POLAR OIL BASED INDUSTRIAL OILS WITH ENHANCED SLUDGE PERFORMANCE

Abstract: Ester based industrial oils containing acid scavengers exhibit improved sludge performance when a minor amount of hydrocarbon oil is included in the formulation.

Description: POLAR OIL BASED INDUSTRIAL OILS WITH ENHANCED SLUDGE PERFORMANCE BACKGROUND OF THE INVENTION FIELD OF THE INVENTION The present invention relates to polar oil, preferably ester based industrial oils of improved sludge performance. DESCRIPTION OF THE RELATED ART USP 3,346,496 is directed to lubricating oils containing carbodiimides as antioxidants. The patent states that the use of carbodiimides makes it possible to substantially improve the resistance of various types of lubricants to oxidative attack. The lubricants can be based on mineral oils or synthetic oil base stocks such as polyethers or polyether esters. The carbodiimides are also reported as being effective protective agents against corrosion and as being capable of keeping decomposition products formed during the lubricating process in solution. The patent states that the c--rbodiimides can be added to the lubricants in combination with diphenyl amine anti oxidants or hydroquinolines and that, surprisingly, a synergistic effect is achieved. Review of the data presented in USP 3,346,496 and the different pathways by which carbodiimides and diphenyl amines act, however, show that these statements are not correct. The carbodiimides react with acidic molecules (carboxylic acids, inorganic acids...) to give neutral products. Thus, if an oil has acidic components, adding a carbodnmide will lower the Total Acid Number (TAN) of the oil. The oxidation of mineral oils is widely understood to take place through a free radical mechanism. Some of the reaction products of this oxidation process are organic acids such as carboxylic acids. The presence of these acids, however, does not significantly promote the oxidation of the mineral oil. Another way of saying this is that the free radical oxidation of mineral oils is not acid catalyzed. Molecules that acts as antioxidants for mineral oils do so by either interrupting the free radical propagation mechanism of the oxidation process or by decomposing free radical initiators such as hydroperoxides. By doing this, they slow down the oxidative degradation of the oils. The TAN of an oil is often used as an indication of the extent to which the oil has oxidized. Again, this is because the concentration of acidic molecules in an oil increases as the oil oxidizes and is thus an indirect measure of the extent of oxidation of the oil. The examples shown in U.S. Patent 3,346,496 use the D 943 oxidation test to measure the oxidation life of the oils. This test measures the TAN of the oil. The time it takes for the TAN of the oil to reach 2.0 mg KOH/mg is deemed the oxidation life of the oil for this test. A unique situation is created when an acid scavenging molecule, such as a carbodim-ide, is added to an oil. The TAN can no longer be used as a measure of the oxidation life of the oil. The oil will undergo its normal oxidation process but the acidic byproducts of oxidation are effectively removed from the oil and therefore the concentration of acid in the sample does not accurately reflect the extent of oil oxidation. It is expected that, in a mineral oil which contains both a diphenyl- amine antioxidant and a carbodiimide acid scavenger, the oxidation life of the oil, as measure by the D 943 test, would be approximately equal to the sum of the oxidation life of the same oil with the same concentration of (hphenyl-miine and the same mineral oil with the same concentration of carbodiimide minus the oxidation life of the mineral oil itself (so you do not count it twice). This is because the mphenylamine antioxidant would react to interfere with the oxidation process of the oil until the diphenylamine was depleted. At this point the oil would start to oxidize and produce acidic products. Once formed, these acidic products would react with the c-irbodiimide. The TAN of the oil would remain low until the carbodiimide was depleted. These two processes are separate events which, for the most part, would happen sequentially. Table 1 of U.S. Patent 3,346,496 lists TAN data, from D 943 testing, relevant to their invention. Review of the data of USP 3,346,496 reveals that the TAN of a naphthene-based oil, with 1% of 2,6,2',6'-tetra-isopropyl- mphenyl-carbodiimide, reaches 