LUBRICATING OIL COMPOSITION

Abstract: Disclosed is a lubricating oil composition comprising, as indispensable components, (A) a synthetic hydrocarbon lubricating oil, (B) a load-withstanding additive and (C) a liquid ethylene/α-olefin random copolymer modified by graft copolymerisation with an unsaturated carboxylic acid or a derivative thereof. In this lubricating oil composition, the load-withstanding oil is homogeneously and stably incorporated. This lubricating oil is significant in that the poor compatibility with a load-withstanding additive, which is the defect of synthetic hydrocarbon lubricating oils, is effectively overcome.

Description: The present invention relates to a lubricating oil composition comprising a synthetic hydrocarbon lubricating oil as the base oil. More particularly, the present invention relates to a lubricating oil composition excellent in the compatibility with an extreme pressure agent. Refined petroleum type lubricating oils and synthetic hydrocarbon type lubricating oils are known as typical examples of lubricating oils. Refined petroleum type lubricating oils easily deteriorate due to oxidation of the structurally unstable double bonds. Furthermore, since the molecular weight is generally low (less than 500), the evaporation loss is large and the abrasion resistance is insufficient. In contrast, the synthetic hydrocarbon type lubricating oils are structurally more stable than the refined petroleum type lubricating oils, and their molecular weight can be adjusted within a broad range. Especially, if a specific monomer is selected and polymerized, it is possible to give such characteristics as a low power point and a high viscosity index to the lubricating oil. Load-withstanding additives are known for use in lubricating oils to impart a load-carrying capacity to a base oil at boundary lubrication and extreme pressure lubrication. There are two main types of load-withstanding additive: oilness agents and extreme pressure agents. Oilness agents are compounds capable of reducing the friction coefficient by physical or chemical adsorption on the friction surface. As oilness agents, there can be mentioned higher fatty acids such as oleic acid and stearic acid, higher alcohols such as oleyl alcohol, stearyl alcohol and palmityl alcohol, and higher amines such as oleylamine, stearylamine and palmitylamine. Extreme pressure agents are compounds capable of preventing wear or seizure by direct reaction with the metal surface under local high-temperature and high-pressure conditions while forming an extreme pressure coating or forming a coating of a thermal decomposition product of the additive on the friction surface. However, these synthetic hydrocarbon type lubricating oils have poor compatibility with the load-withstanding additives generally incorporated into a lubricating oils, and therefore, the use of these synthetic lubricating oils is restricted. The present invention provides a lubricating oil which comprises (A) 100 parts by weight of synthetic hydrocarbon lubricating oil selected from poly-α-olefin oils and ethylene/α-olefin random copolymer oils (B) 0.1 to 20 parts by weight of an extreme pressure agent and (C) 0.8 to 200 parts by weight of a liquid graft-modified ethylene/α-olefin random copolymer comprising an ethylene α-olefin random copolymer containing 30 to 75 % of ethylene graft-substituted by the residues of an unsaturated carboxylic acid or a derivative thereof, at a grafting ratio of 0.2 to 50 parts by weight of the unsaturated carboxylic acid or derivative thereof per 100 parts by weight of the ethylene/α-olefin random copolymer, the liquid graft-modified copolymer having an intrinsic viscosity [η], as measured in decalin at 135°C, in the range of from 0.01 to 0.3 dl/g and a molecular wight distribution ( Mw / Mn ), as determined by gel permeation chromatography, not larger than 4. The composition of the present invention is characterised in that an extreme pressure agent is used as load-withstanding additive and in that a predetermined amount of a liquid modified ethylene/α-olefin random copolymer [component (C)] is incorporated in addition to the synthetic hydrocarbon lubricating oil [component (A)] and the extreme pressure agent [component (B)]. By incorporating a predetermined amount of the liquid modified ethylene/α-olefin random copolymer, the compatibility of the synthetic hydrocarbon lubricating oil with the extreme pressure agent is improved and the respective components can be homogeneously incorporated. Furthermore, since the liquid modified ethylene/α-olefin random copolymer used in the present invention has a lubricating effect by itself, this modified random copolymer improves the lubricating effect without degrading the characteristics of the unmodified ethylene/α-olefin random copolymer that can be a synthetic hydrocarbon lubricating oil as the base oil. The present invention will now be described in detail. Synthetic Hydrocarbon Lubricating Oil (A) Known lubricating oils are used as the base oil in the present invention. There can be used