CA1288410C - Grease composition - Google Patents
Grease compositionInfo
- Publication number
- CA1288410C CA1288410C CA000541569A CA541569A CA1288410C CA 1288410 C CA1288410 C CA 1288410C CA 000541569 A CA000541569 A CA 000541569A CA 541569 A CA541569 A CA 541569A CA 1288410 C CA1288410 C CA 1288410C
- Authority
- CA
- Canada
- Prior art keywords
- grease composition
- oil
- thickener
- grease
- viscosity
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Classifications
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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
- C10M169/00—Lubricating compositions characterised by containing as components a mixture of at least two types of ingredient selected from base-materials, thickeners or additives, covered by the preceding groups, each of these compounds being essential
- C10M169/02—Mixtures of base-materials and thickeners
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- C10M101/00—Lubricating compositions characterised by the base-material being a mineral or fatty oil
- C10M101/02—Petroleum fractions
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- C10M105/00—Lubricating compositions characterised by the base-material being a non-macromolecular organic compound
- C10M105/02—Well-defined hydrocarbons
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- C10M105/00—Lubricating compositions characterised by the base-material being a non-macromolecular organic compound
- C10M105/08—Lubricating compositions characterised by the base-material being a non-macromolecular organic compound containing oxygen
- C10M105/32—Esters
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- C10M107/00—Lubricating compositions characterised by the base-material being a macromolecular compound
- C10M107/02—Hydrocarbon polymers; Hydrocarbon polymers modified by oxidation
- C10M107/10—Hydrocarbon polymers; Hydrocarbon polymers modified by oxidation containing aliphatic monomer having more than 4 carbon atoms
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- C10M117/00—Lubricating compositions characterised by the thickener being a non-macromolecular carboxylic acid or salt thereof
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- C10M2201/14—Inorganic compounds or elements as ingredients in lubricant compositions inorganic compounds surface treated with organic compounds
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- C10M2203/0206—Well-defined aliphatic compounds used as base material
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- 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
- C10M2215/00—Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant compositions
- C10M2215/02—Amines, e.g. polyalkylene polyamines; Quaternary amines
- C10M2215/06—Amines, e.g. polyalkylene polyamines; Quaternary amines having amino groups bound to carbon atoms of six-membered aromatic rings
- C10M2215/064—Di- and triaryl amines
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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
- C10M2219/04—Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions containing sulfur-to-oxygen bonds, i.e. sulfones, sulfoxides
- C10M2219/044—Sulfonic acids, Derivatives thereof, e.g. neutral salts
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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
- C10M2219/06—Thio-acids; Thiocyanates; Derivatives thereof
- C10M2219/062—Thio-acids; Thiocyanates; Derivatives thereof having carbon-to-sulfur double bonds
- C10M2219/066—Thiocarbamic type compounds
- C10M2219/068—Thiocarbamate metal salts
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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
- C10M2223/00—Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions
- C10M2223/02—Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions having no phosphorus-to-carbon bonds
- C10M2223/04—Phosphate esters
- C10M2223/045—Metal containing thio derivatives
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- 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
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2010/00—Metal present as such or in compounds
- C10N2010/06—Groups 3 or 13
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- 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
- C10N2010/08—Groups 4 or 14
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- 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
- C10N2010/10—Groups 5 or 15
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- 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
- C10N2010/12—Groups 6 or 16
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- 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
- C10N2020/00—Specified physical or chemical properties or characteristics, i.e. function, of component of lubricating compositions
- C10N2020/01—Physico-chemical properties
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Abstract
ABSTRACT OF THE DISCLOSURE
The present invention is directed at a grease composition comprising:
A. an oil component having between about 30 and 90 wt.% of a synthetic fluid having a viscosity of at least 50 cSt at 40°C and from about 70 to about 10 wt.% of a mineral oil having a pour point below -20°C; and B. a thickener.
The oil component of the grease composition more preferably comprises between about 40 and about 80 wt.%
synthetic oil and preferably from 60 to 20 wt.% mineral oil.
The viscosity of the synthetic oil preferably is at least 50 cSt, more preferably at least 100 cSt at 40°C. The synthetic oil preferably is selected from polyolefins, esters, polyesters, high VI isoparaffins, and mixtures thereof, with polyalphaolefins being particularly preferred. The polyalphaolefins preferably comprise C8 to C12 monoalphaolefin building blocks.
The present invention is directed at a grease composition comprising:
A. an oil component having between about 30 and 90 wt.% of a synthetic fluid having a viscosity of at least 50 cSt at 40°C and from about 70 to about 10 wt.% of a mineral oil having a pour point below -20°C; and B. a thickener.
The oil component of the grease composition more preferably comprises between about 40 and about 80 wt.%
synthetic oil and preferably from 60 to 20 wt.% mineral oil.
The viscosity of the synthetic oil preferably is at least 50 cSt, more preferably at least 100 cSt at 40°C. The synthetic oil preferably is selected from polyolefins, esters, polyesters, high VI isoparaffins, and mixtures thereof, with polyalphaolefins being particularly preferred. The polyalphaolefins preferably comprise C8 to C12 monoalphaolefin building blocks.
Description
BACKGROUND OF THE INVENTION
The present invention is directed at a grease having desirable properties over wide tempera-ture ranges.
Adequate lubrication of outdoor equipment, such as heavy production, construction, or mining equipmen~, may be hampered for a variety of reasons.