2.0 mg KOH/mg after about 510 hours on test. The TAN of the same naphthene-based oil, with 0.2% 4,4'-dimethylbenzyldi- phenylamine, would reach 2.0 mg KOH/mg after about 350 hours on test. From Table 1 of U.S. Patent 3,346,496 it can be estimated that the naphthene-bases oil per se reached a TAN = 2.0 mg KOH/mg after about 30 hours. Therefore, a formulation in the same naphthene-based oil containing 1% of 2,6,2',6'-tetra- isopropyl-diphenyl-c--rbodiimide and 0.2% 4,4'-α methylben-- ldiphenyl--mine would be expected to reach a TAN of 2.0 mg KOH/mg after about 830 hours on test. The data shows this exact combination to reach a TAN of 2.0 mg KOH/mg after about 915 hours on test. This gives a difference of about 85 hours between the expected lifetime and the measured lifetime. The precision statement for the D 943 test states that the repeatability of the test method is 0.192 x (mean measurement value). Therefore, the measured value of 915 hours has an error of +/- 176 hours. Consequently, the measured value of 915 hours is not statistically different from the expected value of about 830 hours. A synergy has only occurred when the combined effect of two or more agents is greater than the sum of the effects of each of the agents separately. Contrary to the claim, the data presented in the U.S. Patent 3,346,496 shows that the combination of carbocl-Liminde and diphenylamine are not synergistic. EP 715079 describes a refrigerator oil comprising an ester type base oil and further containing tri cresyl phosphate and either an epoxy compound comprising glycidyl ether or a carbodiimide acid scavenger. The formulation can also contain a copper deactivator such as 5-methyl-l H benzotriazole or 1-di-octyl amino methyl benzotriazole. The EP '079 states that the hydrolysis of the polyol ester oil was suppressed and hydrolytic production of fatty acids was stabilized by the use of the carbo di imide acid scavenger. USP 5,641,483 teaches that ester based oils containing carbodiimide are resistant to hydrolytic decomposition. At column 11 beginning at line 8, the patent goes on to state that "...if desired, the lubricants for use in refrigerators of the present invention may be mixed with other known refrigerator oils such as synthetic oils (e.g., alkyl benzene, poly-α-olefin, etc)." This said, the patent contains no examples to a lube formulation comprising polyol ester base and carbo di imide acid scavenger and poly alpha olefin oil or any other strictly hydrocarbon oil. It would be advantageous if a way would be found to reduce the sludging tendency of polyol ester based individual lubricating oils. DESCRIPTION OF THE INVENTION It has been discovered that the sludging tendency of polar base stock oils such as ester based industrial lubricant oil cont-tining an acid scavenger can be improved by the addition to the oil of a minor quantity of a substantially essentially hydrocarbon oil such as high saturates content mineral oil, e.g., catalytically hydrogenated oils including hydrofined, hydrotreated, hydrocracked and hydroisomerized oils, oils obtained by gas conversion (e.g., Fischer-Tropsch oils and oils obtained by the hydroisomerization of Fischer- Tropsch waxes produced from synthesis gas, or synthetic oils as exemplified by poly alpha olefin, preferably polyalpha olefin, most preferably, low viscosity PAOs. The polar base stock oils include vegetable oils, polyalkylene glycols, poly esters, phosphate esters, alkylbenzenes, polyol esters, etc. Ester base oils useful in the present invention are well known in the industry and include dibasic acid ester, polyester, aromatic polybasic acid ester, polyol ester and the like, preferably polyol esters. For certain applications the polyol ester oils exhibiting biodegradability may be preferred. The preferred ester oil, the polyol ester oil, is made by reacting polyhydric alcohols such as those containing from 2 to 6 hydroxyl groups, with acids such as mono or di carboxylic acids conta ing, for example, from 2-40 carbon atoms, preferably mono carboxylic acids containing 16-36 carbon atoms, such as oleic and dioleic acid. Typical polyhydric alcohols include trimethylolpropane and pentaerythritol. Polyol ester oils of this type are well known in the literature. Other useful polyol ester oils are described in USP 5,658,863, USP 5,681,800, USP 5,767,047, and USP 4,826,633. The acid scavenger useful in the present invention are of the mono or poly