MANNICH BASE OIL ADDITIVES

Abstract: Mannich bases are prepared using a phenol substituted with a medium length branched alkyl chain, which is derived from a 1-olefin oligomer. These Mannich bases act as friction-reducing agents when used in lubricant and liquid fuel compositions.

Description: MANNICH BASE OIL ADDITIVES This invention relates to novel additives made from medium-chain l-olefin oligomer alkylated phenols, aldehyde and hydrocarbyl amines, and to lubricant and liquid fuel compositions containing same. Much effort has been directed to providing a lubricant which will permit present-day automotive engines to be operated at a high level of efficiency over long periods of time. One difficulty encountered is that lubricating oils tend to deteriorate under the conditions of use, resulting in the formation of sludge, lacquer, and resinous materials, which adhere to the engine parts and lower the operating efficiency of the engine. Also, friction is a problem any time two surfaces are in sliding or rubbing contact. It is especially significant in an internal combustion engine and related power train components, because loss of substantial amount of the theoretical mileage possible from a given quantity of fuel is traceable directly to friction. The Mannich bases of this invention unexpectedly are effective in decreasing this friction. .Mannich bases have been used as lubricating oil and fuel additives. For instance, U.S. 3,368,972 teaches the use of a conventional Mannich base made using a phenol containing a high molecular weight alkyl substituent as detergents in engine oils. U.S. Patent 2,459,114 also discloses the use of conventional Mannich bases, but made using short-chain, alkyl-substituted hydroxy-aromatics or a relatively high molecular weight straight chain chlorinated aliphatic hydrocarbon. U.S. 3,649,229 teaches the same compounds as fuel additives. It has been found that the additives disclosed in the three mentioned references have no substantial friction-reducing properties. According to the present invention, a reaction product is made by reacting an aldehyde, at least one amine, and at least one alkyl-substituted phenol, wherein the alkyl is branched and is derived from a l-olefin oligomer having from 16 to 40 carbon atoms. Further, according to the present invention, a lubricant or fuel composition is provided which comprises a major portion of fuel or lubricant and antioxidant or friction reducing amount of a reaction product made by reacting an aldehyde, at least one amine, and at least one alkyl-substituted phenol, wherein the alkyl is branched and is derived from a l-olefin oligomer having from 16 to 40 carbon atoms. The reaction products according to this invention are made from (1) a medium molecular weight alkyl-substituted phenol, wherein the alkyl substituent is a branched oligomer made from a l-olefin and having no more than an average of 40 carbon atoms, (2) an aldehyde and (3) a hydrocarbyl amine wherein the respective molar ratio of reactants is 1.0:1.0-2.0:1.0-2.0. The reaction involved, in one of its aspects, can be represented by the following: EMI3.1 wherein R is a branched alkyl group having from about 16 to 40 carbon atoms derived from a 1-olefin having from 8 to 12 carbon atoms, R1 is hydrogen or R, R2 is a hydrogen or hydrocarbyl group, preferably alkyl, containing 6 to 18 carbon atoms, X is hydrogen or R2, R3 is hydrogen or a hydrocarbyl group containing 1 to 10 carbon atoms, preferably an alkyl group, R2 and R3 can also contain hydroxyl, halogen and the like, R4 is alkylene having 1 to 5 carbon atoms and n is from 1 to 10. The reaction can be run at from about 600C to about 130 C, using a hydrocarbon solvent. Such solvents can include benzene, xylene, and toluene. The water formed during the reaction is removed by azeotropic distillation while refluxing the mixture. The phenols contemplated for use in forming the alkylated phenols and making the products of this invention include phenol itself and cresol, xylenol, hydroxydiphenyl, amylphenol, benzylphenol, alpha and beta naphthols, and the like. Specific members include decene dimer phenol, decene trimer phenol, octene dimer and trimer phenol, dodecene dimer and trimer phenol and including mixtures of these. Aldehydes contemplated by the present invention are the aliphatic aldehydes, typified by formaldehyde or paraformaldehyde, acetaldehyde and aldol(f3-hydroxybutyraldehyde); aromatic aldehydes, such as benzaldehyde and heterocyclic aldehydes, such as furfural. The R3 group of the aldehyde may contain a substituent group such as hydroxyl, halogen, nitro