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US3791971A - Lubricating oil compositions - Google Patents

Lubricating oil compositions Download PDF

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Publication number
US3791971A
US3791971A US00215643A US3791971DA US3791971A US 3791971 A US3791971 A US 3791971A US 00215643 A US00215643 A US 00215643A US 3791971D A US3791971D A US 3791971DA US 3791971 A US3791971 A US 3791971A
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United States
Prior art keywords
percent
composition
lubricating oil
acid
neutralization
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US00215643A
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W Lowe
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Chevron USA Inc
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Chevron Research and Technology Co
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M159/00Lubricating compositions characterised by the additive being of unknown or incompletely defined constitution
    • C10M159/12Reaction products
    • C10M159/20Reaction mixtures having an excess of neutralising base, e.g. so-called overbasic or highly basic products
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    • C10M2201/00Inorganic compounds or elements as ingredients in lubricant compositions
    • C10M2201/06Metal compounds
    • C10M2201/062Oxides; Hydroxides; Carbonates or bicarbonates
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    • C10M2203/00Organic non-macromolecular hydrocarbon compounds and hydrocarbon fractions as ingredients in lubricant compositions
    • C10M2203/10Petroleum or coal fractions, e.g. tars, solvents, bitumen
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    • C10M2203/00Organic non-macromolecular hydrocarbon compounds and hydrocarbon fractions as ingredients in lubricant compositions
    • C10M2203/10Petroleum or coal fractions, e.g. tars, solvents, bitumen
    • C10M2203/102Aliphatic fractions
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    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/02Hydroxy compounds
    • C10M2207/023Hydroxy compounds having hydroxy groups bound to carbon atoms of six-membered aromatic rings
    • C10M2207/024Hydroxy compounds having hydroxy groups bound to carbon atoms of six-membered aromatic rings having at least two phenol groups but no condensed ring
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    • C10M2207/02Hydroxy compounds
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    • C10M2207/027Neutral salts thereof
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    • C10M2207/02Hydroxy compounds
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    • C10M2207/028Overbased salts thereof
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    • C10M2209/10Macromolecular compoundss obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
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    • C10M2209/103Polyethers, i.e. containing di- or higher polyoxyalkylene groups
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    • C10M2209/103Polyethers, i.e. containing di- or higher polyoxyalkylene groups
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    • C10M2209/103Polyethers, i.e. containing di- or higher polyoxyalkylene groups
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    • C10M2209/103Polyethers, i.e. containing di- or higher polyoxyalkylene groups
    • C10M2209/107Polyethers, i.e. containing di- or higher polyoxyalkylene groups of two or more specified different alkylene oxides covered by groups C10M2209/104 - C10M2209/106
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    • C10M2209/10Macromolecular compoundss obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
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    • C10M2215/02Amines, e.g. polyalkylene polyamines; Quaternary amines
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    • C10M2215/04Amines, e.g. polyalkylene polyamines; Quaternary amines having amino groups bound to acyclic or cycloaliphatic carbon atoms
    • C10M2215/042Amines, e.g. polyalkylene polyamines; Quaternary amines having amino groups bound to acyclic or cycloaliphatic carbon atoms containing hydroxy groups; Alkoxylated derivatives thereof
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    • C10M2215/02Amines, e.g. polyalkylene polyamines; Quaternary amines
    • C10M2215/06Amines, e.g. polyalkylene polyamines; Quaternary amines having amino groups bound to carbon atoms of six-membered aromatic rings
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    • C10M2215/02Amines, e.g. polyalkylene polyamines; Quaternary amines
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    • C10M2215/086Imides [having hydrocarbon substituents containing less than thirty carbon atoms]
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    • C10M2215/22Heterocyclic nitrogen compounds
    • C10M2215/223Five-membered rings containing nitrogen and carbon only
    • C10M2215/224Imidazoles
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    • C10M2215/24Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant Compositions having hydrocarbon substituents containing thirty or more carbon atoms, e.g. nitrogen derivatives of substituted succinic acid
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    • C10M2223/065Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions having phosphorus-to-carbon bonds containing sulfur
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2010/00Metal present as such or in compounds
    • C10N2010/04Groups 2 or 12

Definitions

  • Lubricating oils are employed as a vehicle for additives which promote the protection of the surfaces lubricated by the oil.
  • the tendency for rusting in internal combustion engines requires that lubricating oils include additives which inhibit rust.
  • the oxidation of lubricating hydrocarbon oils yields a variety of compounds that are deleterious for the service for which the oils are intended.
  • a variety of end products result from this oxidation which attack metals, corrode bearings, and promote wear and rust.
  • Acidic products are also a major source of the oil insolubles that cause ring sticking, sludging, and impede oil flow.
  • the three important mechanisms available for inhibiting rust and corrosion are acid neutralization, inhibition of oil oxidation and protective film formation.
  • acids are involved in the rust and corrosive processes, their neutralization will serve as a preventative.
  • This function is performed by including in lubricating oils for internal combustion engines bases which are capable of neutralizing the acids formed during fuel combustion or introduced into the oil by blow-by or other mechanisms.
  • lubricating oils for internal combustion engines bases which are capable of neutralizing the acids formed during fuel combustion or introduced into the oil by blow-by or other mechanisms.
  • alkaline earth metal carbonates when dispersed in a lubricating oil by means of a dispersant (phenate or sulfonate) will maintain low copper-lead bearing corrosion rates and inhibit rusting as long as the pH of the oil is above 6.
  • Rusting and acidic corrosion constitute serious problems in internal combustion engines, diesel engines, steam turbines, and other machinery exposed to moisture. Corrotsive wear and rusting can be readily controlled by rapid neutralization of acids by effective alkaline additives.
  • compositions of this invention are a combination of a'polyoxyalkylene glycol; or a polyoxyalkylene glycol 3,791,971 Patented Feb. 12, 1974 which has been capped with a polar functional group such as an amino amide, acid, ester, carbonyl, thio or phosphorus group; or the reaction product of a polyoxyalkylene glycol with a carboxylic acid or acid generating compound such as an acid halide or anhydride, or an organic isocyanate, and an alkaline earth metal carbonate dispersed in an oil of lubricating viscosity.
  • a polyoxyalkylene glycol, or its derivatives, in the composition promotes the neutralization of acid from an aqueous phase mixed with the oil as determined by pH measurements.
  • the compositions provide rust and corrosion protection.
  • the alkaline earth metal carbonate will normally be present to provide alkalinity values of from about 0.5 to 100 mg. KOH/g., and more usually from about 1 to 20 mg. KOH/g. While alkalinity values in excess of 10 mg. KOH/g. are not essential for rusting protection, these values will frequently be used for a particular service. For example, in marine lubrication, alkalinity values are high, while in automobile lubrication, alkalinity values are relatively low.
  • additives may be present in the lubricating oil composition to fulfill functions other than those provided for by the dispersed carbonate base and the polyoxyalkylene glycol or its derivatives, as well as to augment the functions of the latter additives.
  • polyoxyalkylene glycols which find use within the scope of the present invention consist of an oxaalkane chain capped by hydroxyl groups and are of the general formula wherein R and R are ethylene or propylene radicals a is in the range from 0 to b/S, b is in the range from 10 to 200, and c is in the range from 0 to b/S, such that the total molecular weight of the polyoxyalkylene glycol is in excess of 1,000.
