EP0119070A2 - Composition lubrifiante comprenant un copolymère d'éthylène-alphaoléfine - Google Patents

Composition lubrifiante comprenant un copolymère d'éthylène-alphaoléfine Download PDF

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Publication number
EP0119070A2
EP0119070A2 EP84301569A EP84301569A EP0119070A2 EP 0119070 A2 EP0119070 A2 EP 0119070A2 EP 84301569 A EP84301569 A EP 84301569A EP 84301569 A EP84301569 A EP 84301569A EP 0119070 A2 EP0119070 A2 EP 0119070A2
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EP
European Patent Office
Prior art keywords
viscosity
lubricants
low
shear
oils
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.)
Withdrawn
Application number
EP84301569A
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German (de)
English (en)
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EP0119070A3 (fr
Inventor
Frederick C. Loveless
Raymond F. Watts
Walter Nudenberg
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Uniroyal Inc
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Uniroyal Inc
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Publication of EP0119070A2 publication Critical patent/EP0119070A2/fr
Publication of EP0119070A3 publication Critical patent/EP0119070A3/fr
Withdrawn legal-status Critical Current

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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
    • C10M169/00Lubricating 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
    • C10M169/04Mixtures of base-materials and additives
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    • C10M105/00Lubricating compositions characterised by the base-material being a non-macromolecular organic compound
    • C10M105/08Lubricating compositions characterised by the base-material being a non-macromolecular organic compound containing oxygen
    • C10M105/32Esters
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    • C10M107/00Lubricating compositions characterised by the base-material being a macromolecular compound
    • C10M107/02Hydrocarbon polymers; Hydrocarbon polymers modified by oxidation
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    • C10M107/00Lubricating compositions characterised by the base-material being a macromolecular compound
    • C10M107/02Hydrocarbon polymers; Hydrocarbon polymers modified by oxidation
    • C10M107/04Polyethene
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    • C10M111/00Lubrication compositions characterised by the base-material being a mixture of two or more compounds covered by more than one of the main groups C10M101/00 - C10M109/00, each of these compounds being essential
    • C10M111/04Lubrication compositions characterised by the base-material being a mixture of two or more compounds covered by more than one of the main groups C10M101/00 - C10M109/00, each of these compounds being essential at least one of them being a macromolecular organic compound
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    • C10M127/00Lubricating compositions characterised by the additive being a non- macromolecular hydrocarbon
    • C10M127/04Lubricating compositions characterised by the additive being a non- macromolecular hydrocarbon well-defined aromatic
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    • C10M129/00Lubricating compositions characterised by the additive being an organic non-macromolecular compound containing oxygen
    • C10M129/02Lubricating compositions characterised by the additive being an organic non-macromolecular compound containing oxygen having a carbon chain of less than 30 atoms
    • C10M129/04Hydroxy compounds
    • C10M129/10Hydroxy compounds having hydroxy groups bound to a carbon atom of a six-membered aromatic ring
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    • C10M129/02Lubricating compositions characterised by the additive being an organic non-macromolecular compound containing oxygen having a carbon chain of less than 30 atoms
    • C10M129/26Carboxylic acids; Salts thereof
    • C10M129/28Carboxylic acids; Salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms
    • C10M129/38Carboxylic acids; Salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms having 8 or more carbon atoms
    • C10M129/42Carboxylic acids; Salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms having 8 or more carbon atoms polycarboxylic
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    • C10M133/02Lubricating compositions characterised by the additive being an organic non-macromolecular compound containing nitrogen having a carbon chain of less than 30 atoms
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    • C10M133/02Lubricating compositions characterised by the additive being an organic non-macromolecular compound containing nitrogen having a carbon chain of less than 30 atoms
    • C10M133/38Heterocyclic nitrogen compounds
    • C10M133/44Five-membered ring containing nitrogen and carbon only
    • C10M133/46Imidazoles