The bearings and gears of such equipmsnt frequently must operate under high, or shock, load conditions, at slow speeds, and in the presence of sand or other abrasive materials. Greases used under such conditions must contain oils of relatively high viscosity at normal operating temperatures to prevent damage to the moving parts because the thickness of the protective lubricant film increases as oil viscosity and sliding speed increase, and decreases directionally with applied load. Clearly, the lubricating film thickness needs to be greater than the diameter of abrasive particles if adequate protection to bearing and gear surfaces is to be provided1 Furthermore, greases used in such dusty environments need to r~sist slumping at high ambien~ summer temperatures in order to maintain adequate sealing capabilities around the shafts-of bearings and gears in order to prevent the ingress of dirt and abrasive materials. Thus, good performance greases for these applications need to have a moderately firm consistency, as well as a relatively high oil viscosity for summer operating conditions.
Automatic lubricating systems used in such heavy equipment frequently involve the use of long, relatively small diameter tubes to deliver the grease ~k 4~ 3 from a cen~ral supply location to the bearing or gear to be lubricated. While this normally presents no problem at ambient summer temperatures, ability to deliver the grease through these lines to the lubrica~ed parts at winter ambient temperatures is often the limiting factor in grease selection. The National Lubricating Grease Institute has developed a series of nomographs by which dispensibility can ba calculated from a number of factors which include tube length, tube diameter, pumping pressure, and grease apparent viscosity. It is well known in the art that grease apparent viscosity is a function primarily-of base oil viscosity and grease consistency, at the dis-pensing temperature. Hence, in sub-arctic regions where ambient temperatures may vary from as low as -40C in winter to as high as 35C in summer, con-flicting demands are placed on grease properties. In winter a low base oil viscosity and soft consistency is preferred for good dispensibility, while, in summer, relatively high viscosity and firm consistency is preferred to provide adequate lubrication and sealing against the ingress of dirt and abrasive materials.
U.S. Patent No. 3,813,338 discloses a lubricant for use in textile machines comprising a naphthenic base oil, 0.3-6 wt.~ polyolefin as a tackiness agent and 0.1-1.5 wt.% lithium soap.
U.S. Patent No. 4,075,112 and U.S. Patent No. 4,075,113 disclose graase compositions comprising 2-15 wt.% aluminum soap, 25 to 97% of a hydrogenated or non-hydrogenated polymer of a monoolefinic hydrocarbon having 4 carbon atoms and a mean molecular weight of between 300 and 2500, and 0-60 wt.% of a lubricating oil, which preferably is a mineral oil~
The present invention is directed at a grease having desirable properties over wide tempera-ture ranges.
Adequate lubrication of outdoor equipment, such as heavy production, construction, or mining equipmen~, may be hampered for a variety of reasons.
The bearings and gears of such equipmsnt frequently must operate under high, or shock, load conditions, at slow speeds, and in the presence of sand or other abrasive materials. Greases used under such conditions must contain oils of relatively high viscosity at normal operating temperatures to prevent damage to the moving parts because the thickness of the protective lubricant film increases as oil viscosity and sliding speed increase, and decreases directionally with applied load. Clearly, the lubricating film thickness needs to be greater than the diameter of abrasive particles if adequate protection to bearing and gear surfaces is to be provided1 Furthermore, greases used in such dusty environments need to r~sist slumping at high ambien~ summer temperatures in order to maintain adequate sealing capabilities around the shafts-of bearings and gears in order to prevent the ingress of dirt and abrasive materials. Thus, good performance greases for these applications need to have a moderately firm consistency, as well as a relatively high oil viscosity for summer operating conditions.
Automatic lubricating systems used in such heavy equipment frequently involve the use of long, relatively small diameter tubes to deliver the grease ~k 4~ 3 from a cen~ral supply location to the bearing or gear to be lubricated. While this normally presents no problem at ambient summer temperatures, ability to deliver the grease through these lines to the lubrica~ed parts at winter ambient temperatures is often the limiting factor in grease selection. The National Lubricating Grease Institute has developed a series of nomographs by which dispensibility can ba calculated from a number of factors which include tube length, tube diameter, pumping pressure, and grease apparent viscosity. It is well known in the art that grease apparent viscosity is a function primarily-of base oil viscosity and grease consistency, at the dis-pensing temperature. Hence, in sub-arctic regions where ambient temperatures may vary from as low as -40C in winter to as high as 35C in summer, con-flicting demands are placed on grease properties. In winter a low base oil viscosity and soft consistency is preferred for good dispensibility, while, in summer, relatively high viscosity and firm consistency is preferred to provide adequate lubrication and sealing against the ingress of dirt and abrasive materials.
U.S. Patent No. 3,813,338 discloses a lubricant for use in textile machines comprising a naphthenic base oil, 0.3-6 wt.~ polyolefin as a tackiness agent and 0.1-1.5 wt.% lithium soap.
U.S. Patent No. 4,075,112 and U.S. Patent No. 4,075,113 disclose graase compositions comprising 2-15 wt.% aluminum soap, 25 to 97% of a hydrogenated or non-hydrogenated polymer of a monoolefinic hydrocarbon having 4 carbon atoms and a mean molecular weight of between 300 and 2500, and 0-60 wt.% of a lubricating oil, which preferably is a mineral oil~
3.~
Japanese Patent Fublication No. J5-9,109,595 discloses a lithiurn soap which may include a refined base stock derived from naphthenic, paraffinic and mixed base crudes. Synthetic lubricating oils also are disclosed as being useful. These synthetic oils in-clude polymers and copolymers of alpha olefins.
Japanese Patent Publications J5-9,142,291-3 disclose lithium containing lubricants comprising an aliphatic hydrocarbon oil.
Japanese Patent Publication No. J5-8,122,996 discloses a grease composition having lithium ~hickener and a base oil comprising substantially a Clg-C30 naphthenic hydrocarbon.
