US2908645A - Blended lithium calcium base grease - Google Patents

Blended lithium calcium base grease Download PDF

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Publication number
US2908645A
US2908645A US504659A US50465955A US2908645A US 2908645 A US2908645 A US 2908645A US 504659 A US504659 A US 504659A US 50465955 A US50465955 A US 50465955A US 2908645 A US2908645 A US 2908645A
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Prior art keywords
grease
acids
lithium
molecular weight
component
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US504659A
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English (en)
Inventor
Arnold J Morway
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ExxonMobil Technology and Engineering Co
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Exxon Research and Engineering Co
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Priority to NL104990D priority Critical patent/NL104990C/xx
Priority to BE546805D priority patent/BE546805A/xx
Application filed by Exxon Research and Engineering Co filed Critical Exxon Research and Engineering Co
Priority to US504659A priority patent/US2908645A/en
Priority to GB9885/56A priority patent/GB793484A/en
Priority to FR1152678D priority patent/FR1152678A/fr
Priority to DEE12287A priority patent/DE1064667B/de
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Publication of US2908645A publication Critical patent/US2908645A/en
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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
    • C10M2219/00—Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions
    • C10M2219/10—Heterocyclic compounds containing sulfur, selenium or tellurium compounds in the ring
    • C10M2219/104—Heterocyclic compounds containing sulfur, selenium or tellurium compounds in the ring containing sulfur and carbon with nitrogen or oxygen in the ring
    • 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
    • C10M2219/10—Heterocyclic compounds containing sulfur, selenium or tellurium compounds in the ring
    • C10M2219/104—Heterocyclic compounds containing sulfur, selenium or tellurium compounds in the ring containing sulfur and carbon with nitrogen or oxygen in the ring
    • C10M2219/106—Thiadiazoles
    • 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
    • C10M2229/00—Organic 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
    • C10M2229/02—Unspecified siloxanes; Silicones
    • 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
    • C10M2229/00—Organic 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
    • C10M2229/04—Siloxanes with specific structure
    • C10M2229/05—Siloxanes with specific structure containing atoms other than silicon, hydrogen, oxygen or carbon
    • 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
    • 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
    • C10N2050/00—Form in which the lubricant is applied to the material being lubricated
    • C10N2050/10—Form in which the lubricant is applied to the material being lubricated semi-solid; greasy