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    • C10M135/00Lubricating compositions characterised by the additive being an organic non-macromolecular compound containing sulfur, selenium or tellurium
    • C10M135/08Lubricating compositions characterised by the additive being an organic non-macromolecular compound containing sulfur, selenium or tellurium containing a sulfur-to-oxygen bond
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    • C10M135/20Thiols; Sulfides; Polysulfides
    • C10M135/28Thiols; Sulfides; Polysulfides containing sulfur atoms bound to a carbon atom of a six-membered aromatic ring
    • C10M135/30Thiols; Sulfides; Polysulfides containing sulfur atoms bound to a carbon atom of a six-membered aromatic ring containing hydroxy groups; Derivatives thereof
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    • C10M137/00Lubricating compositions characterised by the additive being an organic non-macromolecular compound containing phosphorus
    • C10M137/02Lubricating compositions characterised by the additive being an organic non-macromolecular compound containing phosphorus having no phosphorus-to-carbon bond
    • C10M137/04Phosphate esters
    • C10M137/10Thio derivatives
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    • C10M145/02Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • C10M145/10Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing monomers having an unsaturated radical bound to a carboxyl radical, e.g. acrylate
    • C10M145/12Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing monomers having an unsaturated radical bound to a carboxyl radical, e.g. acrylate monocarboxylic
    • C10M145/14Acrylate; Methacrylate
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    • C10M159/20Reaction mixtures having an excess of neutralising base, e.g. so-called overbasic or highly basic products
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Definitions

  • This invention relates to compositions useful as lubricating oils having high viscosity index, improved resistance to oxidative degradation and resistance to viscosity losses caused by permanent or temporary shear.
  • a lubricating composition comprising (1) a high viscosity ethylene-alphaolefin oligomer having a viscosity of from more than 3500 to 175,000 centistokes at 100°C; (2) a low viscosity synthetic hydrocarbon, such as alkylated benzene or low viscosity polyalphaolefin and/or a low viscosity ester, such as monoesters, diesters, polyesters and, optionally (3) an additive package.
  • a high viscosity ethylene-alphaolefin oligomer having a viscosity of from more than 3500 to 175,000 centistokes at 100°C
  • a low viscosity synthetic hydrocarbon such as alkylated benzene or low viscosity polyalphaolefin and/or a low viscosity ester, such as monoesters, diesters, polyesters and, optionally (3) an additive package.
  • An object of the invention is to provide a lubricating composition with properties not obtainable with conventional polymeric thickeners.
  • a further object of the invention is to provide lubricating compositions exhibiting improved shear stability, oxidative stability and excellent temperature-viscosity properties.
  • the viscosity-temperature relationship of a lubricating oil is one of the critical criteria which must be considered when selecting a lubricant for a particular application.
  • the mineral oils commonly used as a base for single and multigraded lubricants exhibit a relatively large change in viscosity with a change in temperature. Fluids exhibiting such a relatively large change in viscosity with temperature are said to have a low viscosity index.
  • the viscosity index of a common paraffinic mineral oil is usually given a value of about 100. Viscosity index (V.I. ) is determined according to ASTM Method D 2770-74 wherein the V.I. is related to kinematic viscosities measured at 40°C and 100°C.
  • Lubricating oils composed mainly of mineral oil are said to be single graded.
  • SAE grading requires that oils have a certain minimum viscosity at high temperatures and, to be multigraded, a certain maximum viscosity at low temperatures.
  • an oil having a viscosity of 10 cSt. at 100°C would be an SAE 30 and if that oil had a viscosity of 3400 cP. at -20°C, the oil would be graded 10W-30.
  • An unmodified mineral oil of 10 cSt. can not meet the low temperature requirements for a 10W-30 multigrade. rating, since its viscosity index dictates that it would have a viscosity considerably greater than 3500 cP. at -20°C, which is the maximum allowed viscosity for a 10W rating.
  • the viscosity requirements for qualification as multigrade engine oils are described by the SAE Engine Oil Viscosity Classification - SAE J300 SEP80, which became effective April 1, 1982.
  • the low temperature (W) viscosity requirements are determined by ASTM D 2602, Method of Test for Apparent Viscosity of Motor Oils at Low Temperature Using the Cold Cranking Simulator, and the results are reported in centipoise (cP).