U.S. Patent No. 3,112,270 discloses a grease comprising a mineral oil, ethylene polymer and a 50ap thickener.
U.S. Patent No. 3,114,708 discloses the manufacture of a dry grease blend comprising 20 to 75 weight percent polyolefin.
U.S~ Patent No. 3,813,338 discloses a high retention thickened oil lubricant for textile machinery comprising a naphthenic base oil, a polyolefin and a lithium thickener.
U.S. Patent No. 3,539~512 discloses the combination of a base oil and a polyolefin thickener to produce a grease having a low tendency to bleed.
U.S. Patent No. 3~541,011 discloses a gel lubricant comprising a mineral oil and polyethylene thickener.
Japanese Patent Fublication No. J5-9,109,595 discloses a lithiurn soap which may include a refined base stock derived from naphthenic, paraffinic and mixed base crudes. Synthetic lubricating oils also are disclosed as being useful. These synthetic oils in-clude polymers and copolymers of alpha olefins.
Japanese Patent Publications J5-9,142,291-3 disclose lithium containing lubricants comprising an aliphatic hydrocarbon oil.
Japanese Patent Publication No. J5-8,122,996 discloses a grease composition having lithium ~hickener and a base oil comprising substantially a Clg-C30 naphthenic hydrocarbon.
U.S. Patent No. 3,112,270 discloses a grease comprising a mineral oil, ethylene polymer and a 50ap thickener.
U.S. Patent No. 3,114,708 discloses the manufacture of a dry grease blend comprising 20 to 75 weight percent polyolefin.
U.S~ Patent No. 3,813,338 discloses a high retention thickened oil lubricant for textile machinery comprising a naphthenic base oil, a polyolefin and a lithium thickener.
U.S. Patent No. 3,539~512 discloses the combination of a base oil and a polyolefin thickener to produce a grease having a low tendency to bleed.
U.S. Patent No. 3~541,011 discloses a gel lubricant comprising a mineral oil and polyethylene thickener.
U.S. Patent No. 4,406,800 discloses a grease useful over ~ wide temperature range comprising a polyalphaolefin base fluid and a thickener.
It would be advantageous to provide a grease having acceptable dispensing and lubricating properties over a wide te~perature range.
It also would be desirable to provide a gre~se having a hlgh oil viscosity and relatively firm consistency in warm weather and a relatively soft consistency and relatively low apparent viscosity for pumping in cold weather.
It ~lsô would be desirable to provide a gr~ase which ;s relatively inexpensive to manufacture, is shear stable, resists slumping, and has good extreme pressure and anti-wear properties.
SUMMARY OF THE INVENTION
The present invention is directed at a grease composition comprising:
A. an oil component having between about 30 and 90 wt.% of a synthetic fluid having a viscosity of at least 50 cSt at 40C and from about 70 to about 10 wt.% of a mineral oil having a pour point below -20C; and B. a thickener.
The oil component of the grease composition more preferably comprises between-about 40 and about 80 wt.%
synthetic oil and preferably from 60 to 20 wt % mineral oil The viscosity of the synthetic oil preferably is at least 50 3 ~34~
cSt, more preferably at least 100 cSt at 40C The synthetic oil preferably is selected from polyolefins, esters, polyesters, high VI isoparaffins, and mixtures thereof, with polyalphaolefins being particularly preferred. The polyalphaolefins preferably comprise C~ to C12 monoalphaolefin building blocks~
The thickener preferably comprises about S
to about 30 wt.~ of a lithium, calcium, aluminum and/or barium soap of a fatty acid, such as stearic acid or 12-hydroxystearic acid or the complex calcium, lithium, barium and/or aluminum soaps/salts of the fatty acids with lower molecular weight mono or dibasic acids, such as azelaic or benzoic acid, or a modified clay thickener. Particularly preferred are lithium, barium, calcium, or aluminum simple or complex soaps and mixtureS thereof, with lithium soaps being particularly preferred. The lithium-containing thickener preferably comprises a complex lithium soap/salt. Particularly preferred are lithium soaps/salts formed by the in-situ saponification reaction of 12-hydroxystearic acid and/or azelaic acid.
The grease of the present invention is of particular utility where the ambient temperature ranges over at least 50C.
DETAILED DESCRIPTION OF THE INVENTION
The present invention is directed at a grease composition having particular utility where the ambient temperature varies over a relatively wide range. The grease composition comprises:
, I ,, 3 ~34~) A. an oil component having between about 30 and go wt.% of a synthetic fluid having a viscosity of at least 50 cSt at 40C and from about 70 to about 10 wt.~ of a mineral oil having a pour point below about -20C; and, B. a thickener.
The viscosity of the ~ineral oil preferably is less than the viscosity of the synthetic fluid over the temperature range for which the use is contemplated.
In order to combine the highest possible oil viscosity at ambient summer temperatures for satis-factory lubrication with the lowest possible oil viscosity at ambient winter temperatures to ensure satisfactory dispensing, the base oil or combination of base oils used in the grease should have a relatively high viscosity index and a relatively low pour point.
As shown by the data in Table 1 and Table 2, the best combinations of high VI and low pour point are obtained from blends of low viscosity, low pour point oils (naphthenic or synthetic) with relatively high vis-cosity, high VI synthetic fluids.
A suitable grease should have an oil component VI above about 100 and preferably above about 125. Similarly, the oil pour point should be below about -20C, preferably below about -30C and more preferably below about -40C.
