AU613451B2 - Mixtures of partial fatty acid esters of polyhydric alcohols and sulfurized compositions, and use as lubricant additives - Google Patents

Description

PCT

DPI DATE 11/08/89 E. ".00 /19 PCT" NUMBE C TaI i S LliE 1 .T) INTERNATIONAL APPL AOJP DATE 07/09/89 (51) International Patent Classificatizn 4:(1)I ClOM 141/08, 135/02, C07C 149/00 Al (43) 11 nternational Publication Number: iternational Publication Date: WO 89/ 06683 27 July 1989 (27.07,89) (21) International Application Number: JPCT/US88/04661 (22) International Filing Date: 22 December 1988 (22.12.88) (31) Priority Application Number: 144,361 (32) Priority Date: 15 January 1988 (15.01.88) (33) Priority Country: us (71) Applicant: THE LUBR140L CORPORATION [US/ US]; 29400 Lakeland Boulevard, Wickliffe, OH4 44092

(US).

(72 Ivenor: 'SCHWIND, James, Jay 36628 Valley Yv'qw Drive, Eastlake, OH 44094 (US).

(74) Agents: FISCHER, Joseph, P. et al.; The Lubrizol Cor, poration, 29400 Lakeland Boulevard, Wickliffe, OH 44092 (US), (81) Designited States: AT (European patent), AU, BE (European patent), CH (European patent), DE (European patent), FR (European patent), GB (European patent), IT (European patent), JP, LU (European patent), NL (European patent), SE (European patent).

Published With international search report, (54)Title: MIXTURES OF PARTIAL F'ATTY ACID ESTERS OF POLYHYDRIC ALCOHOLS AND SULFURIZE1) C~OMPOSITIONS, AND USE AS LUBRICANT ADDITIVES (57) Abstract Mbitures of partial fatty acid esters- of polyhydric alcohols and sulfurized compositions. Compositions compr!81ng these mixtures are useful as additives for a wide Variety of lubricants, No Legalization No Corporate Seal DECLARED AT Wickliffe, Ohio, U.S.A.

this day of July__ 19 89 G. R. Hill Signature of Declarant Senior Vice President To: The Commissioner of Patents.

a WO 89/06683 PCT/US88/04661 I MIXTURES OF PARTIAL FATTY ACID ESTERS OF POLYHYDRIC ALCOHOLS AND SULFURIZED COMPOSITIONS, AND USE AS LUBRICANT ADDITIVES FIELD OF THE INVENTION This invention relates to compositions which comprise mixtures of at least one partial fatty acid ester of a polyhydric alcohol and particular sulfurized compositions.

These compositions are useful as additives for lubricating oils. Lubricating oil compositions containing such mixtures are also contemplated.

BACKGROUND OF THE INVENTION In the past, sulfurized sperm oil was widely used as an additive in many lubricant formulations such as in gear oil, worm, and sput gears, automatic transmission fluids, metal-working, lubricants and the like. Sulfurized sperm oil is especially useful for improving extreme pressure properties while providing excellent lubricity and some degree of rust-inhibition in motor oils, gear lubricants, and rolling oils. However, the sulfurized sperm oils have been replaced in recent years by other sulfurized compositions as a result of the reduction in availability of sperm oil and increased cost. Sulfurized olefins do not WO 89/06683 PCT/US88/04661 2 always exhibit the degree of lubricity which is necessary in many applications.

Habiby, in U.S. patents 3,926,822 and 3,953,347, describes a composition comprising a sulfurized mixture of a fatty acid ester of a mono- or polyhydric alcohol, a fatty acid and an aliphatic olefin. Newingham et al, in U.S. patents 3,825,495 and 4,180,466, teaches lubrication of controlled-slip differentials with a composition comprising a cosulfurized blend of a triglyceride and a monoolefin. Recchuite, in a series of U.S. patents, for example, U.S. patent numbers 4,166,796, U.S. 4,166,797, U.S. 4,321,153 and U.S. 4,456,540 teaches compositions comprising a cosulfurized mixture of triglycerides and an olefinic hydrocarbon. The '540 patent also recites the presence of a fatty acid in the reaction mixture. in U.S.