  • the higher temperature (100°C) viscosity is measured according to ASTM D445, Method of Test for Kinematic Viscosity of Transparent and Opaque Liquids, and the results are reported in centistokes (cSt.).
  • the following table outlines the high and low temperature requirements for the recognized SAE grades for engine oils.
  • the 40°C viscosity estimated by linearly connecting the 100°C and -25°C viscosities would be about 70 cSt.
  • V.I. improved oils have viscosities at -25°C, which are considerably greater than predicted by linear extrapolation of the K.V.100 and K.V.40 values. Therefore, even having a V.I. of 180 does not guarantee the blend would be a 5W-40 oil.
  • V.I. improvers are traditionally high molecular weight rubbers whose molecular weights may vary from 10,000 to 1,000,000. Since the thickening power and V.I. increase are related to the molecular weight of the V.I. improver, most of these polymers normally have a molecular weight of at least 100,000.
  • Temporary shear is the result of the non-Newtonian viscometrics associated with solutions of high molecular weight polymers. It is caused by an alignment of the polymer chains with the shear field under high shear rates with a resultant decrease in viscosity. The decreased viscosity reduces the wear protection associated with viscous oils. Newtonian fluids maintain their viscosity regardless of shear rate.
  • Certain specific blends of high viscosity synthetic hydrocarbons, low viscosity synthetic hydrocarbons and/or low viscosity esters form base fluids from which superior crankcase or gear oils can be produced by the addition of the proper additive "packages". Besides exhibiting a broad range of viscosity the finished oils thus prepared exhibit an improved stability to permanent shear and, because of their nearly Newtonian nature, reduced temporary shear and so maintain the viscosity required for proper wear protection.
  • the oils of this invention have remarkably better stability toward oxidative degradation than those of the prior art.
  • the unexpectedly high viscosity indices produced from our base fluid blends permit the preparation of broadly multigraded crankcase fluids, such as OW-40 and gear oils such as 75W-250.
  • the high viscosity synthetic hydrocarbons have viscosities of 3500 to 175,000 cSt. may be polyalphaolefins, ethylene-alphaolefin oligomers (EP).
  • the high viscosity ethylene-alphaolefin oligomers of this invention are conveniently prepared by Ziegler catalysis. Many references exist covering methods of producing liquid oligomers of ethylene and alphaolefins (particularly propylene).
  • Polymerization is typically performed by subjecting the monomer mixture usually in a solvent to the combination of an organo aluminum compound and a vanadium or titanium compound.
  • the products formed can range from materials having viscosities as low as 20 cSt. to rubbery semi-solids depending on the choice of catalyst, the addition of molecular weight regulating species, temperature of polymerization and, especially, imposed hydrogen pressure.
  • low viscosity oligomers are prepared by the pyrolysis of high viscosity oligomers or rubbery solids.
  • Typical preparations of liquid ethylene-alphaolefin copolymers can be found in references, such as:
  • oligomers of ethylene and at least one other alphaolefin of this invention may be hydrogenated to increase their stability toward oxidation, the proper choice of polymerization catalysts in the presence of hydrogen often produces oligomers having very low levels of unsaturation directly.
  • the alphaolefins which can be used, singly or in combinations, with ethylene include linear alphaolefins of C 3 (propylene) to C 14 (tetradecene) and branched alphaolefins of the same molecular weight range, provided that the branch point is at least in the beta position to the double bond (e.g. 4-methyl pentene-1).
  • propylene and the lower molecular weight olefins are the preferred monomers in the preparation of the oligomers of ethylene and at least one other alphaolefin of this invention.
  • oligomeric ethylene-alpha olefin polymers which contain controlled amounts of unsaturation introduced by copolymerization with certain non-conjugated diene such as dicyclopentadiene, 5-ethylidene-2-norbornene and 1,4-hexadiene.
  • certain non-conjugated diene such as dicyclopentadiene, 5-ethylidene-2-norbornene and 1,4-hexadiene.
  • the introduction of unsaturation is sometimes desired if the oligomer is to be treated in any way to produce polar functionality thus giving the oligomer dispersant properties.