carbodiimide type, the glycidyl ether type, the epoxide type. These materials are well know in the art and will only be briefly described below. Useful mono c-ffbodiimides include materials of the formula Rl — (N = C = N) — R 2 wherein R\ and R2 are the same or different and are hydrogen, hydrocarbyl groups or nitrogen and/or oxygen containing hydrocarbyl groups. Thus Rj and R2 can be C1-C12 aliphatic groups, Cg-Cjg aromatic groups or aromatic- aliphatic groups. Thus, R \ and R2 may be for example hydrogen atom, alkyl groups such as methyl, ethyl, propyl, isopropyl, butyl, isobutyl, pentyl, 2-methylbutyl, hexyl, heptyl, octyl, 2-ethylhexyl, nonyl, decyl, undecyl, dodecyl and the like, alkenyl groups such as propenyl, butenyl, isobutenyl, pentenyl, 2-ethylhexenyl, octenyl and the like, cycloalkyl groups such as cyclopentyl, cyclohexyl, methyl- cyclopentyl, ethylcyclopentyl and the like, aryl groups such as phenyl, naphtyl and the like, alkyl substituted aryl groups such as alkyl substituted phenyl groups for example toluyl, isopropylphenyl, diisopropylphenyl, triisopropylphenyl, nonylphennyl and the like, aralkyl groups such as benzyl, phenetyl and the like. Examples of monocarbodiimides are the following: di-isopropyl-carbodiimide, m-n-butyl-c--rbod-Limide, methyl-tert-butyl-c--rboaiimide, dicyclohexyl- c--rboάijimide, chphenyl-carbodiimide, m-p-tolyl-c-irboα imide and 4,4'- mdodecyl-αiphenyl-c--rboα -ιnide. Of special advantage are diphenyl-mono- c-ιrboc-iimides which carry on the phenyl moiety at the ortho-position to the c-u-boc-iimide group various substituent groups, e.g., alkyl, alkoxy, aryl and aralkyl radicals, such as 2,2'-diethyl-m-phenyl-carbodiiπιide, 2,2'-di-isopropyl- diphenyl-carbodiimide, 2,2'-diethoxy-diphenyl-carbodiimide, 2,6,2'6'-tetra-ethyl- diphenyl-carbodiimide, 2,6,2',6 , -tefr-tisopropyl-m-phenyl-carbodiimide, 2,6,2',6'- tefraethyl-3,3'-ώcUoro-di-phenyl-carbod-j-mide, 2,2'-diethyl-6,6'-dichloro- diphenyl-c-u-bodiimide, 2,6,2 6'-tefra-isobutyl-3,3 , -dinitro-diphenyl- carbodiimide and 2,4,6,2'4^6'-hex sopropyl-mphenyl-c-u:bo(tiimide. Suitable polycarbodiimides are, for example, tetramethylene-ω,ω'- bis-(tert-butyl-carbodiimide), hexamethylene-ω,ω'-bis-(tert-butyl-carboαiimide), teframethylene-ω,ω'-bis-(phenyl-carbodiimide) and those compounds which may be obtained by heating aromatic polyisocyanates such as 1,3-di-isopropyl- phenylene-2,4-di-iso-cyanate, l-methyl-3,5-diethyl-phenylene-2,4-diisocyanate and 3,5,3',5^etia-isopropyl-ώphenylmeth-me-4,4-di-isocyanate, in the presence of tertiary .-mines, basically reacting metal compounds, carboxylic acid metal salts or non-basic organometal compounds at a temperature of at least 120°C, according to the process of German Patent No. 1,156,401. Glycidylether type acid scavengers are generally of the formula where R is an aliphatic or aromatic hydrocarbon. Glycidylether acid scavengers are well known in the literature. Epoxides can be cyclic, acyclic, and polymeric in nature. Cyclic epoxides include the mono- and bis-cyclohexene oxides, monoepoxyethylene cyclohexanes. Acyclic epoxides include epoxidized vegetable oils, epoxidized ester (e.g., ethyl-cis-9,10-epoxy stearate and glycidyl stearate), and the aforementioned glycidyl ethers. Polyepoxy novalacs, polyglycidyl ethers, polyepoxy- cyclohexanes, and polyepoxy esters are examples of polymeric epoxides. Typical useful epoxides are the cycloaliphatic epoxides generally of the formula: where R is a hydrocarbyl group which may contain functional groups such as esters, ethers, ketones, aldehydes, additional epoxy groups, amines, amides, imides, thiolates, etc. Other useful epoxides include epoxides exemplified by: While the use of acid scavengers in ester base oils is well known and an acknowledged way to reduce hydrolysis and increase the oxidation life of ester based oils in the ASTM D943 test (measure of the time it takes for a sample to reach a total acid number of 2.0 mg KOH g), it has been found that the presence of the acid scavenger results in a significant amount of sludge in the oil at the end of 1000 hours in the ASTM D4310 test. The addition of a substantially essentially hydrocarbon oil to polar based oil or ester type base oil containing an acid scavenger has been found to unexpectedly improve the sludge formation resistance of such base oil. The hydrocarbon oil used is any substantially hydrocarbon oil of the paraffinic or naphthenic type, e.g., white oil or