and the like. In short, any substituent can be used which does not take a major part in the reaction. Preference, however, is given to the aliphatic aldehydes, formaldehyde being particularly preferred. The amines and the mixtures thereof contemplated herein are preferably those Which contain a primary amino group. It is contemplated that these preferred amines include saturated and unsaturated aliphatic primary monoamines containing 6 to 18 carbon atoms. More specifically, they include those shown in the above reaction scheme and disclosed hereinbelow, as well as such typical amines as: polyalkylenepolyamines, such as ethylenediamine and propylenediamine; poly-alkenepolyamines, such as those of the formula EMI5.1 wherein R4 is an alkylene group having from 1 to 5 carbon atoms and n is from 1 to 10. Examples of these are dimethylenetriamine, diethylenetriamine, triethylenetetramine, tetraethylenepentamine, hexaethyleneheptamine and the like. Cyclic amines are also contemplated and include cyclohexylamine and dicyclohexylamine. Still more specifically, the amines contemplated are cocoamine, oleylamine, octylamine, nonylamine, decylamine, cyclooctylamine, dodecylamine, tetradecylamine, hexadecylamine, octadecylamine, stearylamine, laurylamine, soyamine, dibutylamine, dioctylamine and other secondary amines, ethanolamine, diethanolamines and other alkanolamines. The alkyl phenols of this invention may be made by reacting 0.1 to 10 moles of a phenol with 1 mole of a l-olefin oligomer in the presence of an alkylation catalyst, such as a complex of BF3 (including the etherate, phenolate or phosphate complexes), BF3 or HC1 gas with AlC13, at 800C to 2500C. This process is particularly effective when conducted by reacting 1 to 1.5, or especially 1.25 moles, of phenol to 1 mole of an olefin oligomer in the presence of a BF3 phenolate at about 150 C. The product is conveniently dissolved in an aromatic solvent and then washed with water to remove unreacted components. Upon filtration and removal of the aromatic solvent by distillation, the product, a clear viscous oil, remains. The above-described reaction products are Mannich bases formed from the specified reactants and have been found to have not only generally applicable anti-friction qualities, but also the ability to reduce fuel consumption in an internal combustion engine. The Manich base additives can be used in a wide variety of systems at from about 0.1$ to about 10% by weight, but preferably about 0.10% to about 4.0%. Transmission fluids illustrate one system in which the present additives can be used. These are blends of highly refined petroleum base oils combined with VI improvers, detergents, defoamants and special additives to provide controlled-friction or lubricity characteristics. Varied transmission design concepts have led to the need for fluids with markedly different frictional characteristics, so that a single fluid cannot satisfy all requirements. The fluids intended for use in passenger car and light-duty truck automatic transmissions are defined in the ASTM Research Report D-2:RR 1005 on "Automatic Transmission Fluid/Power Transmission Fluid Property and Performance Definitions" Specifications for low temperature and aircraft fluids are defined in U. S. Government Specification MIL-H-5606A. In addition, the oxidation and corrosion resistance of functional fluids such as hydraulic fluids can be improved by the adducts of the present invention. Of particular significance, in accordance with the present invention, is the ability of the Mannich base additives to improve a variety of properties of lubricants and liquid fuels, hydrocarbon and alcoholic fuels and their mixtures. These Mannich base additives improve the wear resistance or friction qualities of lubricated parts and they improve resistance to oxidation and corrosion of oleaginous materials such as lubricating media. The liquid fuels improved in accordance with the present invention comprise those which are normally susceptible to forming undesirable carburetor and intake valve deposits in internal combustion engines. Specifically, liquid hydrocarbon fuels boiling from about 750F to about 750 F, including gasoline, jet fuel and dies fuel may be mentioned. Of particular significance is the treatment of petroleum distillate fuels having an initial boiling point of about 750F to about 1350F and an end boiling point from about 2500F to about 7500F. It should be noted, in this respect, that the term "distillate fuels" or "distillate fuel oils" is not intended to be restricted to straight-run distillate fractions. These