearing was packed with the grease and mounted on a motor-driven shaft operating at 3450 R. P. M. and surrounded by a heating jacket, The test was started at room temperature and the bearing radually heated, while running at a constant speed, until the temperature reached 300' F. During the period of the test the lubricating performance was noted. At the conclusion of the test the grease was removed from the bearing and examined as to change in texture and consistency. The results obtained on the subject grease indicated excellent lubrication, with no appreciable change in texture or consistency of the grease at the conclusion of the though supplying excellent lubrication, the grease became semi-fluid toward the end of the test and drained from the hearing when the test was stopped.
A lubricating grease comprising a liquid silicone polymer within the lubricating viscosity range as shearing action on the grease structure. The resuits obtained on the subject grease showed an original miniature penetration of 89 and a final miniature penetration of 113.
A lubricating grease comprising a high molecular weight aliphatic dicarboxylic acid ester as the lubricating base, together with sufllcient Example If A grease base consisting of the lithium soaps of the combination of 75% hydrogenated castor oil and 25% triple-pressed stearic acid and mineral oil was prepared in accordance with the procedure of Example I. This grease base possessed the following calculated composition:
Per cent Lithium soap 47.2 Glycerine 3.5 Mineral on 49.3
the lubricant base, together with sumcient metal soap of a soap-forming hydroxy fatty acid or glyceride, and more specifically the grease of; the
foregoing example, is disclosed and claimed in our co-pending application, Serial No. 20,606, filed April 12, 1948.
Example III 100 grams of lithium 12-hydroxy stearate and 900 grams of di-2-ethylhexyl sebacate were mixed and heated with stirring. At 350 F. the soap began to dissolve in the ester and at 390 F. was completely in solution. The solution was heated to 400 F. and poured in a thin layer on the bottom of a grease pan, taking care that no thick spots were formed. After cooling, a smooth, buttery gel was formed which showed no signs of separation. The ASTM control worked penetration of the grease gel was 240 at 77 F. The product possessed the following calculated composition:
Percent Lithium iz-hydroxystearate 10 DI-Z-ethylheawl sebacate This grease was tested in the dynamic shear test described in Example I-in comparison with a 10% lithium stearate grease containing (ii-2- Lithium Miniature Penetration lgy to gm m 130 m. gaifiiil 2681279 Semi-fluid.
Example IV The kettle was charged with 225 grams of hydrogenated castor oil, 200 grams of mineral oil whose characteristics are set forth in Example I, and 200 grams of water. The mixture was then heated with stirring to 210 F. 88.8 grams of a 45.9% sodium hydroxide solution were 1 then added over a period of one-half hour. At this point the saponiflcation mixture in the kettle was a white, soft dough. Stirring was continued for an additional hour at 186-192 F. and 75 grams of triple-pressed stearic acid added. After stirring for one and one-quarter hours the heat was turned on to dehydrate the soap base at 308 F. and a white, tough, fibrous base was formed. This base was held at 280-308 F. for one-half hour. The heat was then turned off and 142 grams of mineral oil added over a period of one-half hour. When the temperature reached 206 F. 7.8 grams of phenyl alpha naphthylamine and 3.1 grams of triple-pressed stearic acid were added. Thereafter, 877 grams of di-2- ethylhexyl sebacate were added slowly. After the addition of the sebacate ester control ASTM penetrations indicated an unworked penetration of 112 and a worked penetration of 102. 1050 grams of a blend of 71.7% sebacate ester, 27.8% mineral oil and 0.5% phenyl alpha naphthylamine were then added slowly, and at 194 F. a control worked penetration of 376 at 770 F. was obtained. The batch was then drawn and the product obtained was a smooth, buttery, glossy grease of alight color. The calculated composition of the resulting grease was as follows:
Percent Sodium soap 12.1 Glycerine 0.8 Mineral oil 24.2 Di-2-ethylhexyl sebacate 62.4 Phenyl alpha naphthylamine 0.5
Obviously many modifications and variations of the invention, as hereinbefore set forth, may be made without departing from the spirit and scope thereof, and, therefore only such limitations should be imposed as are indicated in the appended claims.