4,166,795, Recchuite teaches the reaction product of sulfur, lard oil, polyisobutylene oligomers and optionally another unsaturated material. All of these patents describe the use of these sulfurized mixtures in lubricants. Other sulfurized fatty acid esters are described in Lincoln et al, U.S. 2,113,811; Wasson et al, U.S.

2,672,444; Eby, U.S. 2,680,718; Wakim, U.S. 3,986,966; Zipf, U.S. 4,036,769; Hotten, U.S. 4,053,427; and J0ackisch, U.S. 4,176,072 and in PCT Publication W086/06371.

Numerous patents describe the use of various partial esters of polyhydric alcohols as friction modifiers, emulsifiers, lubricity agents and corrosion inhibitors.

These include Adams et al 2,268,234), Schwartz (U.S.

2,412,633), Barnum 2,564,423), Adelson et al (U.S.

2,628,941), Wasson et al 2,672,444), Bondi et al 2,788,326), Wisotsky 4,505,829) and U.K.

Patent Application 2,038,355.

SUMMARY OF THE INVENTION It has now been found that lubricants comprising a partial fatty acid ester of a polyhydric alcohol and a WO 89/06683 PCT/US88/04661 3 cosulfurized mixture of 2 or more reactants selected from the group consisting of at least one fatty acid ester of a polyhydric alcohol, at least one fatty acid, (3) at least one olefin, and at least one fatty acid ester of a monohydric alcohol, provide a synergistic benefit.

Described are compositions comprising a partial fatty acid ester of a polyhydric alcohol and a cosulfurized mixture of 2 or more reactants selected from the group consisting of at least one fatty acid ester of a polyhydric alcohol, at least one fatty acid, at least one olefin, and at least one fatty acid ester of a monohydric alcohol.

The compositions of this invention are useful as additives for lubricating oil compositions providing extreme, pressure, antiwear, antioxidant and increased lubricity properties to the lubricating oil compositions.

Thus, it is an object of this invention to provide novel compositions. A further object is to provide useful lubricant additives. Another object is to provide lubricating oil compositions. Other objects will be apparent to those skilled in the art upon reading this disclosure or are described in detail hereinbelow.

DETAILED DESCRIPTION OF THE INVENTION As previously described, this invention relates to compositions comprising a mixture of a partial fatty acid ester of a polyhydric alcohol and a cosulfurized mixture of two or more specified reactants.

Component the partial fatty acid ester of a polyhydric alcohol, contains at least one hydroxyl group in the alcohol portion of the ester; that is, not all of the hydroxyl groups of the polyhydric alcohol are converted to ester groups.

WO 89/06683 PCT/US88/04661 4- Suitable partial fatty acid esters of polyhydric alcohols are known and include, for example, glycol monoesters, glycerol mono- and diesters, and pentaerythritol di- and/or triesters. Partial fatty acid esters of glycerol are preferred. Of the glycerol esters, monoesters are preferred; that is, only one of the hydroxyl groups of a glycerol moiety is converted to an ester group, Partial fatty acid esters of polyhydric alcohols can be prepared by methods well known in the art, such as direct esterification of an acid arnd a polyol, reaction of a fatty acid with an epoxide, etc.

While it is possible to prepare the partial esters useful as component of this invention employing any of a variety of methods, they may, in a general sense, be considered as having been prepared from the reaction of a fatty acid and a polyhydric alcohol. Thus, the partial esters contain a moiety which can be considered as being derived from a fatty acid and a moiety which can be considered as being derived from a polyhydric alcohol.

Suitable compositions of this invention can be prepared when component is a saturated material, is essentially free of olefinic unsaturation. It is prefered that component contains olefinic unsaturation.