poly(α-olefin) oils such as polydecene-1 or a polybutene oil, ethylene/α-olefin random copolymer oils such as an ethylene/propylene random copolymer oils. As the poly-α-olefin oil (for example, low-molecular-weight oligomer of an α-olefin) there can be utilized, for example, low-molecular-weight oligomers of α-olefins having 3 to 20, especially 8 (octene) to 12 (dodecene) carbon atoms and mixtures of these α-olefins. Low-viscosity α-olefin oligomers can be produced by Ziegler catalysis, thermal polymerisation and free radically catalyzed polymerisation, preferably BF₃ catalysed polymerisation. A number of similar processes using BF₃ in conjunction with a cocatalyst are known and disclosed in literature references. A typical polymerisation technique is taught in the specification of U.S. Patent No. 4,045,508. Alkylbenzenes can be used in the present invention in conjunction with low-viscosity poly-α-olefins in blends with high-viscosity synthetic hydrocarbons and low-viscosity esters. The alkylbenzenes prepared by Friedel-Crafts alkylation of benzene with an olefin are usually predominantly dialkylbenzenes where the alkyl chain has 6 to 14 carbon atoms. the alkylating olefins used in the preparation of alkylbenzenes can be linear or branched olefins or mixtures thereof. These materials can be prepared according to the process disclosed in the specification of U.A. Patent No. 3,909,432. Of these lubricating oils, a poly-α-olefin oil, especially a poly-α-olefin oil having a viscosity of : 1-20 mm²/s (1 to 20 cst), and an unmodified ethylene/α-olefin random copolymer used as the base of the liquid modified ethylene/α-olefin random copolymer as the component (C) described hereinafter are especially preferably used. Extreme Pressure Agent (B) All of the known extreme pressure agents can be used in the present invention. For example, there can be mentioned sulfur type extreme pressure agents such as dibutyldithiocarbamic acid sulfide and dibenzyl sulfide, phosphorus type extreme pressure agents such as dibutyl phosphate and diphenyl phosphate, halogen type extreme pressure agents such as oleyl chloride and chlorinated paraffin, and organic metal type extreme pressure agents such as zinc dithiophosphate, molybdenum dithiophosphate and lead naphthenate. In general, sulfur type extreme pressure agents have excellent seizure resistance, and phosphorus type extreme pressure agents have excellent wear resistance. It is preferred that a sulfur type extreme pressure agent and a phosphorus type extreme pressure agent be used in combination. The above-mentioned load-withstanding additives can be appropriately used singly or in the form of a mixture of two or more of them according to the intended use of the lubricant. Liquid Modified random Copolymer (C) In the present invention, a liquid modified ethylene/α-olefin random copolymer is used in addition to the above-mentioned components (A) and (B). The liquid modified random copolymer is a copolymer obtained by graft-modifying a liquid ethylene/α-olefin random copolymer formed from ethylene and an α-olefin having 3 to 20 carbon atoms (often called "unmodified copolymer" hereinafter). As the α-olefin, there can be used α-olefins having 3 to 20 carbon atoms, such as propylene, l-butene, 1-hexene, 4-methyl-1-pentene, 3-methyl-1-pentene, 1-octene, 1-decene, 1-dodecene, 1-tetradecene, 1-hexadecene, 1-octadecene and 1-eicosane. In the unmodified copolymer used for the preparation of the modified random copolymer in order to obtain effect of the present invention, that is the effect of improving the compatibility, it is preferred that the ethylene content (a) should be 30 to 75 mole%, especially 40 to 70 mole%, and the α-olefin content (b) should be 25 to 70 mole%, especially 30 to 60 mole% (the total amount of ethylene and the α-olefin is 100 mole%). As the unmodified liquid copolymer, there is used an unmodified copolymer having an intrinsic viscosity of 0.01 to 0.3 dℓ/g, preferably 0.03 to 0.25 dℓ/g, as measured in decalin at 135°C, a number average molecular weight ( Mn ) of 300 to 12000, preferably 500 to 8000, especially preferably 500 to 4,000 and a molecular weight distribution ( Mw / Mn ) of 1.1 to 4, preferably 1.2 to 3, as measured by the GPC method. An unmodified liquid copolymer having a Z value of 10 to 300, especially 15 to 250, and a σ value of 0 to 3, especially 0 to 2, is preferably used. Incidentally, the ethylene content/propylene content ratio in the ethylene/α-olefin random copolymer is determined according to the infrared absorption spectrum method, and the intrinsic viscosity, molecular weight distribution, number average molecular weight, Z value and σ value are determined according to the following methods. (1) Intrinsic Viscosity (η) (dℓ/g) The intrinsic viscosity is measured in decalin at 135°C . (2) Molecular Weight Distribution The molecular weight distribution is defined as the ratio of the weight average molecular weight ( Mw ) to the number average molecular weight ( Mn ) and is measured by the gel permeation chromatography (GPC) method. (3) The number