We claim:
l. A lubricating grease composition comprising as the essential and at least major portion of the lubricating base a high molecular weight high boiling liquid aliphatic dicarboxylic acid ester within the lubricating oil viscosity rangeand possessing lubricating properties. and suflicient metal soap of a soap-forming fatty material selected from the group consisting of hydroxy fatty acids and hydroxy fatty acid glycerides to thicken said lubricating base, said grease composition being texture-stable under high shearing stress.
2. A lubricating grease composition according to claim 1, wherein the said aliphatic dicar boxylic acid ester is a branched chain aliphatic diester.
, 8. A lubricating grease composition according to claim 2, wherein the said diester is a branched chain aliphatic sebacate.
4. A lubricating grea'se composition according to claim 3, wherein the said ester is di-2- ethylhexyl sebacate'.
5. A lubricating grease "composition according to claim 1. wherein the metal soap is a sodium soap.
6, A lubricating grease composition comprising essentially a lubricating base consisting of at least a major proportion of an oil-soluble high molecular weight high boiling liquid aliphatic dicarboxylic acid ester within the lubricating oil viscosity range and possessing lubricating properties and not more than a minor proportion of mineral lubricating oil, sufllcient metal soap of a soap-forming fatty material containing at least 50% by weight on the basis of the fatty material of hydrogenated castor oil to thicken said lubricating base, glycerine, and a small amount or an oxidation inhibitor.
7. A lubricating grease composition comprising essentially a lubricating base consisting of a major proportion of di-z-ethylhexyl sebacate and a minor proportion of mineral lubricating oil, suiiicient metal soap of hydrogenated castor oil to thicken said lubricating base, glycerine, and a small proportion of an oxidation inhibitor. 8. A lubricating grease composition according to claim 7, wherein said metal soap is a sodium soap, and said oxidation inhibitor is phenyl alpha naphthylamine.
HARRY V. ABHBURN. ROBERT S. BARN'E'I'I'. ONEY P. PURYEAR.
REFERENCES CITED he following references are of record in the file of this patent:
UNITED s'rA'ras PATENTS Number Name Date 2,283,602 Fiero May 19, 1942 2,308,599 Fraser Jan. 19, 1943 2,321,384 Hemker June 8, 1943 2,329,474 Lazar Sept. 14, 1943 2,351,384 Woods et a1. June 13, 1944 2,379,850 1 Morgan July 3, 1945 2,397,956 Fraser .Apr. 9, 1946 Certificate of Correction Patent No. 2,450,221. September 28,1948. HARRY V. ASHBURN ET AL.
It is hereby certified that error appears in the printed specification of the above numbered patent requiring correction as follows:
Column 7, line 40, Example IV, for 770 F. read 77 F1;
and that the said Letters Patent should be read with this correction'therein that the same may conform to the record of the case in the Patent Ofiice.
Signed and sealed this 4th day of January, A. D. 1949.
THOMAS F. MURPHY,
Assistant Uommz'esioner of Patents.
