US2450254A - Lithium base grease and method of preparing the same - Google Patents

Lithium base grease and method of preparing the same Download PDF

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US2450254A
US2450254A US548940A US54894044A US2450254A US 2450254 A US2450254 A US 2450254A US 548940 A US548940 A US 548940A US 54894044 A US54894044 A US 54894044A US 2450254 A US2450254 A US 2450254A
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grease
lithium
soap
lithium base
fatty acid
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Oney P Puryear
Harry V Ashburn
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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
    • C10M5/00Solid or semi-solid compositions containing as the essential lubricating ingredient mineral lubricating oils or fatty oils and their use
    • 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
    • C10M2205/00Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions
    • C10M2205/17Fisher Tropsch reaction products
    • C10M2205/173Fisher Tropsch reaction products used as base material
    • 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
    • C10M2207/04Ethers; Acetals; Ortho-esters; Ortho-carbonates
    • 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
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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
    • 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
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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
    • 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
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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
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/28Esters
    • C10M2207/284Esters of aromatic monocarboxylic 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
    • C10M2207/285Esters of aromatic polycarboxylic 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
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/40Fatty vegetable or animal oils
    • 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
    • C10M2207/40Fatty vegetable or animal oils
    • C10M2207/404Fatty vegetable or animal oils obtained from genetically modified species
    • 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
    • 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
    • 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
    • C10M2215/067Polyaryl amine alkanes
    • 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
    • C10N2050/00Form in which the lubricant is applied to the material being lubricated
    • C10N2050/10Semi-solids; greasy