The composition of each of the grease components is set forth in detail below:
!, ' ~, 34~
A. Synthetic Fluid The viscosity index of the synthetic fluid should be relatively high. The synthetic fluid may comprise polyalphaolefins, diesters, polyolesters, complex esters, the high VI isoparaffins produced by hydrocracking or hydroisomerization of waxes, and mix-tures thereof. Of these, the polyalphaolefins are particularly preferred, since many are commercially available. The preferred hydrogenated polyalphaolefins have viscosities in the range of 8-150 cSt at 100C, VI's of a~ least 125, and pour points below about -20C, preferably below about ~30C and more preferably below about -40C. Suh polyalphaolefins may be produced from linear alpha olefins containing about 8-12 carbon atoms by an oligomerization process which produces dimers, trimers, tetramers, pentamers, etc. of these olefins. In general, the viscosity of the poly-alphaolefins increases with the molecular weight of the oligomer, while the mono olefin carbon number, linearity, and position of unsaturation, determine the VI and pour point of the polyalphaolefin oligomer.
Generally, the higher the carbon number o~ the mono olefin, the higher the VI and the higher the pour point of the oligomer. Nonlinear mono olefins are not pre-ferred, since they tend to produce lower VI oligomers~
Internal olefin monomers also produce more branched polyolefin structures which exhibit lower VI's and generally lower pour points. A satisfactory combina-tion of pour point and VI has been obtained by polymerizing Clo linear alpha olefins monomers and hydrogenating the resulting polymer.
B. Mineral_Oil The mineral oil of the present invention is derived from crude and preferably has a pour point below -20C, more preferably below -30C and most preferably b~low -40C. The mineral oil may comprise any hydrocarbon stream having the desired pour point.
Naphthenic oils, such as transformer oil and/or spindle oil and mixtures thereof, are particularly preferred.
When oils are utilized having pour points above -20C, it has been found ~hat the grease does not have the requisite low temperature dispensibility proper~ies.-C. Thickener The thickener of the present inventionpreferably comprises between about S and about 30 wt.%
of the grease, preferably between about 5 and about 20 wt.~ of the grease composition. The thickener preferably comprises a simple calcium, lithium, aluminum and/or barium soap of a fatty acid, such as stearic acid or 12-hydroxystearic acid or the complex calcium, lithium, barium and/or aluminum soaps/salts of the fatty acids with lower molecular weight mono or aielaic or benzoic acid, or a modified clay thickener.
Particularly preferred are lithium, barium, calcium, or aluminum simple or complex soaps and mixtures thereof, with lithium soaps being particularly preferred~ The lithium containing ~hickener preferably comprises a complex li~hium soap/salt. Particularly preferred are lithium soaps/salts formed by the in-situ saponifica-tion reaction of 12-hydroxystearic acid and/or azelaic acid.
~
A series of tests were conducted to demonstrate th~ utility of the present invention in producing a grease having the desired viscosities and pour point pzopertlesO The greases indicated below had a thickener system co~prising approximately:
8.5 wt.% 12-hydroxystearic acid 3~0 wt~ azelaic acid; and 2~5 wt.% lithium hydroxide monohydrate.
The greases also had an additive package ~omprising an extreme pressure additive, an anti-wear additive, an anti-rust additive and an antioxidant~
The individual additives comprising the additive package may be conventional. Among the preferred extreme pressure additives are lead naphthenate, lead dialkyldithiocarbamate, antimony dialkyldithiocarba-mate, etc.
Among the preferred anti-wear additives are zinc dialkyldithiophosphates, zinc dialkyldithiocarbamates, etc.
Among the preferred anti-oxidant additives are PANA, alkyl-substituted aromatic amines, etc.
.
Among th-e preferred anti-rust additives are various sulphonates based on sodium, barium, etc.
To this additive package may be added other additives required for the specific end use~ such as seal swell agents, tackiness additives, dyes, etc.
34~
In the comparative examples and examples below, an effort was made to maintain the thickener content within the range of about 12-14 wt.%. There were minor variations in the thickener content because different oils were used. Higher thickener content would increase the grease cos~ considerably and could adversely affect pu~pability.
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w ~ ~ ~ ~ s 1:~ ~ ~ t~- Z 2 lil 1~
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~: E E
It would be advantageous to provide a grease having acceptable dispensing and lubricating properties over a wide te~perature range.
It also would be desirable to provide a gre~se having a hlgh oil viscosity and relatively firm consistency in warm weather and a relatively soft consistency and relatively low apparent viscosity for pumping in cold weather.
It ~lsô would be desirable to provide a gr~ase which ;s relatively inexpensive to manufacture, is shear stable, resists slumping, and has good extreme pressure and anti-wear properties.
SUMMARY OF THE INVENTION
The present invention is directed at a grease composition comprising:
A. an oil component having between about 30 and 90 wt.% of a synthetic fluid having a viscosity of at least 50 cSt at 40C and from about 70 to about 10 wt.% of a mineral oil having a pour point below -20C; and B. a thickener.
The oil component of the grease composition more preferably comprises between-about 40 and about 80 wt.%
synthetic oil and preferably from 60 to 20 wt % mineral oil The viscosity of the synthetic oil preferably is at least 50 3 ~34~
cSt, more preferably at least 100 cSt at 40C The synthetic oil preferably is selected from polyolefins, esters, polyesters, high VI isoparaffins, and mixtures thereof, with polyalphaolefins being particularly preferred. The polyalphaolefins preferably comprise C~ to C12 monoalphaolefin building blocks~
The thickener preferably comprises about S
to about 30 wt.~ of a lithium, calcium, aluminum and/or barium soap of a fatty acid, such as stearic acid or 12-hydroxystearic acid or the complex calcium, lithium, barium and/or aluminum soaps/salts of the fatty acids with lower molecular weight mono or dibasic acids, such as azelaic or benzoic acid, or a modified clay thickener. Particularly preferred are lithium, barium, calcium, or aluminum simple or complex soaps and mixtureS thereof, with lithium soaps being particularly preferred. The lithium-containing thickener preferably comprises a complex lithium soap/salt. Particularly preferred are lithium soaps/salts formed by the in-situ saponification reaction of 12-hydroxystearic acid and/or azelaic acid.