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Cited By (31)

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Publication number Priority date Publication date Assignee Title
US2508741A (en) * 1948-04-12 1950-05-23 Texas Co Lubricating grease composition
US2521438A (en) * 1947-12-06 1950-09-05 Standard Oil Dev Co Grease composition
US2524563A (en) * 1946-10-08 1950-10-03 Shell Dev Lubricant
US2576033A (en) * 1949-12-17 1951-11-20 Standard Oil Dev Co Preparing high-temperature lubricating greases
US2589973A (en) * 1949-11-01 1952-03-18 Standard Oil Dev Co Lubricating grease composition
US2610946A (en) * 1951-02-08 1952-09-16 Texas Co Lithium soap grease containing basic alkaline earth metal sulfonate
US2615763A (en) * 1948-12-27 1952-10-28 Taylor Instrument Co Leakless low friction bearing
US2639266A (en) * 1951-04-07 1953-05-19 Texas Co Lubricating grease comprising a complex ester base and sodium myristate
US2641577A (en) * 1951-06-22 1953-06-09 Standard Oil Dev Co Lithium-calcium lubricating grease composition
US2652364A (en) * 1951-12-29 1953-09-15 Shell Dev High-temperature grease compositions
US2653132A (en) * 1949-12-17 1953-09-22 Standard Oil Dev Co Oxo-bottoms base lubricating grease
US2662056A (en) * 1949-06-30 1953-12-08 Gulf Research Development Co Lubricating compositions
US2662058A (en) * 1949-06-30 1953-12-08 Gulf Research Development Co Petroleum lubricating jelly
US2662059A (en) * 1949-06-30 1953-12-08 Gulf Research Development Co Lubricating compositions
US2666033A (en) * 1951-04-11 1954-01-12 Texas Co Lithium soap grease containing methacrylate ester polymer for bearing noise suppression
US2681313A (en) * 1950-02-20 1954-06-15 California Research Corp Alkyl orthosilicate and alkoxysiloxane base grease compositions
US2684944A (en) * 1952-06-02 1954-07-27 Standard Oil Co Lithium polyorgano siloxane polymer grease compositions
US2702276A (en) * 1951-04-10 1955-02-15 Du Pont Water-dispersible emulsions of polysiloxanes
US2714092A (en) * 1953-03-04 1955-07-26 Texas Co Lithium base grease containing group ii divalent metal alkyl salicylate, such as zinc alkyl salicylate, as copper corrosion inhibitor
US2721844A (en) * 1951-12-07 1955-10-25 Texas Co Lithium soap-synthetic base instrument grease
US2756212A (en) * 1956-07-24 Siloxyglycol
US2812306A (en) * 1954-06-23 1957-11-05 Standard Oil Co Lithium soap grease containing rust and copper corrosion inhibitors
US2874192A (en) * 1953-05-29 1959-02-17 Exxon Research Engineering Co Mercaptals of long chain hydrocarbon aldehydes and long chain hydrocarbon mercaptans
US2898298A (en) * 1954-03-16 1959-08-04 Sinclair Refining Co Process for lithium base grease
US2993773A (en) * 1959-02-02 1961-07-25 Petrolite Corp Ester additives
US2993772A (en) * 1959-02-02 1961-07-25 Petrolite Corp Acid additives
US2993771A (en) * 1959-02-02 1961-07-25 Petrolite Corp Process of preventing deposits in internal combustion and jet engines employing additives
US3077438A (en) * 1960-12-02 1963-02-12 Warner Lambert Pharmaceutical Stabilization of orally administrable methenamine mandelate sesame oil suspensions containing 12-hydroxy stearic acid triglyceride
US3115422A (en) * 1960-06-06 1963-12-24 Gen Motors Corp Treatment of metals
US3117088A (en) * 1960-04-25 1964-01-07 Sinclair Research Inc Method of lubricating the clutch assembly of automobile starter motors
US3158574A (en) * 1960-07-26 1964-11-24 Exxon Research Engineering Co Lithium greases

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US2283602A (en) * 1940-01-09 1942-05-19 George W Fiero Grease and lubricant
US2308599A (en) * 1940-01-09 1943-01-19 Internat Lubricant Corp Production of lubricants containing lead soap of hydrogenated ricinoleic acid
US2321384A (en) * 1941-03-31 1943-06-08 Arthur L Parker Compound for sealing and lubricating relatively moving parts
US2329474A (en) * 1937-01-05 1943-09-14 Tide Water Associated Oil Comp Lubricant
US2351384A (en) * 1942-11-18 1944-06-13 Shell Dev Lithium soap grease
US2379850A (en) * 1942-06-03 1945-07-03 Cities Service Oil Co Lubricants