  • the block copolymers are prepared by adding propylene oxide to the two hydroxyl groups of a propylene glycol nucleus.
  • the resulting hydrophobic base can be made to any controlled length varying from 800 to thousands in molecular weight.
  • By adding ethylene oxide to both ends of this hydrophobic base it is possible to put polyoxyethylene hydrophilic groups on both ends of the molecule.
  • the hydrophilic groups may be added to constitute anywhere from a few percent to percent of the final molecule, U.S. Pat. 2,674,619.
  • the polyoxyalkylene glycols are mixtures of compounds that differ slightly in the polymer chain length. However, their properties approximate those of the molecule represented by their average composition.
  • the overall structure of the preferred molecules of this invention is purposely amphipathic.
  • An amphipathic molecule is an organic species emcompassing in the same molecule two dissimilar structural groups, e.g., a water-soluble and a water-insoluble moiety.
  • the composition, solubility properties, relation and relative sizes of these dissimilar moieties in relation to the overall molecular configuration determines the efliciency of the polyoxyalkylene glycol and its derivatives for our purposes.
  • the ability of the polyoxyalkylene glycol or its derivatives to accelerate the rate of neutralization of acid from an acidic phase by dispersed alkaline earth metal carbonate depends on the total molecular weight and composition of the polyoxyalkylene glycol or its derivatives.
  • This sensitivity to composition and amphiphatic balance of the polyoxyalkylene glycol and their derivatives may be related to our study of the rate of acid-base neutralization between an aqueous and nonaqueous phase which is archetypical of practical operating conditions in motors, engines and turbines.
  • Polyoxyalkylene glycol derivatives Preferred neutralization accelerating derivatives of the polyoxyalkylene glycols have been produced by reacting the glycol with organic monoand polyisocyanates; or monoand dicarboxylic acids, or acid halides and anhydrides, all of which are defined as carboxylic generating compounds, to yield high molecular weight complex reaction products which may be typified as complex polyesters or urethanes.
  • polar functional groups such as carbonyl, acidic, ester, amines, amides, thio and phosphoro groups
  • the dicarboxylic acids which can be utilized by reaction with polyoxyalkylene glycols include oxalic, malonic, succinic, glutaric, adipic, pimelic, suberic, azelaic, sebacic, and other fl w-dicarboxylic acids and alkyl or alkenyl substituted acids of the same name. Of these, oxalic acid and its derivatives is especially preferred because of their stability and reactivity.
  • lower molecular weight acids such as acetic and oxalic are preferred over higher molecular weight acids such as substituted succinic acid, lauric, stearic and other fatty acids, because of the greater ease of reaction of the lower molecular weight acids and the stability and solubility of their polyoxyalkylene glycol esters.
  • the reaction between the high molecular weight polyoxyalkylene glycols and a dicarboxylic acid generating compound is carried out by mixing them directly, or solubilizing in a mutual solvent, in a mole ratio of from 1:3 to 3:1 and heating to about ISO-200 C. for 1 to 100 hours. Suitable and well-known esterification catalysts may be utilized to shorten the time of the reaction.
  • the reaction product is believed to be a complex ester of the following repeating unit.
  • phenyl isocyanate toluene diisocyanate, methylene diphenyl diisocyanate, alkylated methylene diphenyl diisocyanate, hexamethylene diisocyanate, and polymeric isocyanates, such as polymethylene polyphenyl isocyanate.
  • the reaction between the high molecular weight polyoxyalkylene glycol and the organic isocyanate is carried out by directly mixing the reagents, or solubilizing in a mutual solvent, in a mole ratio of from 1:3 to 3:1 and heating to about 25100 C. for from 3 to 48 hours.
  • the urethanes which are produced by the reaction are believed to be typified by the following reaction scheme for the case of a diisocyanate Li H 0'...
  • R is the substantially hydrocarbyl or hydrocarbyl substituted moiety of the diisocyanate
  • R R a, b, and 0 have been previously defined.
  • the number of repeating units is represented by x which may range from 1 to 10 and the resulting urethane has a total molecular weight in the range from about 1,000 to about 50,000.
  • reaction product of polyoxyalkylene glycol and oxalic acid 889 grams of the polyoxyalkylene glycol of Example 2 was mixed in a 3-liter flask with 250 m1. of xylene and 12.6 grams of oxalic acid dihydrate. The mixture was stirred and refluxed for 42 hours at temperatures in excess of 300 F. The product was stripped to 230 F. under vacuum. 890 grams of product was obtained, having an acid number of virtually zero.
  • the reaction product of polyoxyalkylene glycol and toluene diisocyanate was prepared by mixing 111 grams of the polyoxyalkylene glycol of Example 2 with 4.35 grams of toluene diisocyanate in a ZOO-ml. flask. The reaction mixture was stirred for 15 hours at 205:5" F. The product was stripped to 200 F. under vacuum. 114 grams of product were obtained.
  • Alkaline earth metal carbonates are magnesium, calcium and barium carbonates, preferably calcium and barium carbonates. Small amounts of the hydroxides of the metals may be present, usually not contributing more than about 20 percent of the alkalinity value from the alkaline earth metal carbonate composition.
  • the alkaline earth metal compounds are not soluble in hydrocarbon media, therefore they are invariably dispersed with some type of metal salt dispersant. These dispersants are well known in the art and will be discussed only summarily.
  • the preferred dispersants are sulfonate and phenate dispersants.
  • the sulfonates are extensively discussed in US. Pat. No. 3,488,284.
  • the organic sulfonates are prepared either from natural or synthetic sources.
  • the natural sulfonates are referred to as mahogany sulfonates and are derived from petroleum mineral oil fractions, and normally have from about 25 to 50 carbon atoms per sulfonic acid.
  • Synthetic sources are also employed which are usually alkylated benzenes having from about 25 to 50 carbon atoms.
  • the use of the sulfonates and the method of preparing overbased sulfonates is well known and indicated in the above patent. Other relevant patents include US. Pat. Nos. 3,021,280, 3,256,186, 3,057,896 and 3,312,618.
  • the phenates are alkylated phenols either individually or polymerized to a low order of from 8 to 5 alkyl phenols, normally bridged with sulfur, alkylene groups, or dialkylene amino groups (Mannich bases).
  • the alkyl group on the phenol is normally of at least 8 carbon atoms and usually does not exceed 36 carbon atoms, more usually being in the range of about l230 carbon atoms.
  • the phenoxide in the phenate also contributes to the alkalinity value.
  • the phosphonates will normally contain at least about 30 carbon atoms and may contain as ,many as 200 carbon atoms, more usually from about 50-125 carbon atoms. These overbased phosphonates-are described in US. Pat. No.-3,312,618.,
  • the alkalinity value of the overbased dispersants will usually be at least 150 and not exceed 500, more, usually being in the range of from about 200 to 450 mg. KOH/ g.
  • the equivalent ratio of base to dispersant will be at least 1:1 and more usually at least 1.5: 1, normally not exceeding about 20:1.