  • the low viscosity synthetic hydrocarbons of the present invention having viscosities of from 1 to 10 cSt., consist primarily of oligomers of alphaolefins and/or alkylbenzenes.
  • Low molecular weight oligomers of alphaolefins from C 8 (octene) to C 12 (dodecene) or mixtures of the olefins can be utilized.
  • Low viscosity alphaolefin oligomers can be produced by Ziegler catalysis, thermal polymerization, free radically catalyzed polymerization and, preferably, BF 3 catalyzed polymerization.
  • BF 3 catalyzed polymerization preferably, BF 3 catalyzed polymerization.
  • a host of similar processes involving BF 3 in conjunction with a cocatalyst is known in the patent literature.
  • a typical polymerization technique is described in United States Patent No. 4,045,508.
  • the alkylbenzenes may be used in the present invention alone or in conjunction with low viscosity polyalphaolefins in blends with high viscosity synthetic hydrocarbons and low viscosity esters.
  • the alkylbenzenes prepared by Friedel-Crafts alkylation of benzene with olefins are usually predominantly dialkylbenzenes wherein the alkyl chain may be 6 to 14 carbon atoms long.
  • the alkylating olefins used in the preparation of alkyl benzenes can be straight or branched chain olefins or combinations. These materials may be prepared as shown in U.S.P. 3,909,432.
  • the low viscosity esters of this invention having viscosities of from 1 to 10 cSt. can be selected from classes of esters readily available commercially, e.g., monoesters prepared from monobasic acids such as pelargonic acid and alcohols; diesters prepared from dibasic acids and alcohols or from diols and monobasic acids or mixtures of acids; and polyol esters prepared from diols, triols (especially trimethylol propane), tetraols (such as pentaerythritol), hexaols (such as dipentaerythritol) and the like reacted with monobasic acids or mixtures of acids.
  • monoesters prepared from monobasic acids such as pelargonic acid and alcohols
  • diesters prepared from dibasic acids and alcohols or from diols and monobasic acids or mixtures of acids
  • esters examples include tridecyl pelargonate, di-2 ethylhexyl adipate, di-2-ethylhexyl azelate, trimethylol propane triheptanoate and pentaerythritol tetraheptanoate.
  • esters and mixtures of esters derived from natural sources, plant or animal are those esters and mixtures of esters derived from natural sources, plant or animal. Examples of these materials are the fluids produced from jojoba nuts, tallows, safflowers and sperm whales.
  • esters used ought to be carefully selected to insure compatibility of all components in finished lubricants of this invention. If esters having a high degree of polarity (roughly indicated by oxygen content) are blended with certain combinations of high viscosity synthetic hydrocarbons and low viscosity synthetic hydrocarbons, phase separation can occur at low temperatures with a resultant increase in apparent viscosity. Such phase separation is detrimental to long term storage of lubricants under a variety of temperature conditions.
  • the additive "packages" mixed with the recommended base oil blend for the production of multigraded crankcase fluids or gear oils are usually combination of various types of chemical additives so chosen to operate best under the use conditions which the particular formulated fluid may encounter.
  • Additives can be classified as materials which either impart or enhance a desirable property of the base lubricant blend into which they are incorporated. While the general nature of the additives might be the same for various types or blends of the base lubricants, the specific additives chosen will depend on the particular type of service in which the lubricant is employed and the characteristics of the base lubricants.
  • a finished lubricant will contain several and possibly most or all of the above types of additives in what is commonly called an "additive package.”
  • the development of a balanced additive package involves considerably more work than the casual use of each of the additive types. Quite often functional difficulties arising from combinations of these materials show up under actual operating conditions. On the other hand, certain unpredictable synergistic effects of a desirable nature may also become evident. The only methods currently available for obtaining such data are from extensive full scale testing both in the laboratory and in the field. Such testing is costly and time-consuming.
  • Dispersants have been described in the literature as “detergents”. Since their function appears to be one of effecting a dispersion of particulate matter, rather than one of "cleaning up” any existing dirt and debris, it is more appropriate to categorize them as dispersants.
  • Materials of this type are generally molecules having a large hydrocarbon "tail” and a polar group head.