US2397956A (en) * 1943-01-15 1946-04-09 Internat Lubricant Corp Production of lubricants

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US2329474A (en) * 1937-01-05 1943-09-14 Tide Water Associated Oil Comp Lubricant
US2283602A (en) * 1940-01-09 1942-05-19 George W Fiero Grease and lubricant
US2308599A (en) * 1940-01-09 1943-01-19 Internat Lubricant Corp Production of lubricants containing lead soap of hydrogenated ricinoleic acid
US2321384A (en) * 1941-03-31 1943-06-08 Arthur L Parker Compound for sealing and lubricating relatively moving parts
US2379850A (en) * 1942-06-03 1945-07-03 Cities Service Oil Co Lubricants
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Cited By (31)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2756212A (en) * 1956-07-24 Siloxyglycol
US2524563A (en) * 1946-10-08 1950-10-03 Shell Dev Lubricant
US2521438A (en) * 1947-12-06 1950-09-05 Standard Oil Dev Co Grease composition
US2508741A (en) * 1948-04-12 1950-05-23 Texas Co Lubricating grease composition
US2615763A (en) * 1948-12-27 1952-10-28 Taylor Instrument Co Leakless low friction bearing
US2662056A (en) * 1949-06-30 1953-12-08 Gulf Research Development Co Lubricating compositions
US2662059A (en) * 1949-06-30 1953-12-08 Gulf Research Development Co Lubricating compositions
US2662058A (en) * 1949-06-30 1953-12-08 Gulf Research Development Co Petroleum lubricating jelly
US2589973A (en) * 1949-11-01 1952-03-18 Standard Oil Dev Co Lubricating grease composition
US2576033A (en) * 1949-12-17 1951-11-20 Standard Oil Dev Co Preparing high-temperature lubricating greases
US2653132A (en) * 1949-12-17 1953-09-22 Standard Oil Dev Co Oxo-bottoms base lubricating grease
US2681313A (en) * 1950-02-20 1954-06-15 California Research Corp Alkyl orthosilicate and alkoxysiloxane base grease compositions
US2610946A (en) * 1951-02-08 1952-09-16 Texas Co Lithium soap grease containing basic alkaline earth metal sulfonate
US2639266A (en) * 1951-04-07 1953-05-19 Texas Co Lubricating grease comprising a complex ester base and sodium myristate
US2702276A (en) * 1951-04-10 1955-02-15 Du Pont Water-dispersible emulsions of polysiloxanes
US2666033A (en) * 1951-04-11 1954-01-12 Texas Co Lithium soap grease containing methacrylate ester polymer for bearing noise suppression
US2641577A (en) * 1951-06-22 1953-06-09 Standard Oil Dev Co Lithium-calcium lubricating grease composition
US2721844A (en) * 1951-12-07 1955-10-25 Texas Co Lithium soap-synthetic base instrument grease
US2652364A (en) * 1951-12-29 1953-09-15 Shell Dev High-temperature grease compositions
US2684944A (en) * 1952-06-02 1954-07-27 Standard Oil Co Lithium polyorgano siloxane polymer grease compositions
US2714092A (en) * 1953-03-04 1955-07-26 Texas Co Lithium base grease containing group ii divalent metal alkyl salicylate, such as zinc alkyl salicylate, as copper corrosion inhibitor
US2874192A (en) * 1953-05-29 1959-02-17 Exxon Research Engineering Co Mercaptals of long chain hydrocarbon aldehydes and long chain hydrocarbon mercaptans
US2898298A (en) * 1954-03-16 1959-08-04 Sinclair Refining Co Process for lithium base grease
US2812306A (en) * 1954-06-23 1957-11-05 Standard Oil Co Lithium soap grease containing rust and copper corrosion inhibitors
US2993773A (en) * 1959-02-02 1961-07-25 Petrolite Corp Ester additives
US2993772A (en) * 1959-02-02 1961-07-25 Petrolite Corp Acid additives
US2993771A (en) * 1959-02-02 1961-07-25 Petrolite Corp Process of preventing deposits in internal combustion and jet engines employing additives
US3117088A (en) * 1960-04-25 1964-01-07 Sinclair Research Inc Method of lubricating the clutch assembly of automobile starter motors
US3115422A (en) * 1960-06-06 1963-12-24 Gen Motors Corp Treatment of metals
US3158574A (en) * 1960-07-26 1964-11-24 Exxon Research Engineering Co Lithium greases
US3077438A (en) * 1960-12-02 1963-02-12 Warner Lambert Pharmaceutical Stabilization of orally administrable methenamine mandelate sesame oil suspensions containing 12-hydroxy stearic acid triglyceride

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