Sulphur coupled hydrocarbyl derived mercaptobenzothiazole adducts as multifunctional antiwear additives and compositions containing same

Abstract: Sulfur-coupled hydrocarbyl-derived mercaptobenzothiazole adducts have been found to be effective multifunctional antiwear additives for fuels and lubricants. The adducts are prepared by reacting a long-chain olefin with a sulfur source and thereafter coupling the reaction product with a mercaptobenzothiazole.

Description: Background of the Invention Lubricants, such as lubricating oils and greases, are subject to oxidative deterioration at elevated temperatures or upon prolonged exposure to the elements. Such deterioration is evidenced, in many instances, by an increase in acidity and in viscosity, and when the deterioration is severe enough, it can cause metal parts to corrode. Additionally, severe oxidation leads to a loss of lubrication properties, and in especially severe cases this may cause complete breakdown of the device being lubricated. Antioxidants or oxidation inhibitors are used to minimize the effects of oil deterioration that occur when hot oil is contacted with air. The degree and rate of oxidation will depend on temperature, air and oil flow rates and, of particular importance, on the presence of metals that may catalytically promote oxidation. Water (moisture) is another critical problem. In spite of even extraordinary precautionary efforts, water is found as a film or in minute droplets in vessels containing various hydrocarbon distillates. This brings about ideal conditions for corrosion and damage of metal surfaces of the vessels and the materials contained therein. Also, in the lubrication of internal combustion engines, quantities of water are often present as a separate phase within the lubricating system. Another serious problem with respect to metallic surfaces that are in contact with adjacent metallic surfaces is the surface wear caused by the contact of such surfaces. A material capable of simultaneously and effectively coping with problems such as these is highly desirable. The use of sulfur-containing compositions such as sulfurized isobutylenes has been well known for their antiwear properties in a varied of lubricant applications as exemplified by U.S. Patents 3,703,504; 3,703,505, and 3,873,454. EPA 0 319 405 discloses the preparation of sulfurized polyolefin compositions obtained by (1) reacting sulfur mono-α-dichloride with a C₆ to C₁₂ aliphatic monoolefin to form a reaction product and (2) reacting the obtained reaction product with a mercaptate or polysulfide mercaptate of the general formula R³S x M in which R³ represents an aliphatic group; an aliphatic group bearing a functional group; an aromatic group; an alkanomatic group or a heterocyclic group. M represents a monovalent atom or group derived from the base MOH; and x takes a value of at least 1. It has now been found that sulfur-coupled hydrocarbyl-derived mercaptobenzothiazole adducts provide exceptional multifunctional antiwear, antioxidant and friction reducing properties. These remarkable benefits are to be expected for a varied of synthetic and mineral oil based lubricants and liquid hydrocarbon fuels. Summary of the Invention This invention is directed to sulfur-coupled, hydrocarbyl-derived mercaptobenzothiazole adducts made by reaction of (a) a C₆-C₆₀ long-chain terminal olefin such as 1-octadecene or 1-decene with (b) a sulfur source such as sulfur monochloride or sulfur dichloride followed by coupling with (c) a mercaptobenzothiazole. These adducts have been found to exhibit excellent multifunctional antiwear, antioxidant and copper corrosivity performance characteristics when blended in additive concentrations of 0.0001% to 10% by weight into fuels or lubricants. This invention is, therefore, also directed to lubricant and fuel compositions containing the aforementioned additive concentrations of the embodied novel sulfur-containing adducts. Although the inventors do not wish to be bound by any particular theory, the hydrocarbyl groups, sulfur moieties and heterocyclic rings are each believed to provide the basis for synergistic antiwear, antioxidant, copper passivating and friction reducing properties. The hydrocarbyl group is believed to provide the lubricity/friction reducing and/or detergency properties. The sulfur-coupling groups provide additional antiwear and antioxidant characteristics. The benzothiazole group may additionally contribute antioxidant, lubricity and high-temperature stabilizing properties to this new class of additives. All of these beneficial properties are believed to be enhanced as a result of this novel internal synergism. This unique internal synergism concept is believed to be applicable to similar structures containing (a) hydrocarbyl groups, (b) sulfur-coupling groups and (c) benzothiazole linkages within the same molecule. Description of Specific Embodiments Generally speaking, long-chain olefins may be reacted with a sulfur halide such as sulfur monochloride followed by a coupling reaction with, for example, 2-mercaptobenzothiazole, optionally in the presence of a phase transfer catalyst and organic or inorganic bases, such as sodium or potassium hydroxide, in a one pot, two step, coupling reaction sequence (addition step followed by substitution step) to form a mixture of reaction products. We believe that the following type of product prepared as disclosed below is included in the mixture, along with related isomers and other possible reaction products: where each R is C₄-C₅₈ hydrocarbyl, preferably C₄-C₄₀ hydrocarbyl and more preferably the R group contains 10 or more carbon atoms, B is halogen, preferably chlorine, x is an integer from 1 to 8 and y is an integer from 1 to 2. R₂ is hydrogen or C₁-C₄₀ hydrocarbyl. R or R₂ can optionally contain sulfur, nitrogen and/or oxygen. An excess of one reagent to another can be used. Mixtures can be used. Molar quantities, less than molar quantities, or more than molar quantities of any of the ingredients can be effectively used. Suitable long chain hydrocarbyl terminal olefins include but are not limited to C₆ to about C₆₀ and preferably C₈ to about C₃₂ olefins such as octene, decene and octadecene or mixtures thereof. Preferred are 1-decene and octadecene-1. Linear and branched olefins are suitable. Optionally the olefins may be substituted with nitrogen, sulfur, and/or oxygen. Suitable mercaptobenzothiazoles include but are not limited to 2-mercaptobenzothiazole, 2-mercapto-6-methylbenzothiazole, 2-mercapto-5-nitrobenzothiazole and derivatives or mixtures thereof. Suitable phase transfer/catalytic agents include but are not limited to quaternary ammonium salts such as benzyltriethylammonium chlorides, cyclic polyethers, poly (ethylene oxides), polyether-amines where the amine is a tertiary-amine or mixtures thereof and the like. However, as previously noted, the use of a phase transfer catalyst is optional. Preferred are trihydrocarbyl ammonium chlorides such as tricaprylyl methylammonium chloride. Solvents can also be used to improve reaction rates. Generally, they are non-reactive hydrocarbon solvents such as toluene or a xylene. Any suitable inorganic or organic base may be used herein. Preferred are sodium hydroxide, potassium hydroxide and organic bases such as ammonium hydroxide or triethylamine. Generally speaking, the various reaction times, temperatures, pressures and quantities of reactive materials may vary widely and are not believed to be critical. Generally, the temperature may vary from about 30° to about 250°C with 70° to 150°C being preferable; the pressure may vary from ambient or autogenous or slightly higher. Reduced pressure can also be used if desired. The molar ratio of reactants may vary from about 1:10 to about 10:1 of sulfurized olefin to mercaptobenzothiazole. Preferred is a molar ratio of 1:2 to about 2:1. The time of reaction will vary depending upon the specific reactants and, if a solvent or catalyst is used, from about 0.5 hour up to about 24 hours or more may be suitable. The additives may be incorporated into any suitable lubricating media which comprise oils of lubricating viscosity, e.g., mineral or synthetic oils; or mixtures of mineral and synthetic oils or greases in which the aforementioned oils are employed as a vehicle or into such functional fluids as hydraulic fluids, brake fluids, power transmission fluids and the like. In general, mineral oils and/or synthetic oils, employed as the lubricant oil, or grease vehicles may be of any suitable lubricating viscosity range, as for example from about 45 SSU (6 cSt) at 37.8°C. (100°F.) to about 6000 SSU (2000 cSt) at 37.8°C. (100°F.), and, preferably, from about 50 to about 250 SSU (7.5 to 55 cSt) at 98.9°C. (210°F.). These oils may have viscosity indices from below zero to about 100 or higher. Viscosity indices from about 70 to about 95 are preferred. The average molecular weight of these oils may range from about 250 to about 800. Where 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. When high temperature stability is not a requirement of the finished grease, mineral oils having a viscosity of at least 40 SSU (4 cSt) at 65.5°C. (150°F.) and particularly those falling within the range from about 60 SSU to about 6,000 SSU (10 to 2000 cSt) at 37.8°C. (100°F.) may be employed. The lubricating vehicles of the improved greases of the present invention, containing the above described additives, are combined with a grease forming quantity of a thickening agent. For this purpose, a wide variety of materials may be dispersed in the lubricating vehicle in grease-forming quantities in such