  • the tail section an oleophilic group, serves as a solubilizer in the base fluid while the polar group serves as the element which is attracted to particulate contaminants in the lubricant.
  • the dispersants include metallic and ashless types.
  • the metallic dispersants include sulfonates (products of the neutralization of a sulfonic acid with a metallic base), thiophosphonates (acidic components derived from the reaction between polybutene and phosphous pentasulfide) and phenates and phenol sulfide salts (the broad class of metal phenates includes the salts of alkylphenols, alkylphenol sulfides, and alkyl phenol aldehyde products).
  • the ashless type dispersants may be categorized into two broad types: high molecular weight polymeric dispersants for the formulation of multigrade oils and lower molecular weight additives for use where viscosity improvement is not necessary.
  • the compounds useful for this purpose are again characterized by a "polar" group attached to a relatively high molecular weight hydrocarbon chain.
  • the "polar” group generally contains one or more of the elements-nitrogen, oxygen, and phosphorus.
  • the solubilizing chains are generally higher in molecular weight than those employed in the metallic types; however, in some instances they may be quite similar.
  • Some examples are N-substituted long chain alkenyl succinimides, high molecular weight esters, such as products formed by the esterification of mono or polyhydric aliphatic alcohols with olefin substituted succinic acid, and Mannich bases from high molecular weight alkylated phenols.
  • the high molecular weight polymeric ashless dispersants have the general formula:
  • an oxidation inhibitor is the prevention of a deterioration associated with oxygen attack on the lubricant base fluid. These inhibitors function either to destroy free radicals (chain breaking) or to interact with peroxides which are involved in the oxidation mechanism.
  • oxidation inhibitors include the phenolic types (chain-breaking) e.g., 2,6-di-tert.-butyl-para- cresol and 4,4'-methylenebis(2,6-di-tert.-butylphenol), and the zinc dithiophosphates (peroxide-destroying).
  • Wear is loss of metal with subsequent change in clearance between surfaces moving relative to each other. If continued, it will result in engine or gear malfunction.
  • the principal factors causing wear are metal-to-metal contact, presence of abrasive particulate matter, and attack of corrosive acids.
  • Metal-to-metal contact can be prevented by the addition of film-forming compounds which protect the surface either by physical absorption or by chemical reaction.
  • the zinc dithiophosphates are widely used for this purpose. These compounds were described under anti-oxidant and anti-bearing corrosion additives. Other effective additives contain phosphorus, sulfur or combinations of these elements.
  • Abrasive wear can be prevented by effective removal of particulate matter by filtration while corrosive wear from acidic materials can be controlled by the use of alkaline additives such as basic phenates and sulfonates.
  • conventional viscosity improvers are often used in "additive packages" their use should not be necessary for the practice of this invention since our particular blends of high and low molecular weight base lubricants produce the same effect.
  • These materials are usually oil-soluble organic polymers with molecular weights ranging from approximately 10,000 to 1,000,000. The polymer molecule in solution is swollen by the lubricant. The volume of this swollen entity determines the degree to which the polymer increases its viscosity.
  • pour point depressants prevent the congelation of the oil at low temperatures. This phenomenon is associated with the crystallization of waxes from the lubricants. Chemical structures of representative commercial pour point depressants are:
  • Chemicals employed as rust inhibitors include sulfonates, alkenyl succinic acids, substituted imidazolines, amines, and amine phosphates.
  • the anti-foam agents include the silicones and miscellaneous organic copolymers.
  • Additive packages known to perform adequately for their recommended purpose are prepared and supplied by several major manufacturers. The percentage and type of additive to be used in each application is recommended by the suppliers. Typically available packages are:
  • a typical additive package for an automotive gear lubricant would normally contain antioxidant, corrosion inhibitor, anti-wear agents, anti-rust agents, extreme pressure agent and foam inhibitor.
  • a typical additive package for a crankcase lubricant would normally be comprised of a dispersant, antioxidant, corrosion inhibitor, anti-wear agent, anti-rust agent and foam inhibitor.
  • An additive package useful for formulating a compressor fluid would typically contain an anti-oxidant, anti-wear agent, an anti-rust agent and foam inhibitor.