Definitions

  • This invention relates to an improved lubricating grease composition and particularly to a texture-stable lithium base grease and methods of preparing the same.
  • lithium base greases prepared from saturated fats or fatty acids, possessa high melting point and are Water-resistant. These properties are particularly desirable in that. they permit lubrication ,over a wide temperature range and minimize the solubilizing or leaching effect of water and moisture condensation on the grease.
  • these greases there are certain diifficulties associated with the production of these greases,
  • a slurry of a lithium soap, such as the stearate, which is either preformed or prepared in situ, and a mineral oil are heated to temperatures of around 360-500 F. until a homogeneous solution is obtained.
  • This solution of lithium soap in oil is then drawn from the kettle and allowed to cool in open pans until a gel structure is set up. The cooled gel is. then subjected to a milling operation where it is homogenized to a homogeneous grease composition. It becomes quite apparent that the effi ciency and economies of such a method of manufacture are quite poor, due to the high tempera-.
  • lithiumbase grease composition of exceptional texture and oxidation stability which is capable of continued operation under conditions of high shearing stresses with negligible change in structure and very little change in consistency, together with an eflicient and economical method of preparation which requires a minimum of equipment, provides an accurate control of consistency and yield of product, and is operated at temperatures attainable in a steam-jacketed kettle.
  • the invention contemplates the use of a soap-forming hydroxy fatty acid glyceride as the acidic component in the preparation of a lithium base grease composition. It has been found that a lithium soap grease prepared from a hydroxy fatty acid glyceride possesses exceptional texture stability and maintains its structure with little change in penetration even after extensive working at either high or low temperatures. Furthermore, the hydroxy fatty acid glyceride permits the use of a simple low temperature method of preparation as distinguished from the high temperature complex methods required by the use of other well-known fats and fatty 'acids.
  • the preparation of the grease is carried out by saponifying a soap-forming hydroxy fatty acid glyceride with a basic lithium compound, dehydrating the reaction product, and adding mineral oil until the desired consistency is obtained.
  • The-total operation is easily conducted in a steam-jacketed open kettle andthe resulting finished lithiumbase grease requires no homogenization or further treatment prior to actual use.
  • the hydroxy fatty acid glyceride's used in accordance with the invention are the glycerides of hydroxy fatty acids containing 12 or more carbon atoms and one or'more hydroxyl radicals which are separated from the carboxyl group by at least one carbon atom. These glycerides may either be used as the sole acidic component of the lithium soap or in combination with other fats or fatty acids, in which case the hydroxy fatty acid glycerides are preferably present in a predominant amount. In" the latter case, the
  • the encased 3 tion or the preformed lithium soaps thereof may be blended in the desired proportions.
  • hydrogenated castor oil is used as the representative soap-forming hydroxy fatty acid glyceride.
  • hydrogenated castor oil possesses the advantage of availability and cost which renders it competitive to the more common fats and fatty acids.
  • the invention is not limited to hydrogenated castor oil and that other soapforming hydroxy fatty acid glycerides may be used in accordance with the invention. Examples of such glycerides are the glycerides of the hydroxy fatty acids produced by catalytic oxidation of hydrocarbon oils and waxes which have been extracted and fractionated to the de sired molecular range.
  • the oil component of the subject grease compositions may be either a mineral oil, a synthetic oil, or an organic oily medium, such as the benzoate or phthalate esters. with a wide range of viscosities, depending upon the type of lubrication required of the finished grease.
  • an oil component possessing a viscosity in the range of 40-70 S. U. S. at 100 F., a low pour point, and a viscosity index of 30 or more is preferred.
  • the soap content may also be varied in accordance with the grade or consistency desired. Normally, the soap content of the lithium base grease of the invention possessing an ASTM penetration in the range of 300450 varies between 10-20% soap.
  • an oxidation inhibitor must be used.
  • the aromatic amine type of inhibitor has been found particularly effective.
  • the polynuclear aromatic amines such as tetrarnethyl diamino diphenyl methane, diphenyl amine, and phenyl alpha naphthylamine are preferred.
  • a steam-jacketed open kettle is charged with a mixture of lithium hydroxide and water and heated with stirring to 160-180 F. until all the lithium hydroxide is dissolved.
  • the required amount of hydrogenated castor oil in equal weight of oil is then added and stirring is continued for three to five hours at 170-200 F., or until the hydrogenated castor oil is completely saponifled.
  • the kettle contents are then heated within the effect the dehydration of the saponified product at temperatln'es above 270 F. At temperatures of around 270 F. it is necessary to heat for several hours in order to cause the soap mass to become translucent and lose its cloudy-white appearance, whereas at temperatures of around 300 F. a shorter dehydration time may be used. At lower 4 temperatures the yields of the product fall 0! materially.
  • the grease prepared in the foregoing example was subjected to a so-called dynamic shear test. This test 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 maintained at a temperature of 225 F., and the piston then.
  • A may be seen from the comparative results soap of a soap-forming hydroxy fatty acid glyceride as the essential soap constituent thereof,
  • said method enabling the use of temperatures attainable in a steam-jacketed kettle without fire hazard, which comprises saponifying with a basic obtained, the lithium soap grease prepared from hydrogenated castor oil possesses a structure which does not break down under the severe conditions of the test and. if anything, formed a tighter grease structure which accounts for the harder consistency. This phenomenon is characteristic of the lithium soap greases prepared from hydroxy fatty acid giycerides.
  • the lithium stearate grease which is representative of the conventional fats and fatty acids, breaks down to a liquid or semi-liquid product.
  • a method of preparing a low temperature geltype lithium base grease containing a lithium lithium compound at a temperature within the range of about Nil-200 F. of a soap-forming hydroxy fatty acid glyceride in the presence of a small proportion of the oleaginous vehicle included in the grease then raising the temperature of the saponified product to about 270-330 F. to dehydrate the product and render the same translucent, thereafter reducing the temperature and adding the balance and large proportion of the oleaginous vehicle as the product cools and the desired consistency is attained, and finally drawing the resultant gel-type grease as a final product.
  • the hydroxy fatty acid glyceride is hydrogenated castor oil
  • the oleaginous vehicle comprises a mineral lubricating oil having a viscosity within the range of -70 S. U. S.,at F.