degree as to impart the desired consistency to the resulting grease composition. Exemplary of the thickening agents that may be employed in the grease formulation are 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 melt and dissolve when used at the required temperature within a particular environment; soap thickeners such as metallic (lithium or calcium) soaps including hydroxy stearate and/or stearate soaps can be used. However, in all other respects, any material which is normally employed for thickening or gelling hydrocarbon fluids or forming greases can be used in preparing the aforementioned improved greases in accordance with the present invention. In instances where synthetic oils are desired in preference to mineral oils, or in combination therewith, various compounds of this type may be successfully utilized as the vehicle for the grease. Typical synthetic vehicles include polyisobutylene, polybutenes, hydrogenated polydecenes, polypropylene glycol, polyethylene glycol, trimethylolpropane esters, neopentyl and pentaerythritol esters, di(2-ethylhexyl) sebacate, di(2-ethylhexyl) adipate, dibutyl phthalate, fluorocarbons, silicate esters, silanes, esters of phosphorous-containing acids, liquid ureas, ferrocene derivatives, hydrogenated mineral oils, chain-type polyphenyls, siloxanes and silicones (polysiloxanes), alkyl-substituted diphenyl ethers typified by a butyl-substituted bis(p-phenoxyphenyl) ether, phenoxy phenylethers, etc. As has been disclosed hereinabove, the reaction products are useful as multifunctional antiwear/antioxidant/antirust agents in lubricants and fuels. They are added to the lubricating medium or fuel in amounts sufficient to impart such properties thereto. More particularly, such properties will be imparted to lubricants by adding from about 0.001% to about 10% by weight, preferably from about 0.01% to about 3% by weight, of the neat product, and to fuels by adding from about 2.3 kg (5 pounds) to 567 kg (1250 pounds) per thousand barrels (158970 liters) of fuel, preferably from about 22.7 kg (50 pounds) to 68 kg (150 pounds) per 1000 barrels (158970 liters). Suitable fuels include but are not limited to liquid hydrocarbon fuels such as gasolines, alcohol and mixtures thereof such as gasohol, distillate fuel oils, diesel fuel and heating fuel oil, and the like. The products of the invention show good stability and compatibility when used in the presence of other commonly used lubricants or fuel additives. Therefore, fully formulated lubricating oils may include a variety of additives (for their known purpose) such as dispersants, detergents, inhibitors, antiwear agents, antioxidants, antifoam agents, antirust agents, demulsifiers, pour depressants and other additives including phenates, sulfonates and zinc dithiophosphates, polymers, polyisobutylsuccinimides, arylamines, hindered phenols, esters, amides, etc. The following examples are exemplary only and are not intended as being limitative of the present invention. Example 1 Octadecene-1/Sulfur Monochloride Adduct Approximately 840 gm (3.0 mol. 90% purity) of octadecene was charged into a 2-liter reactor equipped with dropping funnel, reflux condenser, thermometer, and mechanical stirrer. Approximately 202.5 gm (1.5 mol.) of sulfur monochloride was added through the dropping funnel. Then the reaction mixture was heated to 95° to 100°C to activate the sulfochlorination reaction. A moderate exotherm brought the temperature to 113°C, and then the reaction was held at 110°C for four hours. Near the end of the period at 110°C, the color became dark reddish. At completion, the product was left to cool slowly. This produced 1030.6 gm of liquid material (C₃₆H₇₂S₂Cl₂). Example 2 Octadecene-1/Sulfur Monochloride/2-Mercaptobenzothiazole Adduct 278.4 gm of the product of Example 1 (0.4 mol.), 133.8 gm of 2-mercaptobenzothiazole (0.8 mol.), 8 gm of Aliquat 336 (phase transfer catalyst obtained from Aldrich Chemical Company: tricaprylylmethyl ammonium chloride), 200 ml caustic solution (32 gm sodium hydroxide dissolved in 200 ml water), and 400 ml toluene were mixed in a 2-liter reactor. The reactants were stirred under reflux for six hours, and then cooled to ambient temperature. The aqueous phase was separated, and the organic phase was twice washed with 400 ml of water. Thereafter, toluene was removed by vacuum distillation leaving a dark fluid as the desired product (373 gm). It was further purified by hot filtration through Super-Cel. Nitrogen analysis: 2.4% Sulfur analysis: 19.2% Example 3 (In the Absence of Phase Transfer Catalyst) 33.4 gm of 2-mercaptobenzothiazole (0.2 mol.) was suspended in 150 ml toluene and caustic solution (8 gm sodium hydroxide dissolved in 20 ml water). Approximately 69.6 gm of the product of Example 1 (0.2 mol.), and 20 ml of dimethylformamide (DMF) were added. The reactants were stirred under reflux for three to four hours and a small amount of solid gradually precipitated from the dark brown mixture. Then, the cooled mixture was washed with 100 ml portions of water three times. The organic phase was evaporated at reduced pressure and elevated temperature ( 130°C) to remove volatile materials to afford the final product as a dark brownish oil (70.2 gm). Nitrogen analysis: 2.09% Sulfur analysis: 17.2% Example 4 The procedure of Example 3 was followed with only one exception: dimethylsulfoxide (DMSO) (20 ml) was used instead of dimethylformamide (DMF) (20 ml). Example 5 The procedure of Example 2 was followed on a small scale, i.e., the same ratios of materials were used but the quantities of each were about two thirds (2/3) less. Nitrogen analysis: 2.56% Sulfur analysis 19.2% Example 6 Decene-1/Sulfur Dichloride/2-Mercaptobenzothiazole Adduct The procedure of Examples 1 and 2 were followed with the following exceptions: Decene-1 and sulfur dichloride were used instead of octadecene-1 and sulfur monochloride. Sulfur analysis: 25.4% Evaluation of Product The products of selected examples were evaluated in the Catalytic Oxidation Test to determine antioxidant activity when blended at additive concentrations in the lubricants as shown in Table I. CATALYTIC OXIDATION TEST The test lubricant composition is subjected to a stream of air which is bubbled through the composition at a rate of 5 liters per hour at the specified temperature for the required number of hours. Present in the composition (comprising a 200 second solvent refined paraffinic neutral oil) in addition to the additive compound were metals commonly used as materials to construct engines namely: (a) 15.6 square inch (101 cm²) of sand-blasted iron wire; (b) 0.78 square inch (5.03 cm²) of polished copper wire; (c) 0.87 square inch (5.61 cm²) of polished aluminum wire; and (d) 0.107 square inch (0.69 cm²) of polished lead surface. The test results are reported below in Table I. As confirmed by the good control of (a) increase in viscosity, (b) increase in acid number and (c) lead loss, these sulfur-coupled hydrocarbyl-derived mercaptobenzothiazole adducts demonstrate remarkable antioxidant properties. The products of the examples were also blended into mineral oil and evaluated for antiwear activity using the Four-Ball Wear Test as shown in Table II. The Four-Ball Wear Test (ASTM D2266) In this test, three stationary balls are placed in a lubricant cup and a lubricant containing the additive to be tested is added thereto. A fourth ball is placed on a chuck mounted on a device which can be used to spin the ball at known speeds and loads. Various percentages by weight of each product were placed in the blend. The samples were tested at 200°C and 300°C at a load of 6 kilograms and 2000 rpm for 30 minutes. Four-Ball Wear Test (2,000 rpm, 60 kg load, 30 Minutes) Wear Scar Diameter, mm at 300°F (148.9°C.) at 200°F (93.3°C.) Base Oil (80% Solvent Paraffinic Bright, 20% Solvent Paraffinic Neutral Lubricating Oils.) 4.11 3.20 1% of Example 2 in above Base Oil 0.84 1% of Example 3 in above Base Oil 1.69 0.79 1% of Example 4 in above Base Oil 1.60 1.55 1% of Example 5 in above Base Oil 1.70 0.82 1% of Example 6 in above Base Oil 1.87 0.96 The Four-Ball Wear Test results clearly demonstrate the superior antiwear properties of these compositions. It should be noted that the Four-Ball Wear Test is also a test which indicates or predicts the properties of these additives in fuels. The products of selected examples were further blended into 200 second solvent paraffinic neutral lubricating oil and evaluated for control of copper corrosivity using the ASTM D130 Copper Strip Corrosion Test. The test data are shown in Table III. ASTM D130 Copper Strip Corrosion Test (121.1 °C. (250°F.), 3 Hours) Rating Base Oil (200 Second Solvent Paraffinic Neutral Lubricating Oil) 1A 1% of Example 2 in above Base Oil 2B 1% of Example 3 in above Base Oil 1B Corrosion Test Rating 1 represents zero to slight tarnish; 2 represents moderate tarnish; A & B represent shading within numerical grading. The above test results show the good control of copper corrosivity exhibited by these sulfur-containing compositions. The use of additive concentrations of sulfur-coupled hydrocarbyl-derived mercaptobenzothiazole adducts, in accordance with the present invention, in premium quality automotive and industrial lubricants and fuels will significantly enhance their performance, improve stability and extend service life. These novel compositions as described herein are useful at low concentrations and do not contain any potentially undesirable metals or phosphorus. These multifunctional antioxidants and antiwear additives can be commercially made using an economically favorable process.