  • This invention describes blends of high viscosity synthetic hydrocarbons, having a viscosity range of 3500 to 175,000 cSt. with one or more synthetic hydrocarbon fluids having viscosities in the range of 1 to 10 cSt. and/or one or more compatible ester fluids having a viscosity range of 1 to 10 cSt.
  • Such blends when treated with a properly chosen additive "package,” can be formulated in broad range multigraded crankcase or gear oils having improved shear stability, improved oxidative stability, and nearly Newtonian viscometric properties.
  • the blends of this invention also find uses in certain applications where no additive need be employed.
  • the high viscosity synthetic hydrocarbon provides thickening and VI improvement to the base oil blend.
  • the low viscosity synthetic hydrocarbon fluid is frequently the main ingredient in the base oil blend, particularly in finished lubricants having an SAE viscosity grade of 30 or 40. While certain low viscosity esters are insoluble in high viscosity synthetic hydrocarbons, the presence of low viscosity synthetic hydrocarbon, being a better solvent for low viscosity esters, permits greater variations in the type of esters used in base oil blends of high viscosity synthetic hydrocarbons, low viscosity synthetic hydrocarbons, and low viscosity esters.
  • Crankcase and gear oils consisting solely of hydrogenated polyisoprene oligomers and low viscosity synthetic hydrocarbons with the proper additives produce synthetic fluids having excellent oxidative and hydrolytic stability.
  • Such fluids are exemplified in Examples 1 and 3.
  • the third component, low viscosity esters can be added to produce the superior lubricants of this invention.
  • High viscosity synthetic hydrocarbons and low viscosity synthetic hydrocarbons can be used alone to produce multigraded lubricants.
  • the addition of low levels of low viscosity esters, usually 1-25% results in a base oil blend superior to blends of high viscosity synthetic hydrocarbons and low viscosity synthetic hydrocarbons alone in low temperature fluidity (see Examples 2 and 4).
  • the components of the finished lubricants of this invention can be admixed in any convenient manner or sequence.
  • An important aspect of the present invention is in the use of the properly constituted base oil blend in combination with the proper compatible additive package to produce finished broad-range multigrade lubricants having:
  • the lubricants of this invention when properly formulated, approach viscometrics of Newtonian fluids. That is, their viscosities are changed little over a wide range of shear rates. While the EAO of the invention may, in themselves, display non-Newtonian characteristics, particularly at low temperatures, the final lubricant products utilizing low viscosity oils as diluents are much more Newtonian.
  • the thickening fluids of high viscosity synthetic hydrocarbons of this invention all have molecular weights below 10,000, and shear thinning of their solutions is minimal.
  • the shear rates developed in pistons and gears (equal to or greater than 10 6 sec -1 ) is such that, depending on the polymeric thickener used, the apparent viscosity of the oils approaches that of the unthickened base fluids resulting in loss of hydrodynamic films. Since wear protection of moving parts has been correlated with oil viscosity, it is apparent that the wear characteristics of a lubricant can be downgraded as a result of temporary shear.
  • the Newtonian fluids of the current invention maintain their viscosity under these use conditions and therefore afford more protection to and hence longer lifetime for the machinery being lubricated.
  • the reduced temporary shear exhibited by the lubricants of this invention provides higher viscosity for the protection of moving parts where high shear rates are encountered.
  • SAE grading e.g. SAE 30
  • SAE 30 relied only on a measurement of the viscosity of a fluid at 100°C under low shear conditions, despite the fact that in machinery such as a crankcase high temperatures and very high shear rates are encountered.
  • This disparity has led to the adoption in Europe of a new grading system wherein viscosities for a certain grade are those measured at 150°C and 10 6 sec -1 shear rate. This more realistic approach is currently being considered in the United States.
  • the advantages a Newtonian fluid brings to such a grading system are obvious to anyone skilled in the art.
  • the viscosity of a Newtonian fluid can be directly extrapolated to 150°C under high shear conditions.
  • a polymer thickened fluid will invariably have a viscosity lower than the extrapolated value, frequently close to the base fluid itself.