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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 se V 2a, .1948
BASE GREASE AND METHOD PREPARING THE SAME LITHIUM OneyP. Puryear, ,Fishkill, and Harry V. Ashburn, (llenham, N..-Y., assignors to The Texas Company, New York, N. Y
ware
., a corporation of Delav No Drawing. Application August 10, 1944, Serial No. 548,940
. 2 Claims. 1
This invention relates to an improved lubricating grease composition and particularly to a texture-stable lithium base grease and methods of preparing the same.
In general, lithium base greases, prepared from saturated fats or fatty acids, possessa high melting point and are Water-resistant. These properties are particularly desirable in that. they permit lubrication ,over a wide temperature range and minimize the solubilizing or leaching effect of water and moisture condensation on the grease. However, there are certain diifficulties associated with the production of these greases,
together with certain undesirable performance.
characteristics, which prevent any large scale acceptance thereof as a commercial lubricating grease.
In the preparation of the conventional lithium base grease, a slurry of a lithium soap, such as the stearate, which is either preformed or prepared in situ, and a mineral oil, are heated to temperatures of around 360-500 F. until a homogeneous solution is obtained. This solution of lithium soap in oil is then drawn from the kettle and allowed to cool in open pans until a gel structure is set up. The cooled gel is. then subjected to a milling operation where it is homogenized to a homogeneous grease composition. It becomes quite apparent that the effi ciency and economies of such a method of manufacture are quite poor, due to the high tempera-.
tures of operation, special equipment required,
and the lack of control over the consistency and yield of the final product.
One of the most important drawbacks of the conventional lithium base greases is, however, the inability of these greases to maintain their structure and lubricating qualities under conditions of operation where shearing stresses are involved and particularly at temperatures above atmospheric. In such installations the greases gradually lose their consistency until they become liquid and cause bearing failures. Attempts have been made to correct this deficiency by the incorporation of various stabilizing and thickening agents, such as other metallic soaps and high molecular weight esters.
In accordance with the discovery of the present invention, it has been found possible to provide a lithiumbase grease composition of exceptional texture and oxidation stability which is capable of continued operation under conditions of high shearing stresses with negligible change in structure and very little change in consistency, together with an eflicient and economical method of preparation which requires a minimum of equipment, provides an accurate control of consistency and yield of product, and is operated at temperatures attainable in a steam-jacketed kettle.
In its broadest aspect, the invention contemplates the use of a soap-forming hydroxy fatty acid glyceride as the acidic component in the preparation of a lithium base grease composition. It has been found that a lithium soap grease prepared from a hydroxy fatty acid glyceride possesses exceptional texture stability and maintains its structure with little change in penetration even after extensive working at either high or low temperatures. Furthermore, the hydroxy fatty acid glyceride permits the use of a simple low temperature method of preparation as distinguished from the high temperature complex methods required by the use of other well-known fats and fatty 'acids. The preparation of the grease is carried out by saponifying a soap-forming hydroxy fatty acid glyceride with a basic lithium compound, dehydrating the reaction product, and adding mineral oil until the desired consistency is obtained. The-total operation is easily conducted in a steam-jacketed open kettle andthe resulting finished lithiumbase grease requires no homogenization or further treatment prior to actual use.
The hydroxy fatty acid glyceride's used in accordance with the invention are the glycerides of hydroxy fatty acids containing 12 or more carbon atoms and one or'more hydroxyl radicals which are separated from the carboxyl group by at least one carbon atom. These glycerides may either be used as the sole acidic component of the lithium soap or in combination with other fats or fatty acids, in which case the hydroxy fatty acid glycerides are preferably present in a predominant amount. In" the latter case, the
encased 3 tion or the preformed lithium soaps thereof may be blended in the desired proportions.
In the following description of the preferred form of the invention hydrogenated castor oil is used as the representative soap-forming hydroxy fatty acid glyceride. For practical application at the present time, hydrogenated castor oil possesses the advantage of availability and cost which renders it competitive to the more common fats and fatty acids. However, it is to be understood that the invention is not limited to hydrogenated castor oil and that other soapforming hydroxy fatty acid glycerides may be used in accordance with the invention. Examples of such glycerides are the glycerides of the hydroxy fatty acids produced by catalytic oxidation of hydrocarbon oils and waxes which have been extracted and fractionated to the de sired molecular range.
The oil component of the subject grease compositions may be either a mineral oil, a synthetic oil, or an organic oily medium, such as the benzoate or phthalate esters. with a wide range of viscosities, depending upon the type of lubrication required of the finished grease. For example, in the preparation of a low temperature lithium base grease employed in the lubrication of bearings and the like at temperatures below 60 R, an oil component possessing a viscosity in the range of 40-70 S. U. S. at 100 F., a low pour point, and a viscosity index of 30 or more is preferred. The soap content may also be varied in accordance with the grade or consistency desired. Normally, the soap content of the lithium base grease of the invention possessing an ASTM penetration in the range of 300450 varies between 10-20% soap.