  • Lubricating oils Qth r' dditi es Other additives are often desirably included in the composition. These additives are pourpoint depressants, oiliness'agents, anti-oxidants, detergents, corrosion inhibitors,
  • the individual additives may vary in amounts from about 0.01- [10 weight percent-of the total composition. In concentrates, the weight percent of these additives will usually range from about 03-30 weight percent.
  • a preferred group of additives is the succinimides of Ialkylene polyaminfes.
  • the succinimides are useful as sludge dispersants. They usually have an alkyl or alkenyl bonded to the succinimide group of at least 50 carbon atoms and not more than about 200 carbon atoms.
  • alkylene polyamines are normally ethylene or propylene ly n .,h ie 12-6. i o o s e m usually. from about, 35, amino groups; see, for example,
  • compositions of this invention are especially preferred group of additives, because of their effectiveness when used combination with the neutralizationrate accelerating compounds of this inven-
  • Another preferred aspect of using the compositions of this invention is the inclusion in the lubricating oil of .from: about 1 to 50 rum/kg. of a dihydrocarbyl phosphorodithioate, wherein the hydrocarbyl groups contain from about 436 carbon atoms.
  • the hydrocarbyl groups will be alkyl or alkaryl groups. The remaining valence of the phosphorodithioate will usually be satisfied or athird hydrocarbyl group mayalsobeused.
  • NRT Neutralization Rate Test
  • PI point of inflection
  • TPI point of inflection
  • the PI corresponds to the first end point for the acid-base titration in the given system.
  • the first end point in the purely aqueous titration of 0.01 N HCl with 0.02 N sodium carbonate occurs at pH 4.5 and is believed to correspond to the conversion of HCl to carbonic acid.
  • a second end point occurs at pH 8.1 and is believed to correspond to the conversion of dissolved carbonic acid to bicarbonate.
  • the time elapsed from initial mixing of oil and aqueous phase to the PI is the TPI and it forms the basis for comparing various oil compositions in the NRT.
  • TPI time elapsed from initial mixing of oil and aqueous phase to the PI
  • the one with a low TPI rating fast acid neutralization
  • TPI slow acid neutralization
  • the performance of the lubricating oil compositions in the well-known Sequence IIB engine test are related to NRT results in these cases, all other factors being kept constant.
  • the NRT is used to test the efficiency of the polyoxyalkylene glycols and their derivatives as oil-soluble neutralization rate accelerators.
  • Test procedure is as follows: A 250-ml. beaker containing aqueous HCl (0.01- 0.003 N) is fitted into a test stand with a stirring paddle and the electrodes of a Beckman Expandomatic pH meter immersed in the solution. For highest reproducibility, the
  • the rate of stirring (500 r.p.m.) should be constant and the electrodes (Calomel and Glass electrodes) should be in the same relative position for each test. Since the oil phase may have a tendency to foul the Glass electrode, periodic application of Desicote (Beckman hydrophobic surface coating) should be applied as a preventative.
  • the test oil composition 50 ml., is layered onto the aqueous with as little mixing as possible. The pH meter, stopwatch, and the stirrer are started simultaneously. pH readings are then made at known elapsed times and plotted versus the time.
  • the TPI will vary from more than 150 minutes for certain tested oil compositions containing carbonate, but having no acid neutralization rate accelerators, to less than 1 minute with certain polyoxyalkylene glycols or their derivatives.
  • Important test parameters are, first, base oil viscosity twhich should not vary by more than 15 percent in any comparison of lubricating oil compositions; secondly, the normality of the acid which, if reduced by one-half reduces the TPI (roughly) by one-half. This parameter may be used to adjustthe scale of neutralization times in different series of tests. Reproducibility of the NRT has been established by extensive testing.
  • a lubricating oil composition consisting of a neutral petroleum oil of viscosity SUS at 100 F., 25 mM./
  • Example 3 Lubricating oil composition of Example 1 with the addition of 0.05 percent or more of the reaction product of the polyoxyalkylene glycol of Example 2 with toluene diisocyanate in a mole ratio of approximately 1:1.
  • Example 4 A lubricating oil composition consisting of a neutral petroleum oil of viscosity 100 SUS at 100 F., 25 mM./ kg. of a calcium carbonate sulfonate-dispersant composition containing 2.35 percent calcium, 40 mM./kg. of a calcium carbonate phenate-dispersant composition con taining 9.25 percent calcium, 15 mM./ kg. of zinc dithiophosphate composition containing 2.85 percent phosphorus and 4 percent by Weight of polyisobutylene succinimide of triethylene tetramine.
  • Example 5 The lubricating oil composition of Example 4 with the addition of 0.1 percent of the polyoxyalkylene glycol block copolymer of Example 2.
  • Example 6 The lubricating oil composition of Example 4 with the addition of 0.1 percent of the reaction product of the polyoxyalkylene glycol of Example 2 with oxalic acid in the mole ratio of 2:1.
  • Example 7 The lubricating oil composition of Example 4 with the addition of 0.1 percent of the reaction product of the polyalkylene glycol of Example 2 with oxalyl chloride in the mole ratio of 1:1.
  • Example 8 The lubricating oil composition of Example 4 with the addition of 0.1 percent of the reaction product of the polyoxyalkylene glycol of Example 2 with toluene diisocyanate in the mole ratio 1:1.
  • Example 9 The lubricating oil composition of Example 8 wherein the toluene diisocyanate and the polyoxyalkylene glycol are reacted in the mole ratio of 1:2.
  • Example 10 The lubricating oil composition of Example 4 with the addition of 0.1 percent of the reaction product of the polyoxyalkylene glycol of Example 2 with pblyisobutenyl succinic anhydride in the mole ratio of 1:2.
  • Example 11 The lubricating oil composition of Example 4 with the addition of 0.1 percent of the reaction product of the polyoxyalkylene glycol of Example 2 with dodecenyl succinic anhydride in the mole ratio of 1:2.
  • Example 12 The lubricating oil composition of Example 4 with the addition of 0.1 percent of the reaction productof the polyoxyalkylene glycol of Example 2 withsebacic acid in the mole ratio 1:1.
  • Example 13 The lubricating oil composition of Example 4 with the addition of 0.1 percent of "the reaction product 'of the polyoxyalkylene glycol of Example 2 with phenyl isocyanate in the mole ratio of 1:2.
  • Example 14 The lubricating oil composition of Example 4 with the addition of 0.1 percent of the reaction product of the polyoxyalkylene glycol of Example 2 with decanoic acid in the mole ratio 1:2. 4
  • Reference Oil A is a neutral petroleum oil of viscosity 120 SUS at 100 F., mMJkg. of zinc dithiophosphate and 2 percent by weight of polyisobutenyl succinimide oi tetra ethylenepentamine.
  • Reference oil B is a neutral petroleum oil of viscosity $118 at 100 F., 25 mM./kg. of calcium carbonate suli'onate dispersant composition containing 2.35 percent calcium, 40 mMJkg. of calcium carbonate-phenate dispersant composition containing 9.25 percent calcium, 15 mMJkg. of zinc dithiophosphate and- 4 percent by weight of polyisobutenyl succinimide of triethylene tetramine.
  • Table I illustrates the remarkableneduction in neutralization times achieved by-the addition of'even very small percentages of neutralization rate accelerators.
  • Neutralization times for the reference oils containing calcium carbonate dispersed by sulfonates and phenates is excessive, in spite of the fact that the oils have high alkalinity.