Definitions

  • This invention relates to improved lubricating grease compositions having outstanding lubricating life and water resistance characteristics. More particularly, the invention "pertains to blends of separate grease components to form' greases having excellent water emulsion stability and long lubrication service.
  • the invention in brief compass, relates to lubricating grease compositions comprising a blend of two component greases, one component being a lubricating oil thickened to grease consistency with an organo-metallic soap-salt or mixed salt complex, having a high combined but active metal content, and the other component being a lithium soap thickened grease.
  • These two-component greases areimade separately and then blended togetherby thorough mixing or by the use of a suitable homogenizer or grease mill.
  • organo-metallic complexes having high metal content as grease thickeners has recently been suggested.
  • these complex thickeners have been prepared from the metal salts of low molecular weight carboxylic acids in combination with metal soaps ofhigh molecular weight carboxylic acids, metal salts of intermediate molecular weight carboxylic acids, or metal salts of medium molecular weight carboxylioacids 'and metal soaps of high molecular weight ca'rboxylicacids.
  • the metal constituents of the complex thickeners have usually been selected from the 'divalent metals, especially the alkaline earth metals. Calcium is particularly preferred.
  • Greases containing these complex thickeners have been found to have outstanding extreme pressure properties and long lubricating lives, but they tend to form fluid emulsions when water is churned into them. f
  • lithium soaps in grease-making is well known in theart.
  • Such lithium soap type thickeners have been prepared from the conventional soap-forming high molecular weight carboxylic acids, including their hydroxy derivatives and esters thereof.
  • Lithium-containing grease thickeners have also been prepared from mixtures of lithium and calcium soaps of high; molecular Weight fatty acids. Greases thickened with these lithiumcontaining soaps, such asthe lithium soap of hydroxy stearic acid, haveexcellent water resistance but notably poor lubricating lives.
  • carbon atoms per molecule between the high and medium molecular weight carboxylic acid is at least 7, preferably about 7 to 15.
  • the high molecular Weight carboxylic acids useful for preparing the complex thickeners described above are those saturated and unsaturated, grease-making fatty acids thatare commonly known to the art. In general, these fatty acids have from about 12 to 30 carbon atoms, preferably about 16 to 22 carbon atoms per molecule, and
  • fatty acids include such fatty acids as myristic acid, palmitic acid,
  • stearic acid the various hydroxy s'tearic acids, oleic acid, arachidic acid, behenic acid and the like.
  • -Mixtures in any proportions of these high molecular weight fatty acids are also operable.
  • Naturally occurring high molecular weight acids such as fish oil acids, tallow acids, castor oil acids, coconut oil acids may also be utilized either in their natural state or after partial or complete saturation by hydrogenation.
  • Preferred acids are mixtures derived from natural sources such as hydrogenated fish oil acids,
  • the intermediate molecular Weightacids are those aliphatic monocarboxylic acids containing from about7 to 10 carbon atoms, preferably about 8 to 9 carbon atoms, per molecule. Either saturated or unsaturated fatty acids may be utilized, though the saturated fatty acids are preferred.
  • branched chain acids are useful in the prepara- .tion ofsofter greases, Single or mixed intermediate weight acids having an average saponification valueof 3 from about 310 to 44 0, especially about 320 to 420', are preferred.
  • Suitable acids include:
  • OX0 acids are those formed by the well known Oxo process of synthesis with carbon monoxide, hydrogen and olefins, the latter being 0; and C polymers of propylene with or without some butylene, for making C and C Oxo acids.
  • the medium molecular weight carboxylic acids include straight and branched chain saturated aliphatic carboxylic acids, hydroxy aliphatic monoand poly-carboxylic acids, aromatic monoand poly-carboxylic acids and anhydrides thereof, and heterocyclic acids containing from about 3 to 10, preferably 6 to 9, carbon atoms per molecule.
  • Suitable carboxylic acids are as follows:
  • Pentanoic valeric Glyceric Hexanoic (caproic) Lactic Heptanoic (enanthic) Citric Octanoic (caprylic) Benzoic Nonanoic (pelargonic) Hydroxy benzoic Decanoic (capric) Toluic Isobutyric o-Phthalic C OX0 acids Phthalic anhydride C Oxo acids Terephthalic C Oxo acids Furoic C Oxo acids Thiophene carboxylic Mixed as well as single medium molecular Weight carboxylic acids may be employed in the preparation of these complex thickeners.
  • the low molecular weight carboxylic acids contemplated in this invention include saturated and unsaturated carboxylic acids having from about 1 to 3 carbon atoms, such as formic, acetic, propionic, acyclic and similar acids including their hydroxy derivatives, e.g. lactic acid. Monocarboxylic acids are particularly useful, and acetic acid is especially preferred.