average molecular is measured by the GPC method. (4) Z value The Z value is the ratio of the maximum value of the molecular weight to the minimum value of the molecular weight determined in accordance with the GPC method described in detail hereinafter. (5) σ Value The σ value is calculated in accordance with the following formula: by fractionating the copolymer with acetone/hexane mixed solvents differing in the mixing proportion, and finding the ethylene content (Ei) and the weight ratio (Wi) based on the total weight of the copolymer, of the copolymer extracted in the i-th fraction. The σ value is a measure indicating the composition distribution of the copolymer. More specific methods of determining the molecular weight distribution, the number average molecular weight and the Z value are described below. The number average molecular weight and weight average molecular weight of the copolymer are measured by the following method, which is described in detail in Journal of Polymer Science, Part A-II, vol. 8, pages 89-103 (1970). Elution counts of a standard substance having a known molecular weight (16 samples of monodisperse polystyrene having differnet molecular weights selected from the range of 500 to 840 x 10⁴) are measured by GPC (gel permeation chromatography), and a calibration curve showing the relation between the molecular weight and the elution count is prepared. The GPC pattern of a copolymer sample is taken by GPC. From the calibration curve, the molecular weights (Mi) at the individual counts (i) are read, and from the GPC pattern, the elution volumes (Ni) at the individual counts (i) are read. The number average molecular weight ( Mn ) and weight average molecular weight ( Mw ), both as polystyrene, of the copolymer sample are calculated in accordance with the following equations: Mn = ΣMiNi/ΣNi, and Mw = ΣMi²Ni/ΣMiNi Separately, the molecular weight, calculated as polystyrene, of aqualane (an isoparaffinic standard substance having a molecular weight of 422) is measured by GPC. Thus, the Mn , Q value and Z value of the copolymer of the present invention are calculated by the following equations: The minimum and maximum elution counts of the GPC pattern of the copolymer are read, and the corresponding minimum and maximum molecular weights of the copolymer, calculated as polystyrene, are read from the calibration curve. The Z curve is calculated from the following equation: Specific examples of the α-olefin having 3 to 20 carbon atoms, to be copolymerized with ethylene in the preparation of the ethylenic random copolymer as a base polymer, include propylene, l-butene, 1-hexene, 4-methyl-1-pentene, 3-methyl-1-pentene, 1-octone, 1-docene, 1-dodecene, 1-tetradecene, 1-hexadecene, 1-octadecene and 1-eicosene, α-olefin having 3 to 10 carbon atoms, such as propylene, 1-butene, 1-hexene, 1-octene and 1-decene, particularly propylene and 1-butene, are preferred. They may be used either singly or in combination. The copolymerization of ethylene with the α-olefin can be carried out by using ziegler catalysts known per se, preferably by the methods disclosed in Japanese Patent Application Laid-Open Specifications Nos. 117595/82 and 123205/82 and European Patent Application 60609 (A·1). For example, Japanese Patent Application Laid-Open Specification No. 123205/82 discloses a method for copolymerizing ethylene with an α-olefin having at least 3 carbon atoms in the liquid phase in the presence of hydrogen by using a catalyst formed from a soluble vanadium compound and an organoaluminum compound. In this method, the copolymerization is carried out continuously. The concentration of the vanadium compound in the polymerization system is adjusted to at least 0.3 millimole per liter of the liquid phase, and the vanadium compound to be fed to the polymerization system is used as diluted in a polymerization medium so that its concentration is not more than 5 times the concentration of the vanadium compound in the polymerization system. The ethylene random copolymer used as a base in the present invention is preferably liquid at normal temperature. The liquid modified random copolymer used in the present invention is obtained by graft-modifying the above-mentioned unmodified copolymer with an unsaturated carboxylic acid or a derivative thereof. An unsaturated carboxylic acid having 3 to 20 carbon atoms, preferably 3 to 10 carbon atoms, or a derivative thereof is used as the unsaturated carboxylic acid or its derivative as the grafting comonomer component. For example, there can be mentioned unsaturated carboxylic acids such as acrylic acid, methacrylic acid, maleic acid, fumaric acid, itaconic acid, citraconic acid, tetrahydrophthalic acid and bicyclo[2,2,1]hept-2-ene-5,6-dicarboxylic acid, unsaturated carboxylic acid anhydrides such as maleic anhydride, itaconic anhydride, citraconic anhydride, tetrahydrophthalic anhydride and bicyclo[2,2,1]-hept-2-ene-5,6-dicarboxylic acid anhydride, and esters of unsaturated carboxylic acids such as methyl acrylate, methyl methacrylate, dimethyl maleate, monomethyl