  • the neutralization rate accelerators illustrated in Table I exemplify satisfactorily performing neutralization promoters.
  • neutralization rate accelerators which substantially reduce the TPI relative to that of the reference oil zero-weight percent of acid neutralization accelerator
  • reduction in the TPI of better than 50 percent is regarded as evidence that the addition agent will function to help fulfill the objects of this invention.
  • Other properties which are needed such as additive compatibility, stability, etc.
  • Table II illustrates the distinguishing characteristics of the polyoxyalkylene glycols of the present invention. It is clear that preferably the polyoxyalkylene glycol should contain substantially less than 50 percent polyoxyethylene units by weight and should have a molecular weight substantially over 1,000 and preferably substantially over 5,000.
  • Example 2 gives a satisfactorily clean diesel engine after several hours of running, and also gives a rust rating of 9.2 in the MS Sequence IIB engine rust test (GM specifications require an average engine rust rating of 8.9 to pass the MS Sequence IIB test).
  • Table III illustrates the excellent IIB Average Engine Rust ratings (AER) obtainable from the combination of dispersed alkaline earth metal carbonate and polyoxyalkylene glycol and its derivatives in a lubricating composition. The aforementioned table illustrates that the carbonate alone i insufiicient to retard rust forma tion to the degree desired, although the absence of acid neutralizing carbonate would, of course, lead to severe corrosion and rusting.
  • AER IIB Average Engine Rust ratings
  • compositions of polyoxyalkylene glycols and their derivatives permits smaller amounts of ash to be introduced into the lubricating oil and therefore avoid problems associated with high ash oils.
  • a lubricating oil composition comprising:
  • alkaline earth metal carbonate dispersed in said hydrocarbon oil with a dispersant selected from the group consisting of phenates and sulfonates, to provide an alkalinity value of from 0.5 to mg. KOH/ g.
  • a lubricating oil composition comprising:
  • a major amount of a hydrocarbon oil of lubricating viscosity from about 0.01 to 5 weight percent of an amphipathic oil-soluble acid neutralization accelerating composition which is the reaction product of a polyoxyalkylene glycol having a molecular weight in the range from 1,000 to 10,000 with an organic isocyanate;
  • alkaline earth metal carbonate dispersed in said hydrocarbon oil, with a dispersant selected from the group consisting of phenates and sulfonates, to provide an alkalinity value of from 0.5 to 100 mg. KOH/ g.
  • composition according to claim 1 wherein said alkaline earth metal carbonate is calcium carbonate.
  • composition according to claim 3 wherein said dispersant is a sulfonate dispersant derived from a sulfonic acid of from 25 to 50 carbon atoms.
  • composition according to claim 3 wherein said dispersant is a phenate derived from alkylated phenol or polymerized alkylated phenols having 2 to 5 phenol groups per molecule and an alkyl group of from 12 to 30 carbon atoms.
  • composition according to claim 2 wherein said alkaline earth metal carbonate is calcium carbonate.
  • composition according to claim 6 wherein said dispersant is a sulfonate dispersant derived from a sulfonic acid of from 25 to 50 carbon atoms.
  • composition according to claim 6 wherein said dispersant is a phenate derived from alkylated phenol or polymerized alkylated phenols having 2 to 5 phenol groups per molecule and an alkyl group of from 12 to 30 carbon atoms.

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Abstract

POLYOXYALKYLENE GLYCOLS AND THEIR REACTION PRODUCTS WITH ORGANIC DIISOCYANATE AND DICARBOXYLIC ACID ARE COMBINED WITH ALKALINE EARTH METAL CARBONATES DISPERSED IN A HYDROCARBON MEDIUM TO PROVIDE LYBRICATING COMPOSITIONS OF SUPERIOR ACID NEUTRALIZATION CAPABILITY AND RUST INHIBITION IN INTERNAL COMBUSTION ENGINES.

Description

United States Patent O Na U.S. Cl. 252- 33.4 8 Claims ABSTRACT OF THE DISCLOSURE Polyoxyalkylene glycols and their reaction products with organic diisocyanate and dicarboxylic acid are combined with alkaline earth metal carbonates dispersed in a hydrocarbon medium to provide lubricating compositions of superior acid neutralization capability and rust inhibition in internal combustion engines.
CROSS-REFERENCES This is a continuation-in-part of copending application Ser. No. 142,838, filed May 10, 1971, which is itself a 'continuation-in-part of application Ser. No. 45,567, filed June 11, 1970, now Pat. No. 3,711,406.
BACKGROUND OF THE INVENTION Field of the invention Lubricating oils are employed as a vehicle for additives which promote the protection of the surfaces lubricated by the oil. The tendency for rusting in internal combustion engines requires that lubricating oils include additives which inhibit rust. The oxidation of lubricating hydrocarbon oils yields a variety of compounds that are deleterious for the service for which the oils are intended. A variety of end products result from this oxidation which attack metals, corrode bearings, and promote wear and rust. Acidic products are also a major source of the oil insolubles that cause ring sticking, sludging, and impede oil flow. The three important mechanisms available for inhibiting rust and corrosion are acid neutralization, inhibition of oil oxidation and protective film formation. Since acids are involved in the rust and corrosive processes, their neutralization will serve as a preventative. This function is performed by including in lubricating oils for internal combustion engines bases which are capable of neutralizing the acids formed during fuel combustion or introduced into the oil by blow-by or other mechanisms. For example, alkaline earth metal carbonates, when dispersed in a lubricating oil by means of a dispersant (phenate or sulfonate) will maintain low copper-lead bearing corrosion rates and inhibit rusting as long as the pH of the oil is above 6.
Rusting and acidic corrosion constitute serious problems in internal combustion engines, diesel engines, steam turbines, and other machinery exposed to moisture. Corrotsive wear and rusting can be readily controlled by rapid neutralization of acids by effective alkaline additives.
DESCRIPTION OF THE PRIOR ART Neutralization rate accelerators are new in the lubrication art. Polyoxyalkylene glycols and their esters have often been utilized as synthetic lubricants. Low molecular weight polyoxyalkylene glycols and their esters have found some use as lubricating oil additives. For example, U.S. Pat. 3,509,052 teaches the use of polyoxyalkylene polyols as demulsifiers in certain lubricating oil compositions.
SUMMARY OF THE INVENTION The compositions of this invention are a combination of a'polyoxyalkylene glycol; or a polyoxyalkylene glycol 3,791,971 Patented Feb. 12, 1974 which has been capped with a polar functional group such as an amino amide, acid, ester, carbonyl, thio or phosphorus group; or the reaction product of a polyoxyalkylene glycol with a carboxylic acid or acid generating compound such as an acid halide or anhydride, or an organic isocyanate, and an alkaline earth metal carbonate dispersed in an oil of lubricating viscosity. The presence of a polyoxyalkylene glycol, or its derivatives, in the composition promotes the neutralization of acid from an aqueous phase mixed with the oil as determined by pH measurements. The compositions provide rust and corrosion protection.