  • the low molecular weight carboxylic acid employed should have a saponification value of above about 600, preferably about 750 to 1300.
  • Mixed low molecular weight carboxylic acids, wherein the acids contain from about 1 to 3 carbon atoms, having saponification values above about 600 may also be employed.
  • the acetic acid can be either glacial acetic acid or an aqueous solution of acetic acid. When the latter is employed, the concentration of acid in solution may vary from about 60 to 99.9 wt. percent, and is preferably about 80 wt. percent.
  • the metal component of the complexes described above is used in a form which can combine chemically with carboxylic acids to form salts or soaps. Ordinarily the metal hydroxide is used.
  • the alkaline earth metal hydroxides or carbonates such as those of calcium, barium and strontium are particularly useful for the purposes of this invention. Calcium hydroxide is especially preferred.
  • the alkaline earth metals differ in this respect from the alkali metals, i.e. sodium, potassium and lithium.
  • Complexes having a high alkali metal content and which consist of the combinations of acids, mol ratios, etc. of the alkaline earth metal complexes of this invention yield greases with poor structural stability. 7 It is preferred, therefore, to use metals having a valency of two. Metals such as magnesium and zinc are also useful for the purposes of this invention.
  • the soap-salt complex thickening agents may be utilized in combination with a Wide variety of mineral as well as synthetic lubricating oils.
  • Mineral base lubricating oils ranging in viscosity from about 30 to 1000 SUS at 100 F. are preferably employed as the liquid phase of the grease composition within the range of about 50 to wt. percent based on the total weight of the final grease composition.
  • These naturally occurring mineral lubricating oils may be derived from any petroleum crude source, whether paraffinic or naphthenic in type, and may be refined by any of the well known refining techniques of the petroleum industry.
  • Suitable synthetic lubricating oils include the hydrocarbon, hydrocarbon polymer, ester, complex ester, formal, mercaptal, polyalkylene oxide, silicone and similar types. Synthetic oils such as di-Z-ethylhexyl sebacate, di-C Oxo azelate and other branched chain simple esters of dicarboxylic acids can be used, as well as complex esters prepared from glycols, dicarboxylic acids, and alcohols or monocarboxylic acids.
  • the high metal content soap-salt complex or salt complexes may be prepared by coneutralization of a mixture of the acids employed with suitable bases, particularly the hydroxides and/or carbonates of the metals desired.
  • This coneutralization step may be carried out in situ in the liquid menstruum to which the complex is to be applied in actual use.
  • the mixed acids may be coneutralized in a portion or all of the lubricating oil forming the dispersant of a grease to be thickened by the soap-salt or salt complexes.
  • the coneutralized material is heated to high temperatures of about 400 to 550 F. or higher prior to use in order to dehydrate the product and to promote the formation of the complex.
  • this heating step is carried out in a liquid dispersant, the latter should have a boiling point above the heating temperature or the heating should be carried out under pressure.
  • the high meta'l soap-salt or salt complexes may also be prepared by separately preforming at least a portion of the high molecular weight carboxylic acid soap, when employed, and/or the low and intermediate molecular weight carboxylic acid salts. This method is particularly useful when different metals are employed as bases.
  • Soap-salt or salt complex proportions of about 530- wt. percent, preferably about 10-20 wt. percent, based on the total grease composition may be employed in preparing the greases constituting component 1 of this invention.
  • Component 2 is a lithium base grease, i.e. a lubricating oil thickened to grease consistency with lithium soaps of high molecular weight carboxylic acids. Mixtures of lithium and strontium or lithium and calcium soaps may also be employed to prepare these greases.
  • the grease-forming fats or high molecular weight fatty acids listed above are also suitable for preparing the component 2 grease.
  • the grease can be made ximm J genesis
  • the conventional methods of grease manufacture such as cooking in a fire heated kettle followed by drawing into thin pans or deep. cakes for cooling may be em ployed in preparing the lithium soap thickened greases. They may also be prepared in steam heated kettles followed by cooling with stirring while running cold water through the kettle jacket or by a continuous method of manufacture.
  • US. Patent 2,397,956 discloses the preparation of greases containing a lithium soap of 12-hydroxy stearic or the lithium soap of hydrogenated castor oil as a thickener.
  • the lithium soaps are present in amounts up to 50%, preferably 8 to 40%, of the total weight of the grease.
  • these greases are preferably prepared at temperatures of between about 400 to 425 F.
  • any suitable lithium compound may be used such as lithium hydroxide, lithium carbonate, lithium oxide and the like.
  • the lithium compound used is lithium monohydrate which contains from 53 to 55% .of lithium hydroxide.