distillate fuel oils can comprise straight run distillate fuel oils, catalytically or thermally cracked (including hydrocracked) distillate fuel oils or mixtures of straight run distillate fuel oils, naphthas and the like, with cracked distillate stocks. Moreover, such fuel oils can be treated in accordance with such well known commercial methods as acid or caustic treatment, hydrogenation, solvent refining, clay treatment and the like. The distillate fuels are characterized by their relatively low viscosity, pour point and the like. The principle property which characterizes these hydrocarbons, however, is their distillate range. As hereinbefore indicated, this range will lie between about 750F and about 7500 F. Obviously the distillation range of each individual fuel will cover a narrower boiling range, falling nevertheless, within the above-specified limits. Likewise, each fuel will boil substantially continuously throughout its distillation range. In addition to the hydrocarbon fuels mentioned, other fuels improved by the disclosed additives are alcohols such as methyl alcohol and ethyl alcohol, mixtures thereof and mixtures with the mentioned hydrocarbon fuels. Particularly contemplated among the fuels or fuel oils are Nos. 1, 2 and 3 fuel oils, used in heating and as diesel fuel oils, gasoline and jet combustion fuels. The domestic fuel oils generally conform to the specifications set forth in 4STTX specification D396-48T. Specifications for diesel fuels are defined in ASTM specification D975-48T. Typical jet fuels are defined in military specification MIL-F-624B. In addition, fuel oils of varying viscosity and pour points falling both within and outside the indicated ranges may also be effectively treated through the use of the additives of the present invention. The disclosed products may also be incorporated in lubricating media which may comprise liquid hydrocarbon oils in the form of either a mineral oil or a synthetic oil, or mixtures thereof, or in the form of a grease, in which any of the aforementioned oils are employed as a vehicle. These can also contain detergents and dispersants, as well as antioxidants, inhibitors, antiwear, extreme pressure, antifoam, pour depressant and viscosity index improving additives without negating the beneficial properties of the novel compositions of this invention. The compositions can include commonly used additives such as phenates, sulfonates, polymers, metal dithiophoisphates, succinimides, and the like. In general, mineral oils employed as the lubricant or grease vehicle may be of any suitable lubricating viscosity range as, for example, from about 45 SSU at 1000F to about 6,000 SSU at 1000F, and preferably from about 50 SSU at 2100F to about 250 SSU at 2100F. These oils may have viscosity indexes varying from below 0 to about 100 or higher. Viscosity indexes from about 70 to about 95 are preferred. The average molecular weights of these oils may range from about 250 to 800. Where the lubricant is to be employed in the form of a grease, the lubricating oil is generally employed in an amoung sufficient to balance the total grease composition, after accounting for the desired quantity of the thickening agent, and other additive components to be included in the grease formulation. In instances where synthetic oils and mixtures of synthetic oil and mineral oil are desired in preference to mineral oils only, various compounds of this type may be successfully utilized. Typical synthetic vehicles include polyisobutylene, polybutenes, hydrogenated polydecenes, polypropylene glycol, polyethylene glycol, trimethylol propane esters, neopentyl and pentaerythritol esters, di(2-ethylhexyl) sebacate, di(Z-ethylhexyl) adipate, di( -butylphthalate) fluorocarbons, silicat esters, silanes, esters of phosphorus-containing acids, liquid acids, liquid ureas, ferrocene derivatives, hydrogenated mineral oils, chain-type polyphenols, siloxanes and silicones (polysiloxanes), alkyl-substituted diophenyl ethers typified by a butyl-substituted bis(p-penoxyl phenyl) ether, phenoxy phenylethers, etc. There the lubricant is to be employed in the form of a grease, the lubricating oil is generally employed in an amount sufficient to balance the total grease composition, after accounting for the desired quantity of the thickening agent, and other additive components to be included in the grease formulation. A wide variety of materials may be employed as thickening or gelling agents. These may include any of the conventional metal salts or soaps, which are dispersed in the lubricating vehicle in greaseforming quantities in am