DETAILED DESCRIPTION OF THE INVENTION The combination of polyoxyalkylene glycols or their derivatives and alkaline earth metal carbonates dispersed in an oil of lubricating viscosity, in accordance with the present invention, results in surprising improvement in the rate of acid neutralization as demonstrated by the Acid Neutralization Rate Test to be described. This use of polyoxyalkylene glycols or their derivatives in combination with the dispersed carbonate inhibits rust formation and the corrosion of ferrous metal surfaces in contact with lubricants containing said combinations. The polyoxyalkylene glycols or their derivatives are present in amounts from 0.01 to about 5 percent by weight of the composition.
The alkaline earth metal carbonate will normally be present to provide alkalinity values of from about 0.5 to 100 mg. KOH/g., and more usually from about 1 to 20 mg. KOH/g. While alkalinity values in excess of 10 mg. KOH/g. are not essential for rusting protection, these values will frequently be used for a particular service. For example, in marine lubrication, alkalinity values are high, while in automobile lubrication, alkalinity values are relatively low.
Other additives may be present in the lubricating oil composition to fulfill functions other than those provided for by the dispersed carbonate base and the polyoxyalkylene glycol or its derivatives, as well as to augment the functions of the latter additives.
COMPONENTS Polyoxyalkylene glycols The polyoxyalkylene glycols which find use within the scope of the present invention consist of an oxaalkane chain capped by hydroxyl groups and are of the general formula wherein R and R are ethylene or propylene radicals a is in the range from 0 to b/S, b is in the range from 10 to 200, and c is in the range from 0 to b/S, such that the total molecular weight of the polyoxyalkylene glycol is in excess of 1,000.
Some of the lower molecular Weight polyoxyalkylene glycols within this range, are commercially available from Wyandotte Chemicals Corporation as the Pluronic series. The block copolymers are prepared by adding propylene oxide to the two hydroxyl groups of a propylene glycol nucleus. The resulting hydrophobic base can be made to any controlled length varying from 800 to thousands in molecular weight. By adding ethylene oxide to both ends of this hydrophobic base, it is possible to put polyoxyethylene hydrophilic groups on both ends of the molecule. The hydrophilic groups may be added to constitute anywhere from a few percent to percent of the final molecule, U.S. Pat. 2,674,619. In general, the polyoxyalkylene glycols are mixtures of compounds that differ slightly in the polymer chain length. However, their properties approximate those of the molecule represented by their average composition.
The overall structure of the preferred molecules of this invention is purposely amphipathic. An amphipathic molecule is an organic species emcompassing in the same molecule two dissimilar structural groups, e.g., a water-soluble and a water-insoluble moiety. The composition, solubility properties, relation and relative sizes of these dissimilar moieties in relation to the overall molecular configuration determines the efliciency of the polyoxyalkylene glycol and its derivatives for our purposes. That is, as will be shown, the ability of the polyoxyalkylene glycol or its derivatives to accelerate the rate of neutralization of acid from an acidic phase by dispersed alkaline earth metal carbonate, depends on the total molecular weight and composition of the polyoxyalkylene glycol or its derivatives. This sensitivity to composition and amphiphatic balance of the polyoxyalkylene glycol and their derivatives, may be related to our study of the rate of acid-base neutralization between an aqueous and nonaqueous phase which is archetypical of practical operating conditions in motors, engines and turbines.
Polyoxyalkylene glycol derivatives Preferred neutralization accelerating derivatives of the polyoxyalkylene glycols have been produced by reacting the glycol with organic monoand polyisocyanates; or monoand dicarboxylic acids, or acid halides and anhydrides, all of which are defined as carboxylic generating compounds, to yield high molecular weight complex reaction products which may be typified as complex polyesters or urethanes. Other derivatives of polyoxyalkylene compounds which are useful to a lesser extent as neutralization rate accelerators when used in combination with dispersed alkaline earth metal carbonates include oxaalkane chains capped with polar functional groups such as carbonyl, acidic, ester, amines, amides, thio and phosphoro groups, for example, see Lowe US. Pat. 3,037,056 and US. Pat. 8,879,230. Of these, the acetate ester-capped polyoxyalkylene glycols are preferred in many instances because of their solubility.
The dicarboxylic acids which can be utilized by reaction with polyoxyalkylene glycols include oxalic, malonic, succinic, glutaric, adipic, pimelic, suberic, azelaic, sebacic, and other fl w-dicarboxylic acids and alkyl or alkenyl substituted acids of the same name. Of these, oxalic acid and its derivatives is especially preferred because of their stability and reactivity. In general, lower molecular weight acids such as acetic and oxalic are preferred over higher molecular weight acids such as substituted succinic acid, lauric, stearic and other fatty acids, because of the greater ease of reaction of the lower molecular weight acids and the stability and solubility of their polyoxyalkylene glycol esters.
The reaction between the high molecular weight polyoxyalkylene glycols and a dicarboxylic acid generating compound is carried out by mixing them directly, or solubilizing in a mutual solvent, in a mole ratio of from 1:3 to 3:1 and heating to about ISO-200 C. for 1 to 100 hours. Suitable and well-known esterification catalysts may be utilized to shorten the time of the reaction. The reaction product is believed to be a complex ester of the following repeating unit.
phenyl isocyanate, toluene diisocyanate, methylene diphenyl diisocyanate, alkylated methylene diphenyl diisocyanate, hexamethylene diisocyanate, and polymeric isocyanates, such as polymethylene polyphenyl isocyanate.
The reaction between the high molecular weight polyoxyalkylene glycol and the organic isocyanate is carried out by directly mixing the reagents, or solubilizing in a mutual solvent, in a mole ratio of from 1:3 to 3:1 and heating to about 25100 C. for from 3 to 48 hours. The urethanes which are produced by the reaction are believed to be typified by the following reaction scheme for the case of a diisocyanate Li H 0'...
where R is the substantially hydrocarbyl or hydrocarbyl substituted moiety of the diisocyanate, and R R a, b, and 0 have been previously defined. The number of repeating units is represented by x which may range from 1 to 10 and the resulting urethane has a total molecular weight in the range from about 1,000 to about 50,000.
To prepare the reaction product of polyoxyalkylene glycol and oxalic acid, 889 grams of the polyoxyalkylene glycol of Example 2 was mixed in a 3-liter flask with 250 m1. of xylene and 12.6 grams of oxalic acid dihydrate. The mixture was stirred and refluxed for 42 hours at temperatures in excess of 300 F. The product was stripped to 230 F. under vacuum. 890 grams of product was obtained, having an acid number of virtually zero. The reaction product of polyoxyalkylene glycol and toluene diisocyanate was prepared by mixing 111 grams of the polyoxyalkylene glycol of Example 2 with 4.35 grams of toluene diisocyanate in a ZOO-ml. flask. The reaction mixture was stirred for 15 hours at 205:5" F. The product was stripped to 200 F. under vacuum. 114 grams of product were obtained.
Alkaline earth metal carbonates The alkaline earth metal carbonates are magnesium, calcium and barium carbonates, preferably calcium and barium carbonates. Small amounts of the hydroxides of the metals may be present, usually not contributing more than about 20 percent of the alkalinity value from the alkaline earth metal carbonate composition. The alkaline earth metal compounds are not soluble in hydrocarbon media, therefore they are invariably dispersed with some type of metal salt dispersant. These dispersants are well known in the art and will be discussed only summarily.