The grease of the present invention is of particular utility where the ambient temperature ranges over at least 50C.
DETAILED DESCRIPTION OF THE INVENTION
The present invention is directed at a grease composition having particular utility where the ambient temperature varies over a relatively wide range. The grease composition comprises:
, I ,, 3 ~34~) A. an oil component having between about 30 and go wt.% of a synthetic fluid having a viscosity of at least 50 cSt at 40C and from about 70 to about 10 wt.~ of a mineral oil having a pour point below about -20C; and, B. a thickener.
The viscosity of the ~ineral oil preferably is less than the viscosity of the synthetic fluid over the temperature range for which the use is contemplated.
In order to combine the highest possible oil viscosity at ambient summer temperatures for satis-factory lubrication with the lowest possible oil viscosity at ambient winter temperatures to ensure satisfactory dispensing, the base oil or combination of base oils used in the grease should have a relatively high viscosity index and a relatively low pour point.
As shown by the data in Table 1 and Table 2, the best combinations of high VI and low pour point are obtained from blends of low viscosity, low pour point oils (naphthenic or synthetic) with relatively high vis-cosity, high VI synthetic fluids.
A suitable grease should have an oil component VI above about 100 and preferably above about 125. Similarly, the oil pour point should be below about -20C, preferably below about -30C and more preferably below about -40C.
The composition of each of the grease components is set forth in detail below:
!, ' ~, 34~
A. Synthetic Fluid The viscosity index of the synthetic fluid should be relatively high. The synthetic fluid may comprise polyalphaolefins, diesters, polyolesters, complex esters, the high VI isoparaffins produced by hydrocracking or hydroisomerization of waxes, and mix-tures thereof. Of these, the polyalphaolefins are particularly preferred, since many are commercially available. The preferred hydrogenated polyalphaolefins have viscosities in the range of 8-150 cSt at 100C, VI's of a~ least 125, and pour points below about -20C, preferably below about ~30C and more preferably below about -40C. Suh polyalphaolefins may be produced from linear alpha olefins containing about 8-12 carbon atoms by an oligomerization process which produces dimers, trimers, tetramers, pentamers, etc. of these olefins. In general, the viscosity of the poly-alphaolefins increases with the molecular weight of the oligomer, while the mono olefin carbon number, linearity, and position of unsaturation, determine the VI and pour point of the polyalphaolefin oligomer.
Generally, the higher the carbon number o~ the mono olefin, the higher the VI and the higher the pour point of the oligomer. Nonlinear mono olefins are not pre-ferred, since they tend to produce lower VI oligomers~
Internal olefin monomers also produce more branched polyolefin structures which exhibit lower VI's and generally lower pour points. A satisfactory combina-tion of pour point and VI has been obtained by polymerizing Clo linear alpha olefins monomers and hydrogenating the resulting polymer.
B. Mineral_Oil The mineral oil of the present invention is derived from crude and preferably has a pour point below -20C, more preferably below -30C and most preferably b~low -40C. The mineral oil may comprise any hydrocarbon stream having the desired pour point.
Naphthenic oils, such as transformer oil and/or spindle oil and mixtures thereof, are particularly preferred.
When oils are utilized having pour points above -20C, it has been found ~hat the grease does not have the requisite low temperature dispensibility proper~ies.-C. Thickener The thickener of the present inventionpreferably comprises between about S and about 30 wt.%
of the grease, preferably between about 5 and about 20 wt.~ of the grease composition. The thickener preferably comprises a simple calcium, lithium, aluminum and/or barium soap of a fatty acid, such as stearic acid or 12-hydroxystearic acid or the complex calcium, lithium, barium and/or aluminum soaps/salts of the fatty acids with lower molecular weight mono or aielaic or benzoic acid, or a modified clay thickener.
Particularly preferred are lithium, barium, calcium, or aluminum simple or complex soaps and mixtures thereof, with lithium soaps being particularly preferred~ The lithium containing ~hickener preferably comprises a complex li~hium soap/salt. Particularly preferred are lithium soaps/salts formed by the in-situ saponifica-tion reaction of 12-hydroxystearic acid and/or azelaic acid.
~
A series of tests were conducted to demonstrate th~ utility of the present invention in producing a grease having the desired viscosities and pour point pzopertlesO The greases indicated below had a thickener system co~prising approximately:
8.5 wt.% 12-hydroxystearic acid 3~0 wt~ azelaic acid; and 2~5 wt.% lithium hydroxide monohydrate.
The greases also had an additive package ~omprising an extreme pressure additive, an anti-wear additive, an anti-rust additive and an antioxidant~
The individual additives comprising the additive package may be conventional. Among the preferred extreme pressure additives are lead naphthenate, lead dialkyldithiocarbamate, antimony dialkyldithiocarba-mate, etc.
Among the preferred anti-wear additives are zinc dialkyldithiophosphates, zinc dialkyldithiocarbamates, etc.
Among the preferred anti-oxidant additives are PANA, alkyl-substituted aromatic amines, etc.
.
Among th-e preferred anti-rust additives are various sulphonates based on sodium, barium, etc.