amount to impart to the resulting grease composition the desired consistency. Other thickening agents that may be employed in the grease formulation may comprise the non-soap thickeners, such as surface-modified clays and silicas, aryl ureas, calcium complexes and similar materials. In general, grease thickeners may be employed which do not nelt and dissolve when used at the required temperature within a particular environment; however, in all other respects, any material which is normally employed for thickening or gelling hydrocarbon fluids for forming grease can be used in preparing the aforementioned improved grease in accordance with the present invention. Fuel compositions will contain from about 5 to about 500 pounds of additive per 1000 barrels of fuel, preferably about 20 to about 120 pounds per 1000 barrels. It is to be understood that the compositions contemplated herein can also contain other materials, For example, other corrosion inhibitors, extreme pressure agents, antiwear agents, defoamants, detergents, dispersants, and the like can be used, including phenates, sulfonates, zinc dithiophosphates and succinimides. These materials do not detract from the value of the compositions of this invention. Rather, the materials serve to impart their customary properties to the particular colnpositions in which they are incorporated. The following examples will illustrate the invention. They are illustrative only, and are not intended to limit the invention. EXAMPLE 1 Decene Trimer Alkylated Phenol Cocoamine-Formaldehyde Condensation Reaction Product Approximately 42g (about 0.2 moles) of cocoamine, 72g of l-decene trimer alkylated phenol, 6.5g (about 0.2 moles) of paraformaldehdye and lOOg of benzene solvent were placed in a 500 ml glass reactor fitted with a nitrogen inlet, stirrer, thermometer, Dean-Stark tube and condenser. The reaction mixture was heated with agitation using a nitrogen blanket to a maximum temperature of about 1150C until water evolution stopped. The solvent was removed by vacuum distillation. The reaction product was filtered through diatomaceous earth at about 700C and was collected as a clear, amber colored liquid. EXAMPLE 2 Decene Dimer Alkylated Phenol Cocoamine-Formaldehyde Condensation Reaction Product Approximately 45g (about 0.2 moles) of cocoamine, 100g of l-decene dimer alkylated phenol, 6.5g (about 0.2 moles) of paraformaldehyde and 75g of benzene solvent were placed in a reactor equipped as described in Example 1. The reaction mixture was heated with agitation and a nitrogen blanket to a maximum temperature of 1200C over a period of 3 hours until water evolution stopped. The solvent was removed by vacuum distillation. The reaction product was filtered through diatomaceous earth at about 700C and was collected as a clear, amber colored liquid. EXAMPLE 3 One mole of polybutylphenol (made by reacting phenol with polyisobutylene in the presence of BF3 catalyst), 0.58 mole of tetraethylenepentamine and 1.95 moles of paraformaldehyde were reacted as described in Examples 1 and 2, except that the reaction product was diluted 50:50 with a process oil. EXAMPLE 4 Decene Trimer Alkylated Phenol Triethylenetetraamine-Formaldehyde Condensation Reaction Product Approximately 82.6 grams of triethylene tetraamine, 1030 grams of l-decene trimer alkylated phenol and 37.2 grams of paraformaldehyde were loaded into a reaction vessel fitted with a nitrogen inlet strirrer, thermometer, Dean-Stark tube and condenser. The reaction mixture was heated to a temperature of about 1000C for about one hour. The temperature was then raised to 1500C for a period of one hour while water was evolved. Reduced pressure of 100 mm for 0.5 hours at 1500C was then applied. A total of 25 grams of water was collected. The reaction product was then filtered through dialomaceous earth and was collected as a clear amber fluid. EVALUATION OF THE REACTION PRODUCTS The reaction products of Examples 1, 2 and 3 were evaluated in a low velocity friction apparatus (LVFA) in a fully formulated 5W-20 synthetic engine oil containing an additive package including antioxidant, dispersant and detergent. The reaction product test compound was 4t of the total weight of oil. The low velocity friction apparatus (LVFA) is used to measure the coefficient of friction of test lubricants under various loads, temperatures, and sliding speeds. The LVFA consists of a flat SAE 1020 steel surface (diam. 1.5 in.) which is attached to a drive shaft and rotated over a stationary, raised, narrow ringed SAE 1020 steel surface (area 0.08 in.2). Both surfaces are submerged in the test