The preferred dispersants are sulfonate and phenate dispersants. The sulfonates are extensively discussed in US. Pat. No. 3,488,284. The organic sulfonates are prepared either from natural or synthetic sources. The natural sulfonates are referred to as mahogany sulfonates and are derived from petroleum mineral oil fractions, and normally have from about 25 to 50 carbon atoms per sulfonic acid. Synthetic sources are also employed which are usually alkylated benzenes having from about 25 to 50 carbon atoms. The use of the sulfonates and the method of preparing overbased sulfonates is well known and indicated in the above patent. Other relevant patents include US. Pat. Nos. 3,021,280, 3,256,186, 3,057,896 and 3,312,618.
Another class of dispersant for alkaline earth metal carbonates are the phenates. The phenates are alkylated phenols either individually or polymerized to a low order of from 8 to 5 alkyl phenols, normally bridged with sulfur, alkylene groups, or dialkylene amino groups (Mannich bases). The alkyl group on the phenol is normally of at least 8 carbon atoms and usually does not exceed 36 carbon atoms, more usually being in the range of about l230 carbon atoms. The phenoxide in the phenate also contributes to the alkalinity value. The overbased us. Pat; 3,361,673.
. by zinc, but, polyoxyalkylene phenates are described in numerous patents such as US. Pat. Nos. 3,474,035, 3,429,812, 3,388,063, 3,336,224, and 2,798,852.
Other dispersants which are employed are the alkaline earth metal alkylphosphonates and thiophosphonates. The phosphonates will normally contain at least about 30 carbon atoms and may contain as ,many as 200 carbon atoms, more usually from about 50-125 carbon atoms. These overbased phosphonates-are described in US. Pat. No.-3,312,618.,
The alkalinity value of the overbased dispersants will usually be at least 150 and not exceed 500, more, usually being in the range of from about 200 to 450 mg. KOH/ g. The equivalent ratio of base to dispersant will be at least 1:1 and more usually at least 1.5: 1, normally not exceeding about 20:1. These compositions are used in a sufiicient amount to provide the desired alkalinity value in the final composition. Therefore, the alkaline earth metal carbonates are prepared as concentrates and then diluted in the lubricating oil medium, and the polyoxyalkylated' compound is added to provide the desired end composition.
Lubricating oils Qth r' dditi es Other additives are often desirably included in the composition. These additives are pourpoint depressants, oiliness'agents, anti-oxidants, detergents, corrosion inhibitors,
vl extreme pressure agents, antifoamants, etc. Usually, for .oils to be used in an engine the total amount of these additives will range from about 0.5-15 weight percent,
-' more usually fromabout 0.5- weight percent. The individual additives may vary in amounts from about 0.01- [10 weight percent-of the total composition. In concentrates, the weight percent of these additives will usually range from about 03-30 weight percent.
A preferred group of additives is the succinimides of Ialkylene polyaminfes. The succinimides are useful as sludge dispersants. They usually have an alkyl or alkenyl bonded to the succinimide group of at least 50 carbon atoms and not more than about 200 carbon atoms. The
alkylene polyamines are normally ethylene or propylene ly n .,h ie 12-6. i o o s e m usually. from about, 35, amino groups; see, for example,
.1 An especially preferred group of additives, because of their effectiveness when used combination with the neutralizationrate accelerating compounds of this inven- Another preferred aspect of using the compositions of this invention is the inclusion in the lubricating oil of .from: about 1 to 50 rum/kg. of a dihydrocarbyl phosphorodithioate, wherein the hydrocarbyl groups contain from about 436 carbon atoms. Usually, the hydrocarbyl groups will be alkyl or alkaryl groups. The remaining valence of the phosphorodithioate will usually be satisfied or athird hydrocarbyl group mayalsobeused.
Neutralization rate test The Neutralization Rate Test (NRT) consists of the neutralization of an acidic aqueous phase with a basic oil phase. The progress of the neutralization is followed with a pH meter by measuring the pH at 15-sec., or some other convenient interval. The pH is then plotted versus the time. Lubricating oil compositions containing dispersed alkaline earth metal carbonates will neutralize the acid and exhibit a definite point of inflection (PI), usually in the pH range of 3.5-6.5, but the time elapsed to the point of inflection (TPI) varies widely depending on the presence or absence of a neutralizing rate acceleratorof the present invention, all other test factors being-kept constant.
It is believed that the PI corresponds to the first end point for the acid-base titration in the given system. For example, the first end point in the purely aqueous titration of 0.01 N HCl with 0.02 N sodium carbonate occurs at pH 4.5 and is believed to correspond to the conversion of HCl to carbonic acid. A second end point occurs at pH 8.1 and is believed to correspond to the conversion of dissolved carbonic acid to bicarbonate.
The time elapsed from initial mixing of oil and aqueous phase to the PI is the TPI and it forms the basis for comparing various oil compositions in the NRT. In general, in the comparison of two oil compositions, the one with a low TPI rating (fast acid neutralization) has appeared to have better rust performance than the composition with higher TPI (slower acid neutralization) all other factors being kept constant. In examples to be elaborated below, the performance of the lubricating oil compositions in the well-known Sequence IIB engine test are related to NRT results in these cases, all other factors being kept constant. Thus, the NRT is used to test the efficiency of the polyoxyalkylene glycols and their derivatives as oil-soluble neutralization rate accelerators. Test procedure is as follows: A 250-ml. beaker containing aqueous HCl (0.01- 0.003 N) is fitted into a test stand with a stirring paddle and the electrodes of a Beckman Expandomatic pH meter immersed in the solution. For highest reproducibility, the
rate of stirring (500 r.p.m.) should be constant and the electrodes (Calomel and Glass electrodes) should be in the same relative position for each test. Since the oil phase may have a tendency to foul the Glass electrode, periodic application of Desicote (Beckman hydrophobic surface coating) should be applied as a preventative. Next, the test oil composition, 50 ml., is layered onto the aqueous with as little mixing as possible. The pH meter, stopwatch, and the stirrer are started simultaneously. pH readings are then made at known elapsed times and plotted versus the time. The TPI will vary from more than 150 minutes for certain tested oil compositions containing carbonate, but having no acid neutralization rate accelerators, to less than 1 minute with certain polyoxyalkylene glycols or their derivatives.
Important test parameters are, first, base oil viscosity twhich should not vary by more than 15 percent in any comparison of lubricating oil compositions; secondly, the normality of the acid which, if reduced by one-half reduces the TPI (roughly) by one-half. This parameter may be used to adjustthe scale of neutralization times in different series of tests. Reproducibility of the NRT has been established by extensive testing.
EXAMPLES A lubricating oil composition consisting of a neutral petroleum oil of viscosity SUS at 100 F., 25 mM./
kg. of a calcium carbonate sulfonate-dispersant composition containing 2.35 percent calcium, 40 mM./kg. of a calcium carbonate phenate-dispersant composition containing 9.25 percent calcium, 25 mM./kg. of zinc dithiophosphate composition containing 2.85 percent phosphorm and 4 percent by weight of polyisobutylene succinimide of tetraethylene pentamine (mole ratio of succinic anhydride to polyamine 0.50).
Example 2 The lubricating oil composition of Example 1 with the addition of 0.1 percent of polyoxyalkylene glycol block copolymer having about 10 percent by weight of poly- =oxyethylene and 90 percent by weight of polyoxypropylene, and molecular weight of about 4,440.