Where a high degree of oxidation stability'is required an oxidation inhibitor must be used. For these lithium base greases the aromatic amine type of inhibitor has been found particularly effective. Of this class ofinhibitors the polynuclear aromatic amines, such as tetrarnethyl diamino diphenyl methane, diphenyl amine, and phenyl alpha naphthylamine are preferred.
The procedure involved in the preparation of these lithium base greases may be outlined as follows:
A steam-jacketed open kettle is charged with a mixture of lithium hydroxide and water and heated with stirring to 160-180 F. until all the lithium hydroxide is dissolved. The required amount of hydrogenated castor oil in equal weight of oil is then added and stirring is continued for three to five hours at 170-200 F., or until the hydrogenated castor oil is completely saponifled.
The kettle contents are then heated within the effect the dehydration of the saponified product at temperatln'es above 270 F. At temperatures of around 270 F. it is necessary to heat for several hours in order to cause the soap mass to become translucent and lose its cloudy-white appearance, whereas at temperatures of around 300 F. a shorter dehydration time may be used. At lower 4 temperatures the yields of the product fall 0! materially.
Example Gravity, API 26.9 Flash, F 310 Fire,- F 340 Vic. at 100 F. S. U 60.2 Pour F 55 Color AS'I'M 3 ,4
This mixture was then heated with stirring, for
six hours, at 182-192 F. and shut dowh over night. The temperature was then brought up to dehydration temperature and the contents of the kettle heated with stirring for five hours at 277-285 F. The steam heat was then cut down to 75 pounds pressure and the temperature gradually reduced, with simultaneous addition of the mineral oil. When the temperature of the kettle reached approximately 200 F., 189.5 grams of phenyl alpha naphthylamine, dissolved in oil, were added. Oil addition was then continued until 67 pounds of oil had been added and the worked penetration at 78 F. was 325, The grease thus obtained was a smooth, buttery, semitransparent, very light brown grease. The tests obtained thereon are as follows:
Lithium soap ..Q. per cent" 16.1
Free alkali (LiOH) do-- 0.09 Free fatty acid (as oleic) do- 0.03 Free neutral fat -..do 0.67 Phenyl alpha naphthylamine (calc.) do 0.5
Penetration at 77 F. worked 838 Dropping point F. (ASTM) 356 Navy water absorptionper cent 10 Norma-Hoffman oxidation (100 hrs. at
210 F.), pounds pressure drop max 5 The Institute Spokesman. National Lubricating Grease Institute, January, 1944. Test methods for determining free acid and free alkali in greases."
In order to determine the texture-stabilizing properties and the resistance to shear at high temperatures, the grease prepared in the foregoing example was subiected to a so-called dynamic shear test. This test 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 maintained at a temperature of 225 F., and the piston then.
reciprocated at 49 strokes per minute for. a period of 8 hours; At the conclusion of the test the grease was removed and miniature penetrations taken. This miniature penetration was then compared with the miniature penetration of the grease taken before the test to determine the effect of the shearing action upon the grease structure. .The results obtained" on the subject grease, designated as "Grease No. I," as compared to the lithium stearate grease prepared by the conventionalv high temperature manufacture, designated as Grease No. II," are as follows:
Miniature Penetrometer ior Determining the Consistency of Lubricating Greases." Ind. Eng. Chem, analytical edition, vol. 11, page 108, February 15, 1939,
A may be seen from the comparative results soap of a soap-forming hydroxy fatty acid glyceride as the essential soap constituent thereof,
said method enabling the use of temperatures attainable in a steam-jacketed kettle without fire hazard, which comprises saponifying with a basic obtained, the lithium soap grease prepared from hydrogenated castor oil possesses a structure which does not break down under the severe conditions of the test and. if anything, formed a tighter grease structure which accounts for the harder consistency. This phenomenon is characteristic of the lithium soap greases prepared from hydroxy fatty acid giycerides. On the other hand, the lithium stearate grease which is representative of the conventional fats and fatty acids, breaks down to a liquid or semi-liquid product.
The low temperature method of manufacturing a lithium base grease from a hydroxy fatty acid, such-as 12-hydroxystearic acid, is disclosed and claimed in our co-pending application, Serial No. 588,890, filed Aprii 17, 1945.
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:
1. A method of preparing a low temperature geltype lithium base grease containing a lithium lithium compound at a temperature within the range of about Nil-200 F. of a soap-forming hydroxy fatty acid glyceride in the presence of a small proportion of the oleaginous vehicle included in the grease, then raising the temperature of the saponified product to about 270-330 F. to dehydrate the product and render the same translucent, thereafter reducing the temperature and adding the balance and large proportion of the oleaginous vehicle as the product cools and the desired consistency is attained, and finally drawing the resultant gel-type grease as a final product.
2. The method according to claim 1, wherein the hydroxy fatty acid glyceride is hydrogenated castor oil, and the oleaginous vehicle comprises a mineral lubricating oil having a viscosity within the range of -70 S. U. S.,at F.
' 'ONEY P. PURYEAR.
HARRY V. ASHBURN.
REFERENCES crrEn' The following references are of record in the. file of this patent:
UNITED STATES PATENTS Fraser Apr. 9, 1946
US548940A 1944-08-10 1944-08-10 Lithium base grease and method of preparing the same Expired - Lifetime US2450254A (en)