lubricant. Friction between the steel surfaces is measured as a function of the sliding speed at a lubricant temperature of 2500F. The friction between the rubbing surfaces is measured using a torque arm-strain gauge system. The strain gauge output, which is calibrated to be equal to the coefficient of friction, is fed to the Y axis of an X-Y plotter. The speed signal from the tachometer-generator is fed to the X-axis. To minimize external friction, the piston is supported by an air bearing. The normal force loading the rubbing surfaces is regulated by air pressure on the bottom of the piston. The drive system consists of an infinitely variable-speed hydraulic transmission driven by a 1/2 HP electric motor. To vary the sliding speed, the output speed of the transmission is regulated by a lever-cam-motor arrangement. The rubbing surfaces and 12-13 ml of test lubricant are placed on the LVFA. A 240 psi load is applied, and the sliding speed is maintained at 40 fpm at ambient temperature for a few minutes. Plots of coefficients of friction (Uk vs. speed were taken at 240, 300, 400, and 500 psi. Freshly polished steel specimens are used for each run. The surface of the steel is parallel ground to 4 to 8 microinches. The results in Table 1 refer to percent reduction in coefficient of friction compared to the unmodified oil. That is, the formulation mentioned above was tested without the compound of this invention and this became the basis for comparison. The following results were obtained at 2500F and 500 psi: TABLE 1 Friction Reduction Properties Low Velocity Friction Apparatus Test Medium Additive Percent Reduction in and Conc. Coefficient of Friction, % Additive Wt. % S Ft./Min. 30 Ft./Min. Base Oil only 0 0 0 Example 1 4 20 25 Example 2 4 18 23 Example 3 4* 0 0 *8 of 50% active product The results clearly show substantial friction-reducing properties for the l-olefin oligomer derived alkylated phenol Mannich base condensation product. Example 3, which represents products like those disclosed in U.S. 3,368,972, has no friction reducing properties as measured in this test. The products of Examples 1 and 2 were blended into a 200" solvent paraffinic neutral lubricating oil samples of which were evaluated for oxidative stability using the Catalytic Oxidation Test by placing them in an oven at 3250F for 40 hours. The samples were in the presence of the following metals known to catalyze organic oxidation: a. 15.6 sq. in. of sand blasted iron wire; b. 0.78 sq. in. of polished copper wire; c. 0.87 sq. in. of polished aluminum wire; d. 0.167 sq. in. of polished lead surface. Dry air was passed through the test samples at a rate of about S liters per hour for the full 40 hours. The results demonstrate the antioxidant properties incorporated into these friction-reducing compositions. TABLE 2 Oxidation Characteristics Catalytic Oxidation Test, 40 Hours &commat;32SOF t Increase in Medium Additive Viscosity of and Conc. Oxidized Oil Neutralization Additive Wt. % Using KV &commat; 100 C Number Base Oil only 0 67 3.62 Example 1 1 33 - Example 2 1 25 3.20 The results clearly show substantial antioxidant properties for the l-olefin oligomer derived alkylated phenol Mannich base condensation product. The reaction product of Example 4 was then evaluated in an IFP Renault R-5 Carburetor Detergeny Test using a base fuel consisting of a commercially available regular leaded gasoline containing approximately 0.45 grams Pb/liter. The test procedure employed was similar to that disclosed in Coordinating Research Council (CRC) Report No. 529, published in April 1983. The engine employed is a Renault 810-26 (R5 GTL) with some modification to the piston ring pack, manifold, air cleaner and oil circulation system. It is fitted with a Solex 32 SEIA single body carburetor. The engine was run for a total of 12 hours under cyclic RPM conditions. Basically, the engine was allowed to idle at 800 RPM for 2 minutes followed by 8 minutes at 1800 RPM under a load of 5.85 hp. Engine speed was then allowed to drop back down to idle and the start of another operational cycle. Upon the completion of 12 hours, the carburetor and intake system were inspected for deposits. The test results are set forth below. Carburetor Cleanliness Rating Base Fuel + Rating Method Base Fuel 308 ppm of Ex. 4 Difference BNPE (1) 0.7 6.4 + 5.7 CRC (2) -above throttle plate 3.5 7.7 + 4.2 -below throttle plate 1.8 6.6 + 4.8 throttle plate 3.5 6.9 + 3.4 (1) Standard Institut Francais de Petrol (IFP) method where 10 = clean, 0 = black (2) Coordinating Research Council (CRC) method where 10 = clean, 1 = black.