Claims: A position comprising a major amount of an oil of lubricating viscosity or grease prepared therefrom or liquid hydrocarbyl fuel and a minor multifunctional antioxidant/antiwear/anticorrosion amount of an additive reaction product comprising a sulfur-coupled hydrocarbyl-derived mercaptobenzothiazole prepared by reacting (a) a C₆ to C₆₀ long chain terminal olefin with (b) a sulfur source having the following formula : SxBy wherein B is halogen, x is an integer from 1 to 8 and y is an integer from 1 to 2, and thereafter coupling the product of (a) and (b) with (c) a mercaptobenzothiazole. A position according to claim 1 wherein the mercaptobenzothiazole comprises a 2-mercaptobenzothiazole. A position according to any preceding claim wherein the C₆ to C₆₀ long-chain olefin has the following formula: wherein R represents a C₄ to C₄₀ hydrocarbyl group. A composition to any preceding claim wherein the reaction takes place in the presence of a phase transfer catalyst. A composition according to any preceding claim wherein the phase transfer catalyst comprises a quaternary ammonium salt. A composition according to claim 5 wherein the quaternary ammonium salt comprises tricaprylylmethyl ammonium chloride. A composition according to any preceding claim wherein the reaction product is an octadecene-1/sulfur monochloride/2-mercaptobenzothiazole adduct; a decene-1/sulfur dichloride/2-mercaptobenzothiazole adduct; an octadecene-1/sulfur monochloride/2-mercaptobenzothizole adduct; a decene-1/sulfur dichloride/2-mercaptobenzothiazole adduct; an octadene-1/sulfur monochloride/2-mercaptobenzothiazole adduct; or a decene-1/sulfur dichloride/2-mercaptobenzothiazole adduct. A composition according to any preceding claim wherein the composition comprises an oil of lubricating viscosity selected from mineral oils, synthetic oils and mixtures thereof. A composition according to any of claims 1 to 7 wherein the composition is a grease composition containing from 0.001 to 10% by weight, based on the total weight of the composition, of said reaction product. A composition according to any of claims 1 to 7 wherein the composition is a liquid hydrocarbyl fuel composition. A composition according to claim 10 wherein the composition contains from 2.3 kg (5 pounds) to 567 kg (1250 pounds) of said additive product per 1000 barrels of fuel (158970 liters). A composition according to claim 11 wherein the composition contains from 22.7 kg (50 pounds) to 68 kg (150 pounds) of said additive product per 1000 barrels of fuel (158970 liters). A reaction product which comprises a sulfur-coupled hydrocarbyl-derived mercaptobenzothiazole prepared by reacting (a) a C₆ to C₆₀ long chain terminal olefin with (b) a sulfur source having the following formula : S x B y wherein: B represents a halogen atom; x is an integer from 1 to 8; and y is an integer from 1 to 2, and thereafter coupling the product of (a) and (b) with (c) and mercaptobenzothiazole. A reaction product according to claim 13 wherein less than molar, more than molar or molar quantities of the reactants are used and the reaction temperature varies from ambient to 250°C with the pressure varying from ambient to slightly higher than ambient pressure. A reaction product according to claim 13 or 14 wherein the olefin is a linear olefin. A reaction product according to any of claims 13, 14 or 15 wherein a reactant is defined in any of claims 2 to 7. A process for preparing a lubricant or fuel additive reaction product, which process comprises reacting in molar quantities, less than molar quantities or more than molar quantities (a) a C₆ to C₆₀ long chain terminal olefin having the following formula: wherein R represents a C₄ to C₅₈ hydrocarbyl group, preferably C₄ to C₄₀, with (b) a sulfur source having the following formula: S x B y wherein: B represents a halogen atom; x is an integer from 1 to 8; and y is an integer from 1 to 2, A process according to claim 17 wherein the reaction temperature varies from ambient to 250°C with the pressure varying from ambient to slightly higher and the reaction time varying from 0.5 to at least 24 hours. A process according to claim 17 or 18 wherein the olefin is a linear olefin. A process according to claim 17 or 18 wherein the olefin is a branched olefin. A process according to any of claims 17 to 20 wherein a reactant is defined in any of claims 2 to 7. Use of the additive reaction product of any of claims 13 to 16 in a composition comprising a major amount of an oil of lubricating viscosity or grease prepared therefrom and a minor amount of said additive reaction product to improve the lubricity and fuel economy of internal combustion engines.

Inventors: FARNG LIEHPAO O, HORODYSKY ANDREW G, MURRAY JAMES G, FARNG, LIEHPAO O., HORODYSKY, ANDREW G., MURRAY, JAMES G.
Applicants: MOBIL OIL CORP, MOBIL OIL CORPORATION
Application year: 1990
Main classification: C10M135
IPC codes: C10M151, C10N60, C10N30, C10N70, C10M135, C10L10, C07D277, C10N40, C10L1