other heavily refined mineral oil, or poly alpha olefin, or Fischer-Tropsch wax isomerate oil. Among the preferred mineral oils are the catalyticaUy hydrogenated oils, including hydrofined, hydrocracked, hydrotreated and hydroisomerized oils, such oils having a saturates content of about 92% or higher. By substantially essentially hydrocarbon oil is meant an oil of low or essentially no heteroatom content and having little polarity, an oil essentially made up of carbon and hydrogen. Preferably, the substantially hydrocarbon oil is polyalpha olefin, e.g., PAO 2-PAO 100, preferably PAO 2- PAO 40, most preferably, easily biodegradable PAO 2 (PAO 2 has a percent biodegradability of 53% as measured by the Modified Sturm Test). The particular substantially essentially hydrocarbon oil, e.g., poly alpha olefin oil used, as well as the quantity used is left to the discretion of the practitioner, as dictated by the final viscosity target of the finished lube product. Thus, when using a high viscosity polar oil base stock (e.g., ester), a light substantially essentially hydrocarbon oil will be used to produce a formulated oil of lower overall viscosity. Alternatively, if the base stock is already of the correct viscosity to produce the product a substantially essentially hydrocarbon oil of similar viscosity will be used, the hydrocarbon oil being added for the purpose of reducing the sludging of the polar oil containing the acid scavenger. In practice, the amount of essentially hydrocarbon oil added to the polar base oil acid scavenger combination, will be on the order of about 1 to 25 wt% hydrocarbon oil, preferably about 1 to 10 wt% hydrocarbon oil. The amount of carbodiimide type acid scavenger present will be 0.05 to 5 wt% acid scavenger, preferably 0.1 to 1.0 wt% acid scavenger. When the acid scavenger is of the glycidyl ether or epoxide type, the amount used will be in the range 0.1 to 25 wt%, preferably 1-10 wt%. The lubricating oils for the present invention may also contain any of the other commonly used lubricating oil additives. Thus, the formulated oils can contain additional anti oxidants such as phenol and other amine type anti oxidants, viscosity and viscosity index improvers such as polyalkylene or poly- olefin viscosity improver, e.g., polyisobutylene, poly(meth)acrylate viscosity index improvers metal deactivator such as triazoles and thiadiazoles, extreme pressure and anti wear additives such as phosphate esters, amine phosphates sulfurized olefins, other sulfurized and polysulfurized hydrocarbons, metal thio phosphates such as ZDDP, metal thio carbamates, anti rust agents such as carboxylic acids, dispersants such as succinimides, detergents such as metal sulfonates, phenates or carboxylates, anti foamants, etc. The amount of such other additives included in the formulation will be the amount typically and traditionally used in formulated oils, resulting in an amount in total in the range 0 to 20 wt%. The invention is further described by reference of the following comparative examples and non-limiting examples. EXAMPLE Six (6) formulated oil samples were prepared (Samples A through F). The carbodij-mide acid scavenger Additin RC 8500 was added to three fully biodegradable hydraulic fluid samples. All three formulations have a TAN of less than 2.0 mg KOH/g at the end of 1000 hours in the D4310 test and therefor, are considered to pass the test. All three samples (A, B and C) contain the same additives and a major amount of polyol ester base stock oil. The polyol ester used is described in USP 5,681,800, USP 5,767,046 and USP 5,658,863. It is a neopolyol ester made from tech penta erythritol (mixture of mono-, di-, and tri- pentaeiythritol) reacted with a mixture of predominantly linear Cg-C^ acids and branched Cs acid. The formulations differ in the nature of the minor oil component which is added to adjust down the viscosity of the fluid while m-imtaining good biodegradability. Sample A uses the ester di isodecyladipate (DIDA), Sample B uses polyol ester NP317 and Sample C uses PAO-2. Table 1 presents the formulation data and results. It is seen that Sample C has only 547.9 mg of sludge at the end of the test while Samples A and B have 2571.3 mg and 2979.9 mg respectively. Sample D is similar to Sample B except for the exclusion of the phenolic anti oxidant and the aminic anti oxidant. Sample D also had a high sludge content, 2548.2 mg after 1000 hours. Sample D is presented