Claims: CLAIMS: 1. A reaction product made by reacting an aldehyde, at least one amine and at least one alkyl-substituted phenol, wherein the alkyl is branched and is derived from a l-olefin oligomer having from 16 to 40 carbon atoms. 2. The product of Claim 1 wherein the l-olefin oligomer is derived from a l-olefin having 8 to 12 carbon atoms. 3. The products of Claims 1 or 2 wherein the phenol has the formula EMI15.1 wherein R is a branched alkyl group derived from a l-olefin oligomer having 16 to 40 carbon atoms and R1 is hydrogen or R. 4. The product of Claims 2 or 3 wherein the phenol is phenol itself, cresol, xylenol, hydroxydiphenyl, amylphenol, benzylphenol, alpha naphthol or beta naphthol. 5. The product of any one of Claims 1 to 4 wherein the aldehyde has the formula R3CHO wherein R3 is hydrogen or a hydrocarbyl group containing 1 to 10 carbon atoms or the substituted member thereof. 6. The product of any one of Claims 1 to 5 wherein the aldehyde is an aromatic, aliphatic or heterocyclic aldehyde. 7. The product of Claim 6 wherein the aldehyde is formaldehyde, paraformaldehyde, acetaldehyde, Shydroxybutyraldehyde, benzaldehyde or furfural. 8. The product of Claim 7 wherein the aldehyde is paraformaldehyde. 9. The product of any one of Claims 1 to 8 wherein the amine has the formula EMI16.1 wherein R2 is hydrogen or a hydrocarbyl group or a hydroxyhydrocarbyl group containing 6 to 18 carbon atoms, X is hydrogen or R2, R4 is an alkylene group having 1 to 5 carbon atoms and n is 1 to 10. 10. The product of Claim 9 wherein the amine is cocoamine, oleylamine, octylamine, nonylamine, decylamine, cyclooctylamine, dodecylamine, tetradecylamine, hexadecylamine, octadecylamine, stearylamine, laurylamine, soyamine, dibutylamine, dioctylamine, ethanolamine, diethanolamine, dimethylenetriamine, diethylenetriamine, triethylenetetramine, tetraethylenepentamine, hexaethyleneheptamine, ethylenediamine, propylenediamine, cyclohexylamine or dicyclohexylamine. 11. The product of Claim 1 wherein the alkylated phenol is l-decene trimer alkylated phenol, the aldehyde is paraformaldehyde and the amine is cocoamine. 12. The product of Claim 1 wherein the alkylated phenol is l-decene dimer alkylated phenol, the aldehyde is paraformaldehyde and the amine is cocoamine. 13. A lubricant or liquid fuel composition comprising a major proportion of fuel or lubricant and an antioxidant or friction reducing amount of a reaction product made by reacting an aldehyde, at least one amine and at least one alkyl-substituted phenol, wherein the alkyl is branched and is derived from a l-olefin oligomer having from 16 to 40 carbon atoms. 14. The composition of Claim 13 wherein the l-olefin oligomer is derived from a l-olefin having 8 to 12 carbon atoms. 15. The composition of Claims 13 or 14 wherein the phenol has the formula EMI17.1 wherein R is a branched alkyl group derived from a l-olefin oligomer having 16 to 40 carbon atoms and R1 is hydrogen or R. 16. The composition of any one of Claims 13 to 15 wherein the phenol is phenol itself, cresol, xylenol, hydroxydiphenyl, amylphenol, benzylphenol, alpha naphthol or beta naphthol. 17. The composition of any one of Claims 13 to 16 wherein the aldehyde has the formula R3CHO wherein R3 is hydrogen or a hydrocarbyl group containing 1 to 10 carbon atoms or the substituted member thereof. 18. The composition of any one of Claims 13 to 17 wherein the aldehyde is an aromatic, aliphatic or heterocyclic aldehyde. 19. The composition of Claim 18 wherein the aldehyde is formaldehyde, paraformaldehyde, acetaldehyde, aldolhydroxybutyraldehyde, benzaldehyde or furfural. 20. The composition of Claim 19 wherein the aldehyde is paraformaldehyde. 21. The composition of any one of Claims 13 to 20 wherein the amine has the formula EMI18.1 wherein R2 is hydrogen or a hydrocarbyl group or a hydroxyhydrocarbyl group containing 6 to 18 carbon atoms, X is hydrogen or R2, R4 is an alkylene group having 1 to 5 carbon atoms and n is 1 to 10. 22. The composition of Claim 21 wherein the amine is cocoamine, oleylamine, octylamine, nonylamine, decylamine, cyclooctylamine, dodecylamine, tetradecylamine, hexadecylamine, octadecylamine, stearylamine, laurylamine, soyamine, dibutylamine, dioctylamine, ethanolamine, diethanolamine, dimethylenetriamine, diethylenetriamine, triethylenetetramine, tetraethylenepentamine, hexaethyleneheptamine, ethylenediamine, propylenediamine, cyclohexylamine or dicyclohexylamine. 