maleate, diethyl fumarate, dimethyl itaconate, diethyl citraconate, dimethyl tetrahydrophthalate and dimethyl bicyclo[2,2,1]-hept-2-ene-5,6-dicarboxylate. Of these compounds, maleic anhydride is especially preferred. In the present invention, in order to improve the compatibility, it is preferred that the grafting ratio of the unsaturated carboxylic acid or its derivative should be 0.2 to 50 parts by weight, especially 0.5 to 40 parts by weight, per 100 parts by weight of the unmodified ethylene α-olefin copolymer. In the present invention, in order to improve the compatibility of the component (B) with the load-withstanding additive, it is preferred that the intrinsic viscosity [η] of the liquid modified ethylene type random copolymer should be 0.01 to 0.3 dℓ/g, especially 0.03 to 0.25 dℓ/g, as measured in decalin at 135°C., and the molecular weight distribution ( Mw / Mn ) is not larger than 4, especially from 1.2 to 3, as measured by the gel permeation chromatography (GPC). In the present invention, the number average molecular weight of the above-mentioned liquid modified ethylene type copolymer is ordinarily 310 to 8000 and preferably 500 to 4000. Incidentally, the liquid modified random copolymer can be prepared from the unmodified copolymer according to the process previously proposed by us in Japanese Patent Application Laid-Open Specification No. 123205/82 and EP Laid-Open No. 183493. The liquid modified random copolymer of this invention can be produced by reacting (graft copolymerizing) the ethylenic random copolymer with the modifier in the presence of a radical initiator. The reaction can be carried out usually in an inert gas atmosphere in the presence of a solvent, or in the absence of a solvent. The reaction can be carried out, for example, by continuously or intermittently feeding the modifier compound and the radical initiator with stirring to the heated liquid ethylenic random copolymer in the presence or absence of a solvent. The proportions of the modifier and the radical initiator fed in this graft copolymerization reaction, and the reaction temperature and time can be varied depending upon the type of the modifier, etc. Generally, these reaction conditions may be selected as tabulated below according to the type of the modifier compound. Usually organic peroxides are used as the radical initiator for the graft copolymerization reaction. The organic peroxides preferably have a decomposition temperature, at which the half value is 1 minute, of 60 to 270°C, especially 150 to 270°C. Specific examples are organic peroxides and organic peresters, such as benzoyl peroxide, dichlorobenzoyl peroxide, dicumyl peroxide, di-tert-butyl peroxide, 2,5-dimethyl-2,5-di(peroxybenzoate)hexyne-3, 1,4-bis(tert-butylperoxyisopropyl)benzene, lauroyl peroxide, tert-butyl peracetate, 2,5-dimethyl-2,5-di(tert-butylperoxy)hexyne-3, 2,5-di-methyl-2,5-di(tert-butylperoxy)hexane, tert-butyl perbezoate, tert-butyl perphenylacetate, tert-butyl perisobutyrate, tert-butyl per-sec-octoate, tert-butyl perpivalate, cumyl perpivalate and tert-butyl perdiethylacetate. Examples of the solvent that can be used are aromatic hydrocarbons such as benzene, toluene, xylene, monochlorobenzene and dichlorobenzene, and aliphatic or alicyclic hydrocarbons or halogenation products thereof, such as pentane, hexane, cyclohexane, heptane, and octane. The aromatic hydrocarbon solvent is preferred. The absence of solvent is also preferred. The separation of the modified ethylenic random copolymer from the reaction mixture and its purification may be carried out by methods known per se , for example by distillation or solvent fractionation. Preparation of Lubricating Oil Composition The lubricating oil composition of the present invention can be easily prepared by incorporating (B) 0.1 to 20 parts by weight, especially 1 to 15 parts by weight, of a load-withstanding additive and (C) 0.8 to 200 parts by weight, especially 1 to 150 parts by weight, of a liquid modified ethylene/α-olefin random copolymer into (A) 100 parts by weight of a synthetic hydrocarbon lubricating oil. The incorporation may be carried out at ordinary temperature (25°C) or under heating. However, there is preferably adopted a method in which the components (B) and (C) are mixed in advance under heating (50 to 250°C) and the lubricating oil (A) as the base oil is added to the mixture. In order to obtain a good compatibility, it is preferred that the load-withstanding additive (B) and the liquid modified ethylene/α-olefin random copolymer (C) be mixed at a mixing (C)/(B) weight ratio of from 0.05 to 200, especially from 1 to 150. In the lubricating oil composition of the present invention, in addition to the foregoing three components (A) through (C), there may be incorporated a refined petroleum lubricating oil or a synthetic lubricating oil such as a polyether oil, an ester oil or silicon oil in an amount of up to 100% by weight based on the synthetic hydrocarbon lubricating oil as the component (A). Furthermore, known additives, for example, viscosity index improvers such