Such olefinic unsaturation usually appears in the acid moiety of the ester.

The term "fatty acid" as used in the specification and claims refers to acids which may be obtained by the hydrolysis of a naturally occurring vegetable or animal fat o oil. These acids usually contain from' 8 to 22 carbon atoms and include, for example, caprylic acid, caproic acid, pamitic acid, stearic acid, oleic acid, linoleic acid, eto. Acids containing 16 to 20 carbon atoms are prefe..red, and those containing 16 to 18 carbon atoms are especially preferred.

As. mentioned hereinabove, it is preferred that component contains olefinic unsaturation, usually in the acid moiety of the ester. Sitable unsaturated acid WO 89/06683 PCT/US88/04661 moieties include those which can be considered as being derived from various fatty alkenoic acids, for example, octenoic acids, tetradecenoic acids and the like. Oleate esters are especially preferred.

Suitable polyhydric alcohols will have from 2 to about 12 carbon atoms, preferably from 2 to about 5 carbon atoms, and from 2 to about 8 hydroxyl groups, preferably 2 Sto about 4 hydroxyl groups, most preferably about 3 hydroxyl groups. Examples of suitable polyhydric alcohols include ethylene glycol, propylene glycol, trimethylene glycol, neopentylene glycol, glycerol, pentaerythritol, etc. Ethylene glycol and glycerol are preferred; glycerol is especially preferred. Polyhydric alcohols containing alkoxy groups, particularly ethoxy groups or propoxy groups, are contemplated.

The partial fatty acid esters may be present as components of a mixture containing a variety of other components. The other components may include unreacted S, fatty acid, fully esterified polyhydric alcohols, and other materials. From the standpoint of economics, it is preferred that the partial fatty acid ester content of such a mixture is at least about 25%, more preferably at least about 50% by weight. In a particular embodiment, the monoester constitutes at least about 30% by weight of such a mixture, more preferably at least about 45% by weight.

As mentioned hereinabove, suitable partial fatty acid esters can be prepared by methods known in the art. One Smethod for preparing monoglycerides of fatty acids from fats and oils is described in Birnbaum, U.S. Patent 2,875,221. This patent teaches a continuous process for reacting glycerol and fats to provide a product having a high proportion of monoglyceride. Furthermore, many glycerol esters are commercially available. Such esters usually contain at least about 30% by weight of the preferred monoester, generally from about 35 to about by weight monoester, about 30 to about 50% by weight WO 89/06683 PCT/US88/04661 19 f l yr WO 89/06683 PCT/US88/04661 6 diester, and the balance, in the aggregate, usually is no more than about 15%, more often less than about 10% by weight of triester, free fatty acid and other components.

Another method for preparing compositions comprising partial fatty acid esters of this invention is described in the following example.

Example 1 A mixture of glycerol oleates is prepared by reacting 882 parts of a high oleic content sunflower oil which comprises about 80% oleic, about 10% linoleic and the balance saturated triglycerides, and which contains less than 1% by weight acidity measured as oleic acid, and 499 parts glycerol in the presence of a catalyst prepared by dissolving KOH in glycerol to yield a material containing about 16.7% by weight alkoxide. The reaction is conducted by heating the mixture to 155 0 C under a nitrogen sparge, then heating under nitrogen, for 13 hours at 155°C. The materials are cooled to less than 100°C; then 9.05 parts

H

3 P0 4 is added to neutralize the catalyst. The neutralized reaction mixture is transferred to a 2-liter separatory funnel. The lower layer is removed and discarded. The upper layer is the product which contains, by analysis, 56.9% by weight glycerol monooleate, 33.3% glycerol dioleate (primarily and 9.8% glyce-ol trioleate.

Repeating the procedure of this example generally provides products containing from about 54-57% by weight glycerol monooleate, about 33-36% by weight of glycerol Sdioleate and about 8-10% by weight glycerol trioleate.