to show that neither the phenol nor aminic anti oxidants are responsible for the sludge formation. Sample E is identical to Sample D except for the exclusion of the carbodώnide acid scavenger, Additin RC 8500. After 336 hours the sample had a TAN of 2.535 mg KOH/g and clearly failed the test but sludge formation was found to be negligible, leading to the conclusion that sludge formation is intimately linked to the presence of the acid scavenger. Sample F is similar to Sample A, B and C but excludes the DIDA, the NP317 and the PAO of those samples. This sample was evaluated to determine whether the poor sludging tendencies of Samples A and B were due to the presence of the DIDA or NP317 or the absence of PAO 2. Sample F exhibited a sludging tendency which was very high (3516.8 mg). This strongly suggests that the low sludging tendency of Sample C was due to the presence of the PAO 2. Analysis of the sludge from all the samples indicate that the sludge is iron oxide (rust). This suggests that the PAO acts to improve the anti rust characteristics of ester based formulations which contain acid scavenger. This being the case it can be expected that other polar base stocks would be similarly advantageously effected in respect to sludge formation by the addition of PAO. The results are summarized in Table 1. TABLE 1 I * Quantities are in wt%. ** Additive Package A contains triazole metal deactivators, dimercaptothiadiazole metal deactivator, aryl thiophosphate, succinimide rust inhibitor, alkylated phenyl-naphthyl amine antioxidant, and a sulfurized hydrocarbyl sulfurized fatty acid ester EP agent.

Claims: CLAIMS: 1. A lubricating industrial oil of enhanced sludge resistance performance comprising a major amount of a polar base oil containing an acid scavenger and a minor amount of a substantially essentially hydrocarbon oil. 2. The lubricating oil of claim 1 wherein the acid scavenger is selected from the group consisting of carbodiimide, epoxide and glycidyl ether. 3. The lubricating oil of claim 2 wherein when the acid scavenger is carbochimide the c-irbodj-irnide is present in an amount in the range of about 0.05 to 5 wt% and when the acid scavenger is epoxide or glycidyl ether, the epoxide or glycidyl ether is present in an amount in the range of about 0.1 to 25 wt%. 4. The lubricating oil of claim 1, 2 or 3 wherein the substantially essentially hydrocarbon oil is a mineral oil or synthetic oil. 5. The lubricating oil of claim 4 wherein the substantially essentially hydrocarbon oil selected from the group consisting of hydrofined mineral oil, hydrotreated mineral oil, hydrocracked mineral oil, hydroisomerized mineral oil, oil obtained by gas conversion, hydroisomerized Fischer-Tropsch wax, poly alpha olefin. 6. The lubricating oil of claim 1, 2 or 3 wherein the substantially essentially hydrocarbon oil is present in an amount in the range of about 1 to 25 wt%. 7. A method for enhancing the sludge resistance performance of a lubricating oil comprising a major amount of a polar base oil containing an acid scavenger by adding to said lubricating oil a minor amount of a substantially essentially hydrocarbon oil. 8. The method of claim 7 wherein the acid scavenger is selected from the group consisting of carbodiimides, epoxide and glycidyl ether. 9. The method of claim 8 wherein when the acid scavenger is carbodiimides the carboα imide is present in an amount in the range of about 0.05 to 5 wt% and when the acid scavenger is epoxide or glycidyl ether, the epoxide or glycidyl ether is present in an amount in the range of about 0.1 to 25 wt%. 10. The method of claim 7, 8 or 9 wherein the substantially essentially hydrocarbon oil is a mineral oil or synthetic oil. 11. The method of claim 10 wherein the substantially essentially hydrocarbon oil selected from the group consisting of hydrorefined mineral oil, hydrotreated mineral oil, hydrocracked mineral oil, hydroisomerized mineral oil, oil obtained by gas conversion, hydroisomerized Fischer-Tropsch wax, poly alpha olefin and mixtures thereof. 12. The method of claim 7, 8 or 9 wherein the substantially essentially hydrocarbon oil is present in an amount in the range of about 1 to 25 wt%.

Inventors: NADASDI TODD TIMOTHY, NADASDI, TODD, TIMOTHY
Applicants: EXXON RESEARCH ENGINEERING CO, EXXON RESEARCH AND ENGINEERING COMPANY
Application year: 1999
Main classification: C10M169
IPC codes: C10M101, C10M105, C10M107, C10M129, C10M135, C10M169, C10N30