as polymethacrylic acid esters, polyisobutylene, styrene/isoprene/styrene block copolymers and styrene/butadiene/styrene block copolymers, pour point depressants such as chlorinated paraffin/naphthalene condensates and polyalkyl methacrylates, rust-preventive agents such as dodecylamine and dodecyl ammonium stearate, detergent dispersants such as metal salts of alkyl aromatic sulfonic acids and succinimide, defoaming agents such as dimethyl polysiloxane, colorants such as oil-soluble dyes and anti-oxidants such as phenolic compounds and amine compounds may be added. The amounts incorporated of these additives differ according to the kinds of the additives, but in general, the additives are incorporated in amounts of 0.1 to 10% by weight based on the synthetic hydrocarbon lubricating oil. The lubricating oil composition of the present invention is excellent in the liquid stability, and even if various load-withstanding additives are incorporated, precipitates are not formed at all and the compatibility is very good. This quality is very important and valuable as is seen from the fact that JIS K-2215 concerning the quality of a lubricating oil for an internal combustion engine stipulates that water or precipitates should not be contained. Furthermore, since various load-withstanding additives can be optionally incorporated with a good compatibility, it is possible to impart a very high load-carrying capacity according to the intended use. As is apparent from the examples given hereinafter, the lubricating oil composition of the present invention can be used within a very broad temperature range of from -50°C to 250°C, and the oxidation stability and shear stability are very high and these characteristics are durable for a long time, with the result that the oil exchange period can be prolonged. The present invention will now be described in detail with reference to the following examples that by no means limit the scope of the invention. At first, the preparation of the liquid modified ethylene/α-olefin random copolymer will be described in the following referential examples. Referential Example 1 An ethylene/propylene copolymer having the following properties was used as the copolymer to be graft-modified. Ethylene content: 50 mole% Number average molecular weight ( Mn ): 810 Mw / Mn : 1.40 Intrinsic viscosity [η] : 0.04 dℓ/g Z value: 80 σ value: 0.1 Kinematic viscosity (100°C): 22.8 cst A 2-liter glass reaction vessel equipped with a nitrogen blow-in tube, a water-cooling condenser, a thermometer, two dropping funnels and a stirrer was charged with 800 g of the above-mentioned ethylene/propylene copolymer, and substitution of the inner atmosphere with nitrogen was carried out for 2 hours to expel dissolved oxygen. Then, the inner temperature of the reaction vessel was elevated to 160°C, and 40 g of maleic anhydride (liquefied by heating at 60°C) and 8 g of di-t-butyl peroxide charged in the two dropping funnels, respectively, were added dropwise over a period of 4 hours. After completion of the dropwise addition, reaction was further conducted for 4 hours, and the inner temperature of the reaction vessel was elevated to 180°C and unreacted maleic anhydride and a decomposition product of di-t-butyl peroxide were removed under a reduced pressure of 0.5 mmHg. The liquid modified ethylene/propylene copolymer having the following properties was obtained as the product. Appearance: yellow transparent liquid Intrinsic viscosity [η] : 0.04 dℓ/g Number average molecular weight ( Mn ): 815 Mw / Mn : 1.40 Kinematic viscosity (100°C): 33.8 cst Grafting ratio: 4.5 parts by weight per 100 parts by weight of ethylene/propylene copolymer Referential Example 2 A graft-modified liquid ethylene/propylene copolymer was prepared in the same manner as described in Referential Example 1 except that an ethylene/propylene copolymer having the following properties was used. Ethylene content: 50 mole% Number average molecular weight ( Mn ): 1450 Mw / Mn : 1.7 Intrinsic viscosity [η] : 0.05 dℓ/g Z value: 100 Kinematic viscosity (100°C): 110 cst σ value: 0.1 The properties of the obtained liquid modified ethylene/propylene copolymer were as follows. Appearance: yellow transparent liquid Intrinsic viscosity [η] : 0.08 dℓ/g Number average molecular weight ( Mn ): 1455 Mw / Mn : 1.7 Kinematic viscosity (100°C): 135 cst Grafting ratio: 4.4 parts by weight Referential Example 3 A liquid modified ethylene/propylene copolymer was prepared in the same manner as described in Referential Example 1 except that 80 g of maleic anhydride and 16 g of di-t-butyl peroxide were added dropwise over a period of 8 hours. Appearance: yellow transparent liquid Intrinsic viscosity [η]: 0.09 dℓ/g Number average molecular weight ( Mn ): 820 Mw / Mn : 1.5 Kinematic viscosity (100°C): 170 cst Grafting ratio: 9.6 parts by weight Referential Example 4 An ethylene/propylene copolymer having the following properties was used as the copolymer to be graft-modified. Ethylene content: 49 mole% Number average molecular weight ( Mn ): 1500 Mw / Mn : 1.65 Intrinsic viscosity [η] : 0.05 dℓ/g Z value: 110 Kinematic viscosity (100°C): 145 cst σ value: 0.1 A 1-liter glass reaction vessel was charged with 595 g of this ethylene/propylene copolymer, and the temperature was elevated to 140°C. Then, 105 g of n-butyl methacrylate and 9.0 g of di-t-butyl peroxide were added and heat reaction was conducted for 4 hours. The deaeration treatment was carried out under a reduced pressure of 10 mmHg while maintaining the temperature at 140°C to remove volatile components, and then, the reaction product was cooled to obtain a liquid modified ethylene/propylene copolymer. The properties of the obtained copolymer were as shown below. Appearance: colorless transparent liquid Intrinsic viscosity [η] : 0.06 dℓ/g Number average molecular weight ( Mn ): 1500 Mw / Mn : 1.63 Kinematic viscosity (100°C): 200 cst Grafting ratio: 16 parts by weight (n-butyl methacrylate) Referential Example 5 To 126 parts by weight of an isobutylene polymer having a number average molecular weight of 1260 was added 10 parts by weight of maleic anhydride, and reaction was carried out at 180°C for 5 hours with stirring. Unreacted maleic anhydride was removed by distillation under reduced pressure to obtain an acid-modified isobutylene copolymer. The number average molecular weight of this modified copolymer was 1360, and the grafting ratio of maleic anhydride was 7.8 parts by weight per 100 parts by weight of the isobutylene polymer. Examples 1 through 4 and Comparative Examples 1 through 5 Liquid modified ethylene/propylene copolymers obtained in Referential Examples 1, 3 and 4, starting ethylenen/propylene copolymers and extreme pressure agents were mixed at room temperature (25°C) as shown in Table 1, and the mixtures were heated at 100°C to obtain homogeneous compositions. Each of the so-obtained lubricating compositions was allowed to stand still at room temperature for 7 days and the transparency was evaluated with the naked eye according to the following scale: ○ : transparent ▵ : semi-transparent X : opaque or discreted For comparison, the above-mentioned test was conducted on liquid mixtures of the starting ethylene/propylene copolymers used in Referential Examples 1, 3 and 4 and extreme pressure agents. The obtained results are shown in Table 1. Example 5 In 60 parts by weight of the lequid modified copolymer prepared in Referential Example 2 was incorporated and dissolved 2 parts by weight of molybdenum dithiophosphate (SAKURA-LUBE® #300 supplied by Asahi Denka, Mo content = 9.0% by weight, P content = 3.2% by weight, S content = 10.5% by weight) at room temperature to obtain a brown transparent liquid mixture. The so-obtained liquid mixture was added to 100 parts by weight of the starting unmodified copolymer used in Referential Example 2, and the mixture was sufficiently stirred to obtain a green transparent stable liquid mixture. Comparative Examples 6 The procedures of Example 5 were repeated in the same manner except that the liquid modified copolymer was not used at all but the unmodified ethylene/propylene copolymer was mixed with molybdenum dithiophosphate. Both the components were not compatible with each other but they were separated from each other. Examples 6 through 8 and Comparative Examples 7 through 9 A commercially available extreme pressure additive (Package A, TC-7978 supplied by Texaco, S content = 2.7% by weight, Ca content = 4.1% by weight, Zn content = 1.0% by weight, P content = 1.0% by weight) was used as the extreme pressure agent. A liquid mixture was prepared by mixing 13 parts by weight of Package A, a predetermined amount of the liquid modified ethylene/propylene copolymer and 50 parts by weight of an ester oil (diisodecyl adipate) under heating at 100°C for 30 minutes. Then, 100 parts by weight of a liquid ethylene/propylene random copolymer having the following properties was added to the so-obtained liquid mixture, and the mixture was stirred at room temperature to obtain a lubricating oil composition. Ethylene content: 50 mole% Number average molecular weight ( Mn ): 1030 Mw / Mn : 1.5 Intrinsic viscosity [η] : 0.05 dℓ/g Kinematic viscosity (100°C): 40 cst Z value: 90 σ value: 0.1 With respect to each of the so-obtained compositions, the compatibility was evaluated in the same manner as described in Example 1. The obtained results are shown in Table 2. As is apparent from the results shown in Table 2, if the amount incorporated of the liquid modified ethylene/propylene copolymer is small, the mixture is opaque and precipitates are formed when the mixture is allowed to stand still, and the mixture is not suitable as a lubricating oil. Incidentally, in preparing the lubricating oil composition, it was important that the extreme pressure additive, Package A, should be mixed with the liquid modified ethylene/propylene random copolymer under heating in advance and then, the unmodified ethylene/propylene copolymer should be added. If both the copolymers were simultaneously added or heating was not conducted, it was difficult to obtain a transparent composition. Example 9 A liquid mixture