23. The composition of Claim 13 wherein the alkylated phenol is l-decene trimer alkylated phenol, the aldehyde is paraformaldehyde and the amine is cocoamine. 24. The composition of Claim 13 wherein the alkylated phenol is l-decene dimer alkylated phenol, the aldehyde is paraformaldehyde and the amine is cocoamine. 25. The composition of any one of Claims 13 to 24 wherein the lubricant is a mineral lubricating oil, a synthetic lubricating oil, mixtures thereof or a grease prepared from any of these. 26. The composition of any one of Claims 13 to 24 wherein the fuel composition comprises an automotive internal combustion engine fuel composition. CLAIMS FOR AUSTRIA: 1. A process of making an oxidation or friction reducing agent comprising reacting (a) at least one alkyl-substituted phenol wherein the alkyl is branched and is derived from a l-olefin oligomer having from 16 to 40 carbon atoms; (b) an aldehyde; and (c) at least one amine. 2. A process of making a lubricant or liquid fuel composition comprising mixing a major proportion of a fuel or lubricant with an antioxidant or friction reducing amount of the reaction product of claim 1. 3. The process of claim 1 or 2 wherein the molar ratio of (a):(b):(c) is 1.0:1.0-2.0:1.0-2.0. 4. The process of any one of the preceeding claims wherein the reaction among (a), (b) and (c) is conducted at a temperature of 600 to l300C. 5. The process of any one of the preceeding claims wherein the l-olefin oligomer is derived from a l-olefin having 8-12 carbon atoms. 6. The process of any one of the preceeding claims wherein the phenol has the formula EMI20.1 cIAlms FOR AUSTRIA: wherein R is a branched alkyl group derived from a l-olefin oligomer having 16 to 40 carbon atoms and R1 is hydrogen or R. 7. The process of any one of the preceeding claims wherein the phenol is phenol itself, cresol, xylenol, hydroxydiphenyl, amylphenol, benzylphenol, alpha naphthol or beta naphthol. 8. The process of any one of the preceeding claims wherein the aldehyde has the formula R3CHO wherein R3 is hydrogen or a hydrocarbyl group containing 1 to 10 carbon atoms or the substituted member thereof. 9. The process of any one of the preceeding claims wherein the aldehyde is an aromatic, aliphatic or heterocyclic aldehyde. 10. The process of any one of the preceeding claims wherein the aldehyde is formaldehyde, paraformaldehyde, acetaldehyde, aldolhydroxybutyraldehyde, benzaldehyde or furfural. 11. The process of any one of the preceeding claims wherein the amine has the formula EMI21.1 wherein R2 is hydrogen or a hydrocarbyl group or a hydroxyhydrocarbyl group containing 6 to 18 carbon atoms, X is hydrogen or R2, R4 is an alkylene group having 1 to 5 carbon atoms and n is 1 to 10. CLAIMS FOR AUSTRIA: 12. The process of any one of the preceeding claims wherein the amine is cocoamine, oleylamine, octylamine, nonylamine, decylamine, cyclooctylamine, dodecylamine, tetradecylamine, hexadecylamine, octadecylamine, stearylamine, laurylamine, soyamine, dibutylamine, dioctylamine, ethanolamine, diethanolamine, dimethylenetriamine, diethylenetriamine, triethylenetetramine, tetraethylenepentamine, hexaethyleneheptamine, ethylenediamine, propylenediamine, cyclohexylamine or dicyclohexylamine. 13. The process of any one of the preceeding claims wherein the alkylated phenol is l-decene trimer alkylated phenol, the aldehyde is paraformaldehyde and the amine is cocoamine. 14. The process of any one of the preceeding claims wherein the alkylated phenol is l-decene dimer alkylated phenol, the aldehyde is paraformaldehyde and the amine is cocoamine. 15. The process of any one of claims 2 to 14 wherein the lubricant is a mineral lubricating oil, a synthetic lubricating oil, mixtures thereof or a grease prepared from any of these. 16. The process of any one of claims 2 to 14 wherein the fuel composition comprises an automotive internal combustion engine fuel composition.

Inventors: GEMMILL, ROBERT MACDONALD, JR., HORODYSKY, ANDREW GENE
Applicants: MOBIL OIL CORPORATION
Application year: 1984
Main classification: C07C215
IPC codes: C08G14, C10L1, C10M159