To this additive package may be added other additives required for the specific end use~ such as seal swell agents, tackiness additives, dyes, etc.
34~
In the comparative examples and examples below, an effort was made to maintain the thickener content within the range of about 12-14 wt.%. There were minor variations in the thickener content because different oils were used. Higher thickener content would increase the grease cos~ considerably and could adversely affect pu~pability.
~ C~ a~ o Z ~ O _I ~ ~C7 o ol l l l l l l l ~ ~ v u~
o :~: I r ~ ou~ a~ O ~ a~
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u~
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~ O
a: u~ o ~ r c~o a _~r~ u~
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:~ o ~ t o ~ 0 ~r a u~ c c z .,~
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u~ 3~ o o ~1 ~ a c~ ~ 3 3 3 ~ ~ ~ o o a ~ a ~ ~ ~, ~Ll E~ U U
o ~ u u X X X X X ~ ~ U
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~ c c c ~ s~ ~ ~ ~s U~ ~ ~ L C C ~ IJ
w ~ ~ ~ ~ s 1:~ ~ ~ t~- Z 2 lil 1~
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~: E E
5: O o ~ ~ ~ ~ X
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, .
34~
.
o o - CO
I I I ~ I I ~ O ~O
~ ~D O ~ ~ I
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, _ ,, U~
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t . U~
t O E I o o ~ al v~ ~ o a o I I I I I I o ~r ~r o co ~ V ~ U ~ o o ~ U~
~: ~ o o U 1`
~ ~ U I I ~ o ~ Ct~ In C~ o o O U~ ~, t ~ I I ~ ~ I I I I O ~,, C~ U, o ~ o I o I I I I I I o ~ a~
U~
. ...
O S ~D
~ ~ o 3 ~ o ~ ~ ~ ol 3L~r~
~o u~ l o~ o o o ~ o ~
~ ~ o o o o o u~ l oLrl o ~ o l o u~ ~ ~
:~ ~ r~
~ o ~ ~ - ~ ~
~ ~ o E~ ~ ~
h ~ ~ ~V
O ~
E~ ~ u~
~ O
oe o ô o ~ _ ~ _~I~ o~~ ~ In ~ ~ za ~ ' ~ I
h~ C:
~ U~ ; , ~: .~ ~ o ~
J- I ~ ~p ~ er ~7 1 ~ I
~: .,. I . . . . . I . I
C~ ~
~ dP ~
C ~
u~ 3 C) ~
~ c tn o _, ~ ~ o D
~ .~ o I ~ o ~n I ' I
E~ . ~ t~
C~ O
~: Q~
R:C E
~: U a C
~ t .~
~J
" ~ a ~ ~C a~ o ~ ~ ~ ~ ~ ~
4~~
~ s shown in Table III, the Grease EE and Grease FF exhibited good low temperature dispensibil-ity, as evidenced by the low apparent viscosity at -40C. As indicated in Table II, these greases a lso contained a high VI oil blend with a high viscosity at the upper operating temperature of 35 to 45C. Grease EE would be preferred because of its significantly lower cost and lower thickener content~
While the grease of the present invention set forth in Tables I and II was formulated to meet NLGI ~l l/2 grade specifications~ the grease also could be formulated to mee~ other NLGI penetration ranyes by adjusting the thickener content, and the relative amounts o mineral oil and synthetic oil.
3: U w ~ ~
C~ O _l ~ C
u~ , ~ ~ c s a~ ~ X
. ~ :~ a3 Q. X N 0 5-1 . .~ ~ 0 ~ ~ L-~-1 .S: U~ O ~ 3 .~ ~ ~o ~ ~ ~ o o ~
O _~ r` o u~ ~ ; s O tll Z * O I I I I I I I 1 O ~ ~ ~r ~- O ~~: ' . S E~
E~ o ~c~: O
3 ~O ~ ~r ~I ra X ~a 3 ~
s ~ C,) 1~ ~ ;~ Q Cl T
, .
34~
.
o o - CO
I I I ~ I I ~ O ~O
~ ~D O ~ ~ I
o o U~ ~, 5: I ~ I ~ t ~ ~ o er Ln ~ , o _ o ~
, _ ,, U~
I ~.1 1u~ ~ I O a3_, o~ I o o ~ o o ~-- o c:~ u ~ I I I I I I c~
C~ ~ ~9 o Z
U~ 3 I o o~
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t . U~
t O E I o o ~ al v~ ~ o a o I I I I I I o ~r ~r o co ~ V ~ U ~ o o ~ U~
~: ~ o o U 1`
~ ~ U I I ~ o ~ Ct~ In C~ o o O U~ ~, t ~ I I ~ ~ I I I I O ~,, C~ U, o ~ o I o I I I I I I o ~ a~
U~
. ...
O S ~D
~ ~ o 3 ~ o ~ ~ ~ ol 3L~r~
~o u~ l o~ o o o ~ o ~
~ ~ o o o o o u~ l oLrl o ~ o l o u~ ~ ~
:~ ~ r~
~ o ~ ~ - ~ ~
~ ~ o E~ ~ ~
h ~ ~ ~V
O ~
E~ ~ u~
~ O
oe o ô o ~ _ ~ _~I~ o~~ ~ In ~ ~ za ~ ' ~ I
h~ C:
~ U~ ; , ~: .~ ~ o ~
J- I ~ ~p ~ er ~7 1 ~ I
~: .,. I . . . . . I . I
C~ ~
~ dP ~
C ~
u~ 3 C) ~
~ c tn o _, ~ ~ o D
~ .~ o I ~ o ~n I ' I
E~ . ~ t~
C~ O
~: Q~
R:C E
~: U a C
~ t .~
~J
" ~ a ~ ~C a~ o ~ ~ ~ ~ ~ ~
4~~
~ s shown in Table III, the Grease EE and Grease FF exhibited good low temperature dispensibil-ity, as evidenced by the low apparent viscosity at -40C. As indicated in Table II, these greases a lso contained a high VI oil blend with a high viscosity at the upper operating temperature of 35 to 45C. Grease EE would be preferred because of its significantly lower cost and lower thickener content~
While the grease of the present invention set forth in Tables I and II was formulated to meet NLGI ~l l/2 grade specifications~ the grease also could be formulated to mee~ other NLGI penetration ranyes by adjusting the thickener content, and the relative amounts o mineral oil and synthetic oil.