  • polymer thickened oils will require a more viscous base fluid.
  • the use of thicker base fluids will produce higher viscosities at low temperature making it more difficult to meet the low temperature (5W for crakcase of 75W for gear oil) requirements for broadly multigraded oils.
  • Viscosity index is determined by low shear viscosity measurements at 40°C and 100°C.
  • the nearly Newtonian lubricants of this invention not only produce high viscosity index multigraded fluids which stay "in grade", but the V.I. and multigrade rating are realistic since they are not very sensitive to shear rate.
  • the invention uses a high viscosity ethylene-alphaolefin oligomer having a viscosity of 3500 to 175,000 cSt at 100°C.
  • a shear stability decreases.
  • the high viscosity oligomers of the invention exhibit an improvement over the V.I. improvers of the prior art. This is particularly true for broadly graded lubricants such as 75W-250 gear oils and OW-40 crankcase oils.
  • This example illustrates the preparation of automotive gear oils using an ethylene-propylene oligomer (EAO), having a kinematic viscosity @ 100°C of 25,700 cSt, with synthetic hydrocarbon.
  • EAO ethylene-propylene oligomer
  • the lubricants had the properties shown:
  • the lubricants had the properties shown:
  • This example illustrates the preparation of crankcase oil using EAO's of the kinematic viscosities shown in blends containing only synthetic hydrocarbon.
  • the lubricants had the properties shown:
  • This example illustrates the preparation of automotive gear lubricants using an EAO of the indicated kinematic viscosity in combination with ester and low viscosity hydrocarbon.
  • the lubricants had the properties shown:
  • the lubricants had the properties shown:

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  • Chemical & Material Sciences (AREA)
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  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
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  • Lubricants (AREA)
EP84301569A 1983-03-09 1984-03-08 Composition lubrifiante comprenant un copolymère d'éthylène-alphaoléfine Withdrawn EP0119070A3 (fr)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005028599A1 (fr) * 2003-09-13 2005-03-31 Exxonmobil Chemical Patents Inc. Compositions lubrifiantes pour engrenages automobiles
US8318993B2 (en) 2002-03-05 2012-11-27 Exxonmobil Research And Engineering Company Lubricant blend composition
WO2014209712A1 (fr) * 2013-06-28 2014-12-31 Dow Global Technologies Llc Procédé pour la préparation de polyoléfines ramifiées pour des applications comme lubrifiants

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1246880A (en) * 1969-06-30 1971-09-22 Exxon Research Engineering Co Ethylene/alpha-olefin polymers and lubricating oils containing them
US3634249A (en) * 1967-11-20 1972-01-11 Exxon Research Engineering Co Lubricating oil composition
EP0088453A1 (fr) * 1982-03-10 1983-09-14 UNIROYAL CHEMICAL COMPANY, Inc. Composition lubrifiante

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3634249A (en) * 1967-11-20 1972-01-11 Exxon Research Engineering Co Lubricating oil composition
GB1246880A (en) * 1969-06-30 1971-09-22 Exxon Research Engineering Co Ethylene/alpha-olefin polymers and lubricating oils containing them
EP0088453A1 (fr) * 1982-03-10 1983-09-14 UNIROYAL CHEMICAL COMPANY, Inc. Composition lubrifiante

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8318993B2 (en) 2002-03-05 2012-11-27 Exxonmobil Research And Engineering Company Lubricant blend composition
WO2005028599A1 (fr) * 2003-09-13 2005-03-31 Exxonmobil Chemical Patents Inc. Compositions lubrifiantes pour engrenages automobiles
US7585823B2 (en) 2003-09-13 2009-09-08 Exxonmobil Chemical Patents Inc. Lubricating fluids with enhanced energy efficiency and durability
WO2014209712A1 (fr) * 2013-06-28 2014-12-31 Dow Global Technologies Llc Procédé pour la préparation de polyoléfines ramifiées pour des applications comme lubrifiants
US9963648B2 (en) 2013-06-28 2018-05-08 Dow Global Technologies Llc Process for the preparation of branched polyolefins for lubricant applications

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BR8401058A (pt) 1984-10-16

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