  • operable proportions include from about 20 to 80% of component 1 and from about 20 to 80% of component 2.
  • Preferred proportions are from about 40 to 80% of component 1 and from about 20 to 60% of component 2.
  • the temperatures of blending are within the range of about 100 to 300 F., preferably about 180 to 225 F.
  • the maximum temperature range may be just below the phase change in the lithium grease, i.e. when the grease changes in structure from a rubbery fibrous product to a smooth homogeneous product.
  • the two grease components are blended together by thorough mixing or by being passed through a Gaulin homogenizer or Morehouse mill at a temperature suflicient to give an outlet temperature below the phase change of the lithium soap thickened grease component.
  • Grease B I A grease was prepared from the following ingredients:
  • the fatty acid and about one half of the mineral oil were added to steam kettle, and the calcium hydroxide was stirred in at a temperature of about 155 F. Heating and stirring were continued, and the lithium hydroxide added as a 10% aqueous solution at a temperature of 198 F.
  • the grease batch was then heated to a temperature of about 290 F. to eifect dehydration. During this period the viscosity of the mass was cut down by the addition of small amounts of oil. Thereafter the heat was shut oif, and the balance of the mineral oil added while stirring over a period of about 1 to 2 hours.
  • the grease was finished by being passed through a Morehouse rnillat an inlet temperature of about 90 F. and an outlet temperature of about 118 F.
  • Greases C, D, E and F These greases were prepared by blending Greases A and B, separately prepared as described above, in accordance with formulations listed in the table below at a temperature of 125 F.
  • Grease G A grease was prepared from the following ingredients:
  • the mixture 'of acetic acid and caprylic acid was charged to the kettle, and the temperature raised with stirring to about 480 F. At this temperature, heating was discontinued and the mixture cooled to about 250 F. with stirring. Phenyl alpha naphthylamine was. then added, and cooling continued to a temperature of about 200 F. The resulting grease composition was milled through a Gaulin homogenizer and filtered.
  • Grease H A grease was prepared from the following ingredients:
  • the methyl 12-hydroxy stearate and the mineral oil were charged to a fire heated kettle and warmed while mixing to F.
  • a 20% aqueous boiling water solution of the lithium monohydrate was then added and the grease heated to 400 F.
  • the fluid grease was cooled while stirring to 350 F. where the grease was just starting to solidify.
  • the phenyl alpha naphthylamine was then added, and the grease drawn into pans for cooling.
  • Greases I, J, K, L and M These greases were prepared by blending Greases G and H, separately prepared as described above, in accordance with the formulations listed in the table below at a temperature of 180 F.
  • this invention relates to new and improved lubricating grease compositions comprising blends of l) soap-salt complex or mixed salt complex thickened greases having a high combined metal content and (2) lithium soap thickened greases.
  • the blended grease compositions prepared in accordance with the invention have lubricating lives superior to the individual lithium soap thickened greases and a water resistance superior to the individual complex thickened greases.
  • Blends containing from about 20' The invention is not necessarily limited to the specific conditions and materials of the foregoing example. These conditions and materials may be varied within the limits indicated in the general portions of the specification. Moreover, the conventional grease additives such as oxidation inhibitors, pour point depressors, corrosion inhibitors and the like can be effectively incorporated in the grease blends of this invention.
  • a blended grease composition comprising a blend of two component greases, one component being a grease thickened with a calcium mixed salt complex of lowand intermediate molecular weight mono-carboxylic acids, wherein the mol ratio of low to intermediate weight acid is about 2:1 to 40:1, the other component being a lithium base grease thickened with the lithium soap of a highmolecular weight fatty acid, said blend consisting essentially of from 40 to 80% by Weight of the first component and 20 to by weight of the second component.
  • blended grease composition of claim 1 wherein said blend consists essentially of from about 40 to 60% by weight of the first component and from about 40 to 60% by weight of'the second component.
  • the blended grease composition of claim 1, wherein said calcium mixed salt complex is a mixed salt complex of a low molecular weight carboxylicacid having from 1 to 3 carbon atoms per molecule and an intermediate molecular weight carboxylic acid having from 7 to 10 carbon atoms per molecule.
  • the blended grease composition of claim 1 wherein the first component is a grease thickened with the mixed salt complex of calcium acetate and calcium caprylate, and the second component is a lithium base grease thickened with lithium 12-hydroxystearate said blend consisting essentially of from about 40 to 60% by weight of the first component and 40 to 60% by weight of the second component.