Claims (11)
1. A grease composition comprising:
A. an oil component having between about 30 and 90 wt.% of a synthetic fluid having a viscosity of at least 50 cSt at 40°C. and from about 70 to about 10 wt.% of a mineral oil having a pour point below -20°C; and B. a thickener.
A. an oil component having between about 30 and 90 wt.% of a synthetic fluid having a viscosity of at least 50 cSt at 40°C. and from about 70 to about 10 wt.% of a mineral oil having a pour point below -20°C; and B. a thickener.
2. The grease composition of claim 1 wherein the synthetic fluid is selected from the group consisting of polyolefins, esters, polyesters, high VI
isoparaffins and mixtures thereof.
isoparaffins and mixtures thereof.
3. The grease composition of claim 2 wherein the synthetic fluid comprises a polyalphaolefin.
4. The grease composition of claim 3 wherein the polyalphaolefin comprises oligomers of C8-C12 linear alphaolefins.
5. The grease composition of claim 1 wherein the mineral oil has a pour point below -30°C.
6. The grease composition of claim wherein the thickener contains a metal selected from the group consisting of lithium, calcium, barium, aluminum and mixtures thereof.
7. The grease composition of claim 6 wherein the thickener comprises a lithium complex soap.
8. The grease composition of claim 1 wherein the synthetic oil content ranges between about 40 and 80 wt.% of the oil component.
9. The grease composition of claim 1 wherein the mineral oil content ranges from 60 to 20 wt.% of the oil component.
10. The grease composition of claim 1 wherein the thickener content ranges between about 5 and about 30 wt.% of the grease composition.
11. A grease composition comprising:
A. an oil component having from about 30 to about 90 wt.% of a C8-C12 polyalphaolefin and from about 70 to about 10 wt.% of a mineral oil having a pour point below about -20°C; and B. about 5 to about 30 wt.% of a lithium-containing thickener.
A. an oil component having from about 30 to about 90 wt.% of a C8-C12 polyalphaolefin and from about 70 to about 10 wt.% of a mineral oil having a pour point below about -20°C; and B. about 5 to about 30 wt.% of a lithium-containing thickener.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US06/885,140 US4749502A (en) | 1986-07-14 | 1986-07-14 | Grease composition |
US885,140 | 1986-07-14 |
Publications (1)
Publication Number | Publication Date |
---|---|
CA1288410C true CA1288410C (en) | 1991-09-03 |
Family
ID=25386231
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA000541569A Expired - Lifetime CA1288410C (en) | 1986-07-14 | 1987-07-08 | Grease composition |
Country Status (6)
Country | Link |
---|---|
US (1) | US4749502A (en) |
CA (1) | CA1288410C (en) |
DK (1) | DK366487A (en) |
FI (1) | FI92073C (en) |
NO (1) | NO170494C (en) |
SE (1) | SE465085B (en) |
Families Citing this family (36)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4859352A (en) * | 1988-02-29 | 1989-08-22 | Amoco Corporation | Low temperature high performance grease |
US4879054A (en) * | 1988-02-29 | 1989-11-07 | Amoco Corporation | Process for producing low temperature high performance grease |
JPH02248496A (en) * | 1989-03-23 | 1990-10-04 | Japan Atom Energy Res Inst | Lubricating grease |
US5207935A (en) * | 1989-03-31 | 1993-05-04 | Amoco Corporation | Wheel bearing grease |
GB2241707A (en) * | 1990-03-07 | 1991-09-11 | Exxon Research Engineering Co | Lubricating grease composition |
JP2512618B2 (en) * | 1990-08-31 | 1996-07-03 | 株式会社東海理化電機製作所 | Sliding contact grease |
US5133888A (en) * | 1990-09-28 | 1992-07-28 | Amoco Corporation | Cruise missile engine bearing grease |
US5902849A (en) * | 1991-11-07 | 1999-05-11 | Henkel Kommanditgesellschaft Auf Aktien | Filling compound |
DE4136617C2 (en) * | 1991-11-07 | 1997-08-14 | Henkel Kgaa | Filling compound and its use |
JP2795767B2 (en) * | 1991-12-27 | 1998-09-10 | 株式会社東海理化電機製作所 | Grease for sliding contacts |
US5372737A (en) * | 1993-09-17 | 1994-12-13 | Spauschus; Hans O. | Lubricating oil composition for refrigerant and method of use |
US5854185A (en) * | 1994-03-31 | 1998-12-29 | Shell Oil Company | Lubricant mixtures and grease compositions based thereon |
JP3324628B2 (en) * | 1994-11-18 | 2002-09-17 | 日本精工株式会社 | Low dusting grease composition |
US5558807A (en) * | 1995-05-19 | 1996-09-24 | Exxon Research And Engineering Company | Wax isomerate-based high temperature long bearing life grease |
US5783531A (en) * | 1997-03-28 | 1998-07-21 | Exxon Research And Engineering Company | Manufacturing method for the production of polyalphaolefin based synthetic greases (LAW500) |