Example 3 Lubricating oil composition of Example 1 with the addition of 0.05 percent or more of the reaction product of the polyoxyalkylene glycol of Example 2 with toluene diisocyanate in a mole ratio of approximately 1:1.
Example 4 A lubricating oil composition consisting of a neutral petroleum oil of viscosity 100 SUS at 100 F., 25 mM./ kg. of a calcium carbonate sulfonate-dispersant composition containing 2.35 percent calcium, 40 mM./kg. of a calcium carbonate phenate-dispersant composition con taining 9.25 percent calcium, 15 mM./ kg. of zinc dithiophosphate composition containing 2.85 percent phosphorus and 4 percent by Weight of polyisobutylene succinimide of triethylene tetramine.
Example 5 The lubricating oil composition of Example 4 with the addition of 0.1 percent of the polyoxyalkylene glycol block copolymer of Example 2.
Example 6 The lubricating oil composition of Example 4 with the addition of 0.1 percent of the reaction product of the polyoxyalkylene glycol of Example 2 with oxalic acid in the mole ratio of 2:1.
Example 7 The lubricating oil composition of Example 4 with the addition of 0.1 percent of the reaction product of the polyalkylene glycol of Example 2 with oxalyl chloride in the mole ratio of 1:1.
Example 8 The lubricating oil composition of Example 4 with the addition of 0.1 percent of the reaction product of the polyoxyalkylene glycol of Example 2 with toluene diisocyanate in the mole ratio 1:1.
Example 9 The lubricating oil composition of Example 8 wherein the toluene diisocyanate and the polyoxyalkylene glycol are reacted in the mole ratio of 1:2.
Example 10 The lubricating oil composition of Example 4 with the addition of 0.1 percent of the reaction product of the polyoxyalkylene glycol of Example 2 with pblyisobutenyl succinic anhydride in the mole ratio of 1:2.
Example 11 The lubricating oil composition of Example 4 with the addition of 0.1 percent of the reaction product of the polyoxyalkylene glycol of Example 2 with dodecenyl succinic anhydride in the mole ratio of 1:2.
Example 12 The lubricating oil composition of Example 4 with the addition of 0.1 percent of the reaction productof the polyoxyalkylene glycol of Example 2 withsebacic acid in the mole ratio 1:1. v I Example 13 The lubricating oil composition of Example 4 with the addition of 0.1 percent of "the reaction product 'of the polyoxyalkylene glycol of Example 2 with phenyl isocyanate in the mole ratio of 1:2.
Example 14 The lubricating oil composition of Example 4 with the addition of 0.1 percent of the reaction product of the polyoxyalkylene glycol of Example 2 with decanoic acid in the mole ratio 1:2. 4
TAB LE I Percent additive.
Composition 1 99999999999 rv-nr-nwi-nwwrpvno 1 Compositions correspond to numbered examples of the same number.
1 Weight percent of neutralization rate accelerator in lubricating oil composition containing dispersed alkaline earth metalcarbonate.
3 Time to point of inflection (TPI) in minutes, 0.01 N HCl aqueous phase in the neutralization rate test.
TABLE II Percent Percent polyoxy- Molecpolyoxyalkylene ular Composition 1 ethylene 3 glycol 3 weight 4 TIP A- 0 c 165 18 02 1 B 10 0.1 r-a 10 0.2 1 10 0.1 3 A 10 0.5 1 10 0.5 I 1 10 0.2 3 1o 0. 1 30 10 0.5 1 10 0.2 30 A- 10 p 0.5 2 B- 10 0.5 56 30 0.5 37 A 30 0.5 2 50 0.5 40 50 0.5 40 10 0.1 1.0 10 0.075 4.6 B 10 0.05 73 0 0.05 8,000 1.65 0 0. 025 8, 000 6. 25
1 Composition consisting of reference oils A or B including dispersed alkaline earth metal carbonate and polyoxyalkylene glycol as shown, in indicated percentages. Reference Oil A is a neutral petroleum oil of viscosity 120 SUS at 100 F., mMJkg. of zinc dithiophosphate and 2 percent by weight of polyisobutenyl succinimide oi tetra ethylenepentamine. Reference oil B is a neutral petroleum oil of viscosity $118 at 100 F., 25 mM./kg. of calcium carbonate suli'onate dispersant composition containing 2.35 percent calcium, 40 mMJkg. of calcium carbonate-phenate dispersant composition containing 9.25 percent calcium, 15 mMJkg. of zinc dithiophosphate and- 4 percent by weight of polyisobutenyl succinimide of triethylene tetramine. a v
1 Percent by weight of polyoxyethylene in polyoxyalkylene block copolymer, remainder is poiyoxypropylene. i
8 Percent by weight of polyoxyalkylene glycol in composition.
4 Average molecular weight of polyoxyalkylene glycol. v
5 Time to point of inflection (TF1) in minutes, 0.01 N RC1 in aqueous phase in neutralization rate test. V
Table I illustrates the remarkableneduction in neutralization times achieved by-the addition of'even very small percentages of neutralization rate accelerators. Neutralization times for the reference oils containing calcium carbonate dispersed by sulfonates and phenatesis excessive, in spite of the fact that the oils have high alkalinity. The neutralization rate accelerators illustrated in Table I exemplify satisfactorily performing neutralization promoters. In general, neutralization rate accelerators which substantially reduce the TPI relative to that of the reference oil (zero-weight percent of acid neutralization accelerator) are preferred, since reduction in the TPI of better than 50 percent is regarded as evidence that the addition agent will function to help fulfill the objects of this invention. There are, of course, other properties which are needed such as additive compatibility, stability, etc. So far as rust inhibition is concerned, there is strong evidence that while a satisfactory NRT result is not quantitatively predictive of an MS Sequence IIB rust rating, at the very least, the NRT result does tend to correlate with the comparative rust inhibition properties of any two additives, all other factors being kept constant.
Table II illustrates the distinguishing characteristics of the polyoxyalkylene glycols of the present invention. It is clear that preferably the polyoxyalkylene glycol should contain substantially less than 50 percent polyoxyethylene units by weight and should have a molecular weight substantially over 1,000 and preferably substantially over 5,000.
TABLE III Percent Composition 1 additive i AER B l Lubricating oil compositions containing at least 25mM./kg. oi calcium carbonate-sulfonate dispersant composition containing 2.35 percent calcium (0, D, F), at least 25 mM./kg. of calcium carbonatephenate dispersant composition containing 9.25 percent calcium, mM./kg. of zincdithiophosphate, at least 4 percent by weight of polyisobutenyl succinimide of triethylene tetramine (C, D), 3 percent by weight of polyisobutenyl succinimide of tetra ethylene pentamine (E) and 3.3% by weight of polyisobutenyl amine (F).
2 Percent of polyoxyalkylene glycol neutralization rate accelerator of Example 2 added to lubricating oil composition.
3 Average engine rust in the sequence IIB engine test.
Other test results show, for example, that the lubricating oil composition of Example 2 gives a satisfactorily clean diesel engine after several hours of running, and also gives a rust rating of 9.2 in the MS Sequence IIB engine rust test (GM specifications require an average engine rust rating of 8.9 to pass the MS Sequence IIB test). Table III illustrates the excellent IIB Average Engine Rust ratings (AER) obtainable from the combination of dispersed alkaline earth metal carbonate and polyoxyalkylene glycol and its derivatives in a lubricating composition. The aforementioned table illustrates that the carbonate alone i insufiicient to retard rust forma tion to the degree desired, although the absence of acid neutralizing carbonate would, of course, lead to severe corrosion and rusting.