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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)
US504659A 1955-04-28 1955-04-28 Blended lithium calcium base grease Expired - Lifetime US2908645A (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
NL104990D NL104990C (cs) 1955-04-28
BE546805D BE546805A (cs) 1955-04-28
US504659A US2908645A (en) 1955-04-28 1955-04-28 Blended lithium calcium base grease
GB9885/56A GB793484A (en) 1955-04-28 1956-03-29 Improved grease compositions
FR1152678D FR1152678A (fr) 1955-04-28 1956-04-18 Graisses composées lubrifiantes
DEE12287A DE1064667B (de) 1955-04-28 1956-04-24 Schmierfett und Verfahren zu seiner Herstellung

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Application Number Priority Date Filing Date Title
US504659A US2908645A (en) 1955-04-28 1955-04-28 Blended lithium calcium base grease

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US2908645A true US2908645A (en) 1959-10-13

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BE (1) BE546805A (cs)
DE (1) DE1064667B (cs)
FR (1) FR1152678A (cs)
GB (1) GB793484A (cs)
NL (1) NL104990C (cs)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3223633A (en) * 1963-07-01 1965-12-14 Exxon Research Engineering Co Lubricant
US3298953A (en) * 1964-04-01 1967-01-17 Exxon Research Engineering Co Lubricants containing mixed metal salts of fatty acid and aromatic polybasic acid
US3389085A (en) * 1964-03-31 1968-06-18 Exxon Research Engineering Co Lubricants containing mixed metal salts of mono- and polybasic acids
US5015403A (en) * 1990-03-23 1991-05-14 Shell Oil Company Preparation of lithium-calcium grease compositions
WO2015021052A1 (en) * 2013-08-05 2015-02-12 Sr Lubricant Solutions, Llc Lubricant with spherical copper and bismuth powders

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL258842A (cs) * 1959-12-11
DE2027403C2 (de) * 1970-06-04 1983-12-15 Exxon Research and Engineering Co., 07036 Linden, N.J. Dauerschmierfett

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2397956A (en) * 1943-01-15 1946-04-09 Internat Lubricant Corp Production of lubricants
US2417428A (en) * 1946-09-19 1947-03-18 Union Oil Co Lubricating composition
US2641577A (en) * 1951-06-22 1953-06-09 Standard Oil Dev Co Lithium-calcium lubricating grease composition
US2844536A (en) * 1954-04-30 1958-07-22 Exxon Research Engineering Co High temperature complex grease manufacturing processes

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2712527A (en) * 1952-08-26 1955-07-05 Exxon Research Engineering Co Improved lubricating greases containing dihydroxy stearic acid soap

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2397956A (en) * 1943-01-15 1946-04-09 Internat Lubricant Corp Production of lubricants
US2417428A (en) * 1946-09-19 1947-03-18 Union Oil Co Lubricating composition
US2641577A (en) * 1951-06-22 1953-06-09 Standard Oil Dev Co Lithium-calcium lubricating grease composition
US2844536A (en) * 1954-04-30 1958-07-22 Exxon Research Engineering Co High temperature complex grease manufacturing processes

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3223633A (en) * 1963-07-01 1965-12-14 Exxon Research Engineering Co Lubricant
US3389085A (en) * 1964-03-31 1968-06-18 Exxon Research Engineering Co Lubricants containing mixed metal salts of mono- and polybasic acids
US3298953A (en) * 1964-04-01 1967-01-17 Exxon Research Engineering Co Lubricants containing mixed metal salts of fatty acid and aromatic polybasic acid
US5015403A (en) * 1990-03-23 1991-05-14 Shell Oil Company Preparation of lithium-calcium grease compositions
WO2015021052A1 (en) * 2013-08-05 2015-02-12 Sr Lubricant Solutions, Llc Lubricant with spherical copper and bismuth powders

Also Published As

Publication number Publication date
GB793484A (en) 1958-04-16
FR1152678A (fr) 1958-02-21
BE546805A (cs)
NL104990C (cs)
DE1064667B (de) 1959-09-03

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