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US548940A US2450254A (en) 1944-08-10 1944-08-10 Lithium base grease and method of preparing the same
GB25803/45A GB601346A (en) 1944-08-10 1945-10-04 Improvements in or relating to lithium base lubricating grease compositions and method of preparing the same
FR917111D FR917111A (en) 1944-08-10 1945-11-08 Lithium-based lubricating greases and process for their production

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Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2600058A (en) * 1949-03-09 1952-06-10 Texas Co Lubricant containing soap of phosphated hydroxy fatty acid or glyceride
US2614076A (en) * 1949-09-16 1952-10-14 Shell Dev Grease compositions
US2629695A (en) * 1948-01-13 1953-02-24 Shell Dev Manufacture of lithium lubricating greases
US2697693A (en) * 1951-11-05 1954-12-21 Standard Oil Co Manufacture of lithium hydroxy carboxylic acid soap greases
US2760936A (en) * 1952-05-20 1956-08-28 Nat Cylinder Gas Co Manufacture of lithium grease
US2846394A (en) * 1954-11-30 1958-08-05 Standard Oil Co Rheopectic grease composition
US2898298A (en) * 1954-03-16 1959-08-04 Sinclair Refining Co Process for lithium base grease
US2959543A (en) * 1958-04-14 1960-11-08 Pure Oil Co Extreme pressure lithium greases
US3020233A (en) * 1959-04-29 1962-02-06 Richfield Oil Corp Grease composition
US3171812A (en) * 1960-07-25 1965-03-02 Exxon Research Engineering Co Antiplugging agents for hydroxy stearate greases
US3388065A (en) * 1965-08-05 1968-06-11 Sinclair Research Inc Process for lithium soap greases
EP1327621A1 (en) * 2002-01-12 2003-07-16 Lithchem International Dry powder lithium carboxylates

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3998745A (en) * 1975-02-12 1976-12-21 Texaco Inc. Method for manufacturing traction motor gear lubricant

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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
US2351384A (en) * 1942-11-18 1944-06-13 Shell Dev Lithium soap grease
US2397956A (en) * 1943-01-15 1946-04-09 Internat Lubricant Corp Production of lubricants

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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
US2351384A (en) * 1942-11-18 1944-06-13 Shell Dev Lithium soap grease
US2397956A (en) * 1943-01-15 1946-04-09 Internat Lubricant Corp Production of lubricants

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2629695A (en) * 1948-01-13 1953-02-24 Shell Dev Manufacture of lithium lubricating greases
US2600058A (en) * 1949-03-09 1952-06-10 Texas Co Lubricant containing soap of phosphated hydroxy fatty acid or glyceride
US2614076A (en) * 1949-09-16 1952-10-14 Shell Dev Grease compositions
US2614077A (en) * 1949-12-28 1952-10-14 Shell Dev Grease composition
US2697693A (en) * 1951-11-05 1954-12-21 Standard Oil Co Manufacture of lithium hydroxy carboxylic acid soap greases
US2760936A (en) * 1952-05-20 1956-08-28 Nat Cylinder Gas Co Manufacture of lithium grease
US2898298A (en) * 1954-03-16 1959-08-04 Sinclair Refining Co Process for lithium base grease
US2846394A (en) * 1954-11-30 1958-08-05 Standard Oil Co Rheopectic grease composition
US2959543A (en) * 1958-04-14 1960-11-08 Pure Oil Co Extreme pressure lithium greases
US3020233A (en) * 1959-04-29 1962-02-06 Richfield Oil Corp Grease composition
US3171812A (en) * 1960-07-25 1965-03-02 Exxon Research Engineering Co Antiplugging agents for hydroxy stearate greases
US3388065A (en) * 1965-08-05 1968-06-11 Sinclair Research Inc Process for lithium soap greases
EP1327621A1 (en) * 2002-01-12 2003-07-16 Lithchem International Dry powder lithium carboxylates

Also Published As

Publication number Publication date
FR917111A (en) 1946-12-26
GB601346A (en) 1948-05-04

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