Finally, the use of the compositions of polyoxyalkylene glycols and their derivatives permits smaller amounts of ash to be introduced into the lubricating oil and therefore avoid problems associated with high ash oils.
What is claimed is:
1. A lubricating oil composition comprising:
a major amount of a hydrocarbon oil of lubricating viscosity;
10 from about 0.01 to 5 weight percent of at least one oil-soluble acid neutralization accelerating amphipathic block copolymer of the formula wherein R and R are ethylene or propylene radicals, a is in the range of 0 to b/5, b is in the range from 10 to 200, and c is in the range from 0 to b/S, such that the total molecular weight of said compound is in excess of 1,000;
and sutficient alkaline earth metal carbonate dispersed in said hydrocarbon oil, with a dispersant selected from the group consisting of phenates and sulfonates, to provide an alkalinity value of from 0.5 to mg. KOH/ g.
2. A lubricating oil composition comprising:
a major amount of a hydrocarbon oil of lubricating viscosity; from about 0.01 to 5 weight percent of an amphipathic oil-soluble acid neutralization accelerating composition which is the reaction product of a polyoxyalkylene glycol having a molecular weight in the range from 1,000 to 10,000 with an organic isocyanate;
and sufficient alkaline earth metal carbonate dispersed in said hydrocarbon oil, with a dispersant selected from the group consisting of phenates and sulfonates, to provide an alkalinity value of from 0.5 to 100 mg. KOH/ g.
3. A composition according to claim 1 wherein said alkaline earth metal carbonate is calcium carbonate.
4. A composition according to claim 3 wherein said dispersant is a sulfonate dispersant derived from a sulfonic acid of from 25 to 50 carbon atoms.
5. A composition according to claim 3 wherein said dispersant is a phenate derived from alkylated phenol or polymerized alkylated phenols having 2 to 5 phenol groups per molecule and an alkyl group of from 12 to 30 carbon atoms.
6. A composition according to claim 2 wherein said alkaline earth metal carbonate is calcium carbonate.
7. A composition according to claim 6 wherein said dispersant is a sulfonate dispersant derived from a sulfonic acid of from 25 to 50 carbon atoms.
8. A composition according to claim 6 wherein said dispersant is a phenate derived from alkylated phenol or polymerized alkylated phenols having 2 to 5 phenol groups per molecule and an alkyl group of from 12 to 30 carbon atoms.
References Cited UNITED STATES PATENTS 3,004,917 10/1961 Fefer 25233.4 2,620,302 12/1952 Harle 25233.6 2,674,619 4/1954 Lunsted 25233.4 2,964,473 12/1960 Hughes et al 25233.4 3,404,092 10/1968 Jacobson et a1. 25251.5 R 2,879,230 3/1959 Newman et al. 2525l.5 A 3,368,971 2/1968 Retzloif et al. 25233.4
DANIEL E. WYMAN, Primary Examiner I. VAUGHN, Assistant Examiner US. Cl. X.R.
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US2833717A (en) * 1956-03-16 1958-05-06 Standard Oil Co Corrosion inhibiting lubricating oil
US2964473A (en) * 1956-12-24 1960-12-13 Standard Oil Co Additive for minimizing cold sludge formation and lubricating oil containing the same
US3368971A (en) * 1965-11-22 1968-02-13 Ethyl Corp Lubricating oil compositions
US3711406A (en) * 1970-06-11 1973-01-16 Chevron Res Lubricating oil containing an hydroxylated amine and an overbased sulfonate or phenate

Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3954915A (en) * 1973-08-13 1976-05-04 Mobil Oil Corporation Block copolymers of hydrogenated diene-styrene with polymerized alkylene oxide and alkylene sulfide
US3867295A (en) * 1973-08-13 1975-02-18 Mobil Oil Corp Block copolymers and lubricant compositions containing the same
US3915872A (en) * 1974-08-08 1975-10-28 Emery Industries Inc Conversion of distillation residues to useful metal working lubricants
US4501616A (en) * 1979-06-26 1985-02-26 Th. Goldschmidt Ag Lubricant and mold-release agent for the manufacture of ties
US4487658A (en) * 1980-12-23 1984-12-11 Agip Petroli S.P.A Aqueous neutralizing and lubricating composition for diesel engines
US4438005A (en) 1981-01-12 1984-03-20 Texaco Inc. Marine diesel engine lubricant of improved spreadability
US4402845A (en) * 1981-05-26 1983-09-06 Texaco Inc. Process for improving the spreadability of marine diesel cylinder oils
US4758247A (en) * 1987-01-02 1988-07-19 Texaco Inc. Novel sarcosine-polyol reaction product and deposit-inhibited motor fuel composition
US5250203A (en) * 1987-02-27 1993-10-05 The Lubrizol Corporation Lubricating oil compositions containing a polyoxyalkylene carboxylic acid salt additive
US4784781A (en) * 1987-02-27 1988-11-15 The Lubrizol Corporation Lubricating oil compositions containing multi-functional additive component
US4954273A (en) * 1987-02-27 1990-09-04 The Lubrizol Corporation Oil formulations containing overbased multi-functional additive
US5037570A (en) * 1989-06-02 1991-08-06 E. I. Du Pont De Nemours And Company Refrigeration compositions and process for using
US5248431A (en) * 1990-02-06 1993-09-28 Dai-Ichi Kogyo Keiyaku Co., Ltd. Metal working lubricating composition
US5171462A (en) * 1991-12-23 1992-12-15 Texaco Inc. Mixtures of polyoxyalkylene ester and aminopolyazoles as oxidation and corrosion resistant lubricant additives
US20110101280A1 (en) * 2008-05-27 2011-05-05 Tadaaki Motoyama Rust preventive oil composition
US9080123B2 (en) * 2008-05-27 2015-07-14 Jx Nippon Oil & Energy Corporation Rust preventive oil composition
US20110034359A1 (en) * 2009-08-07 2011-02-10 Rabbat Philippe Marc Andre Lubricant composition
US8802605B2 (en) 2009-08-07 2014-08-12 Basf Se Lubricant composition
US9340745B2 (en) 2009-08-07 2016-05-17 Basf Se Lubricant composition
US8802606B2 (en) 2010-08-06 2014-08-12 Basf Se Lubricant composition having improved antiwear properties

Also Published As

Publication number Publication date
FR2094182B1 (en) 1975-08-22
FR2166380A2 (en) 1973-08-17
GB1347914A (en) 1974-02-27
DE2263366A1 (en) 1973-07-12
US3856687A (en) 1974-12-24
US3711406A (en) 1973-01-16
DE2263366B2 (en) 1979-01-18
DE2128655A1 (en) 1971-12-16
DE2263366C3 (en) 1979-09-20
FR2094182A1 (en) 1972-02-04
US3933662A (en) 1976-01-20
CA984371A (en) 1976-02-24
GB1399991A (en) 1975-07-02

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