was prepared by mixing 3 parts by weight of a commercially available extreme pressure additive (Package B, Anglamol 98A supplied by Nippon LUBRIZOL INDUSTRIES), 6 parts by weight of the liquid modified ethylene/propylene random copolymer prepared in Referential Example 2 and 13 parts by weight of an ester oil (diisodecyl adipate) under heating at 100°C for 30 minutes. The liquid mixture was mixed with 84 parts by weight of the starting unmodified ethylene/propylene copolymer used in Referential Example 2 and 16 parts by weight of a polydecene-1 oligomer (the kinematic viscosity was 12.5 cst as measured at 100°C), and the mixture was stirred at room temperature (25°C) to obtain a transparent and stable lubricating oil composition. Comparative Examples 10 A lubricating oil composition was prepared in Example 9 except that the liquid modified ethylene/propylene random copolymer was not incorporated. This lubricating oil composition was opaque, and when the composition was allowed to stand still, precipitates were formed. Example 10 A lubricating oil composition was prepared in the same manner as described in Example 6 except that a commercially available extreme pressure additive, Package C (LZ3928 supplied by Nippon Brisol, S content = 3.3% by weight, Ca content = 4.4% by weight, Zn content = 0.94% by weight, P content = 0.85% by weight, N content = 0.25% by weight) was used as the load-withstanding additive. The obtained lubricating oil composition was transparent and excellent in the compatibility. Comparative Example 11 A lubricating oil composition was prepared in the same manner as described in Example 10 except that the liquid modified ethylene/propylene copolymer was not used. The composition was opaque and when the composition was allowed to stand still, precipitates were formed. Example 11 A commercially available organic molybdenum extreme pressure additive (molybdenum dithiophosphate) (SAKURA-LUBE® #300 supplied by Asahi Denka, Mo content = 9.0% by weight, P content = 3.2% by weight, S = 10.5% by weight) was used as the load-withstanding additive. A liquid mixture was prepared by mixing 5 parts by weight of the above-mentioned extreme pressure additive and 10 parts by weight of the liquid modified ethylene/propylene copolymer prepared in Referential Example 2 under heating at 60°C for 15 minutes. The liquid mixture was mixed with 100 parts by weight of an unmodified ethylene/propylene copolymer having properties described below at room temperature with stirring to obtain a bluish green homogeneous transparent lubricating oil composition. Properties of Unmodified Ethylene/Propylene Copolymer Ethylene content: 50 mole% Number average molecular weight ( Mn ): 810 Mw / Mn : 1.40 Intrinsic viscosity [η]: 0.04 dℓ/g Kinematic viscosity (100°C): 20 cst This lubricating oil composition was excellent in the compatibility. Comparative Examples 12 A lubricating oil composition was prepared in the same manner as described in Example 11 except that the liquid graft-modified ethylene/propylene copolymer was not incorporated. The composition was opaque, and when the composition was allowed to stand still, precipitates were formed. Example 12 Lubricating characteristics of the lubricating oil prepared in Example 7 were tested. The obtained results are shown in Table 3. Comparative Example 13 A commercially available mineral oil type engine oil (for racing) comprising a refined petroleum lubricating oil as the base oil was tested in the same manner as in Example 12. The obtained results are shown in Table 3. For comparison, the lubricating oil composition prepared in Comparative Example 7 and a lubricating oil composition prepared in the same manner as described in Example 7 except that the modified isobutene polymer of Referential Example 5 was incorporated instead of the liquid modified ethylene/propylene copolymer of Referential Example 2 were similarly subjected to the test, but the test could not be performed because of the presence of precipitates. Incidentally, the shear stability was expressed by the reduction ratio of the kinematic viscosity at 100°C, observed when the sample was subjected to ultrasonic wave irradiation (10 kHz, 40°C, 30 minutes). Example 13 The procedures of Example 1 were repeated in the same manner except that 100 parts by weight of a poly-α-olefin oligomer (PAO-6, Synfluid CST6 supplied by Chevron Chemical Company, kinematic viscosity = 6 cst/100°C, viscosity index = 135) was used as the synthetic hydrocarbon oil instead of 100 parts by weight of the starting unmodified ethylene/propylene copolymer used in Example 1. The compatibility was evaluated as " ○" (transparent). Example 14 The procedures of Example 1 were repeated in the same manner except that 100 parts by weight of a poly-α-olefin oligomer (PAO-100, SHF-1001 supplied by Mobil Chemical, kinematic viscosity = 100 cst/100°C) was used as the synthetic hydrocarbon oil instead of 100 parts by weight of the starting unmodified ethylene/propylene copolymer used in Example 1. The compatibility was evaluated as " ○" (transparent).