US6207286B1 (en) | 1997-04-18 | 2001-03-27 | Alcoa Inc. | Lubricated sheet product and lubricant composition |
US6239085B1 (en) | 1998-10-23 | 2001-05-29 | Exxon Research And Engineering Company | Grease composition containing pao, alkylaromatic synthetic fluid and white oil for industrial bearings |
EP1013748B1 (en) * | 1998-12-22 | 2005-05-04 | Kyodo Yushi Co., Ltd. | Lubricating grease composition for bearings of electronic devices |
JP4328120B2 (en) * | 2003-03-31 | 2009-09-09 | 住友重機械工業株式会社 | Swing intermeshing planetary gear device and method for improving durability thereof |
US7829512B2 (en) * | 2003-10-17 | 2010-11-09 | Exxonmobil Research And Engineering Company | Method and equipment for making a complex lithium grease |
US7121365B2 (en) * | 2003-12-23 | 2006-10-17 | Smith International, Inc. | Rock bit with grease composition utilizing polarized graphite |
US20060211581A1 (en) * | 2005-03-17 | 2006-09-21 | Bullock Charles L Jr | Blend comprising group III and group IV basestocks |
US20060231450A1 (en) * | 2005-04-11 | 2006-10-19 | Ruby Gary V | Can bodies |
JP4687226B2 (en) * | 2005-04-28 | 2011-05-25 | 株式会社ジェイテクト | Rolling device using lubricating grease composition and electric power steering device using this rolling device |
US7413784B2 (en) * | 2006-06-19 | 2008-08-19 | Advanced Elastomer Systems, L.P. | Thermoplastic vulcanizates for potable water applications |
WO2008013697A2 (en) * | 2006-07-21 | 2008-01-31 | Exxonmobil Research And Engineering Company | Grease compositions |
EP2144979B1 (en) * | 2007-04-10 | 2018-08-29 | ExxonMobil Research and Engineering Company | Synthetic lubricating compositions |
US20090152754A1 (en) * | 2007-12-12 | 2009-06-18 | Sumitomo Chemical Company, Limited | Thermoplastic elastomer composition for foam injection molding, foam body, and process for producing foam body |
WO2009114599A2 (en) * | 2008-03-11 | 2009-09-17 | Baker Hughes Incorporated | Non-grease type bearing lubricant |
US8703675B2 (en) * | 2008-04-09 | 2014-04-22 | Saint-Gobain Performance Plastics Corporation | Bearing grease composition |
RU2529461C1 (en) * | 2013-08-30 | 2014-09-27 | Общество с ограниченной ответственностью "Инженерная смазочная компания "МИСКОМ" | Grease lubricant for heavily loaded rolling friction units |
JP6858501B2 (en) * | 2016-07-11 | 2021-04-14 | セイコーインスツル株式会社 | Grease, rolling bearings, rolling bearing devices and information recording / playback devices |
JP6777285B2 (en) * | 2016-11-30 | 2020-10-28 | 出光興産株式会社 | Mixed grease |
FR3060605B1 (en) | 2016-12-15 | 2021-05-28 | Skf Ab | GREASE COMPOSITIONS AND THEIR MANUFACTURING PROCESS |
FR3060604B1 (en) | 2016-12-15 | 2021-05-28 | Skf Ab | GREASE COMPOSITIONS AND THEIR MANUFACTURING PROCESS |
CN115572634A (en) * | 2022-10-21 | 2023-01-06 | 中国石油化工股份有限公司 | Composite lithium barium lubricating grease composition and preparation method thereof |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3114708A (en) * | 1960-12-29 | 1963-12-17 | Exxon Research Engineering Co | Dry polyolefin/oil blends |
US3813338A (en) * | 1970-05-06 | 1974-05-28 | Sun Oil Co | Textile-machinery lubricant composition |
US3939083A (en) * | 1972-04-04 | 1976-02-17 | Sun Oil Company Of Pennsylvania | Textile-machinery lubricant composition |
US4075113A (en) * | 1975-01-28 | 1978-02-21 | Labofina S.A. | Grease composition |
US4075112A (en) * | 1975-01-28 | 1978-02-21 | Labofina S.A. | Grease composition |
-
1986
- 1986-07-14 US US06/885,140 patent/US4749502A/en not_active Expired - Lifetime
-
1987
- 1987-07-01 SE SE8702725A patent/SE465085B/en not_active IP Right Cessation
- 1987-07-08 CA CA000541569A patent/CA1288410C/en not_active Expired - Lifetime
- 1987-07-13 FI FI873091A patent/FI92073C/en not_active IP Right Cessation
- 1987-07-13 NO NO872914A patent/NO170494C/en unknown
- 1987-07-14 DK DK366487A patent/DK366487A/en not_active Application Discontinuation
Also Published As
Publication number | Publication date |
---|---|
NO872914L (en) | 1988-01-15 |
FI873091A0 (en) | 1987-07-13 |
SE8702725D0 (en) | 1987-07-01 |
NO170494C (en) | 1992-10-21 |
DK366487A (en) | 1988-01-15 |
SE465085B (en) | 1991-07-22 |
US4749502A (en) | 1988-06-07 |
FI92073C (en) | 1994-09-26 |
SE8702725L (en) | 1988-01-15 |
DK366487D0 (en) | 1987-07-14 |
FI92073B (en) | 1994-06-15 |
NO872914D0 (en) | 1987-07-13 |
NO170494B (en) | 1992-07-13 |
FI873091A (en) | 1988-01-15 |
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