Claims: A lubricating oil composition which comprises (A) 100 parts by weight of synthetic hydrocarbon lubricating oil selected from poly-α-olefin oils and ethylene/α-olefin random copolymer oils, (B) 0.1 to 20 parts by weight of an extreme pressure agent and (C) 0.8 to 200 parts by weight of a liquid graft-modified ethylene/α-olefin random copolymer comprising an ethylene/α-olefin random copolymer containing 30 to 75 mole % of ethylene graft-substituted by the residues of an unsaturated carboxylic acid or a derivative thereof, at a grafting ratio of 0.2 to 50 parts by weight of the unsaturated carboxylic acid or derivative thereof per 100 parts by weight of the ethylene/ α-olefin radom copolymer, the liquid graft-modified copolymer having an intrinsic viscosity [η], as measured in decalin at 135°C, in the range of from 0.01 to 0.3 dl/g and a molecular weight distribution ( M w/ M n), as determined by gel permeation chromatography, not larger than 4. A composition according to claim 1, wherein the extreme pressure agent (B) and the graft-modified copolymer (C) are incorporated at a (B)/(C) weight ratio of from 0.05 to 200. A composition according to claim 1 or claim 2 wherein the synthetic lubricating oil (A) is an ethylene/α-olefin random copolymer oil and the graft-modified copolymer (C) is a graft modification product of the ethylene/α-olefin random copolymer oil. A composition according to any one of claims 1 to 3 wherein the synthetic lubricating oil (A) is a random copolymer of ethylene and at least one α-olefin selected from propylene, 1-butene, 1-hexane, 4-methyl-1-pentene, 3-methyl-1-pentene, 1-octene, 1-decene, 1-dodecene, 1-tetradecene, 1-hexadecene, 1-octadecene and 1-eicosane. A composition according to any one of claims 1 to 4 wherein the graft-modified copolymer (C) is a copolymer of ethylene and at least one α-olefin selected from propylene, 1-butene, 1-hexene, 4-methyl-1-pentene, 3-methyl-1-pentene, 1-octene, 1-decene, 1-dodecene, 1-tetradecene, 1-hexadecene, 1-octadecene and 1-eicosane. A composition according to any one of claims 1 to 5 wherein the graft-modified copolymer (C) is graft-substituted by the residues of an unsaturated carboxylic acid or a derivative thereof selected from acrylic acid, methacrylic acid, maleic acid, fumaric acid, itaconic acid, citraconic acid, tetrahydrophthalic acid, bicyclo[2,2,1]hept-2-ene-5,6-dicarboxylic acid, maleic acid anhydride, itaconic acid anhydride, citraconic acid anhydride, tetrahydrophthalic acid anhydride, bicyclo[2,2,1]hept-2-ene-5,6-dicarboxylic acid anhydride, methyl acrylate, methyl methacrylate, dimethyl maleate, monomethyl maleate, diethyl fumarate, dimethyl itaconate, diethyl citraconate, dimethyl tetrahydrophthalate and dimethyl bicyclo[2,2,1]-hept-2-ene-5,6-dicarboxylate. A composition according to any one of claims 1 to 6 comprising at least one extreme pressure agent (B) selected from dibutyldithio carbamic acid sulphide, dibenzyl sulphide, dibutyl phosphate, diphenyl phosphate, oleyl chloride, chlorinated paraffin, zinc dithiophosphate, molybdenum dithiophosphate and lead naphthenate. A process for producing a composition according to any one of claims 1 to 7 which comprises admixing the lubricating oil (A), the extreme pressure agent (B) and the graft-modified copolymer (C). A process according to claim 8 comprising producing the graft-modified liquid ethylene/α-olefin random copolymer (C) by reacting an ethylene/α-olefin random copolymer having an ethylene content of from 30 to 75 mole % with an unsaturated carboxylic acid or derivative thereof as modifier and a graft-polymerisation initiator.

Inventors: KANESHIGE, RYOUSUKE, MIZUI, KINYA
Applicants: MITSUI PETROCHEMICAL INDUSTRIES, LTD.
Application year: 1988
Main classification: C10M169
IPC codes: C10M169, C10N20, C10M161, C10N30