Specific examples of commercially available materials comprising partial fatty acid esters of glycerol include Emery 2421 (Emery Industries, Inc.), Cap City GMO (Capital), DUR-EM 114, DUR-EM GMO, etc. (Durkee Industrial Foods, Inc.) and various materials identified under the mark Mazol GMO (Mazer Chemicals, Inc.) Other partial fatty acid esters of polyhydric alcohols are described in j WO 89/06683 PCT/US88/04661 7 K. S. Markley, Ed., "Fatty Acids", second edition, parts I and, V, Interscience Publishers (1968). Numerous commereially available fatty acid esters of polyhydric alcohols are listed by tradename and manufacturer in the two volumes: McCutcheon's Functional Materials and McCutcheon's Emulsifiers and Detergents, North American and International Editions (1987).

As mentioned hereinabove, the compositions of this invention include a cosulfurized mixture of 2 or more reactants selected from the group described hereinbelow.

Reactant is at least one fatty acid ester of a polyhydric alcohol. Reactant may be the same as, but is preferably different than the partial ester (A) Reactant may be a partial fatty acid ester, a full ester, or a mixture thereof. As in the case for Component these fatty acid esters of polyhydric alcohols may be prepared in a variety of ways known in the art. In the same way as Component reactant also may be considered as being derived from the'reaction of a fatty acid with a polyhydric alcohol. The fatty acids and polyhydric alcohols from which Reactant may be derived are the same as those described herein~, ve for Component These fatty acid esters are also available from commercial sources, including several of those enumerated hereinabove for Component It is preferred that reactant contains a major amount of the fully esterified ester. Particularly preferred is where the fully esterified ester is a triglyceride, especially 4, wherein the acid moiety is derived from oleic acid.

Especially preferred are the fatty oils, that is, naturally occurring esters of glycerol with the above-noted long chain carboxylic acids and synthetic esters of similar structure. Still more preferred are fatty oils derived from unsaturated acids, especially oleic and linoleic, including such naturally occurring animal and vegetable ols such as lard oil, peanut oil, cottonseed oil, soybean oil, corn oil, sunflower seed oil and others. Specially N WO 89/06683 PCT/US88/04661 8 grown sunflowers yield an oil containing high amounts of oleic acid greater than 80% or more by weight of oleic acid). Such sunflower oils are available commercially under the trademark TRISUN from SVO Enterprises Corporation.

Reactant is at least one fatty acid. Thus, reactant may be at least one fatty acid as described hereinabove. It is usually an unsaturated fatty Sacid Vuch as oleic or linoleic acid, and may be a mixture of acids such as is obtained from tall oil or by the hydrolysis of peanut oil, soybean oil or the like.

Reactant is at least one olefin. This olefin is preferably an aliphatic olefin. That is, it is essen- Stially free of aromatic groups such as phenyl groups, naphthyl groups and the like. The olefin usually will contain from about 4 to about 40 carbon atoms, preferably from about 8 to about 36 carbon atoms. Terminal olefins, or alpha-olefins, are preferred, especially those having from 12 to 20 .carbon atoms. Olefins having internal double bonds are also useful. Mixtures of these olefins are commercially available, and such mixtures are contemplated for use in this invention.

Reactant is a fatty acid ester of a monohydric alcohol. Such a fatty acid ester is one which may be considered as being derived from a fatty acid as described hereinabove with an aliphatic monohydric alcohol such as methanol, ethanol, n-propanol, isopropanol, the butanols, etc. Mixtures thereof are also useful. Reactant (4) can be prepared by methods well known in the art. Such fatty acid esters of monohydric alcohols are also commercially available from numerous sources.

As is apparent from the above discussion, Component and the reactants employed to prepare Component (B) contain various hydrocarbon groups such as alkyl or alkenyl groups, alkylene groups, etc. These hydrocarbon groups may contain non-hydrocarbon substituents or heteroatoms, provided such non-hydrocarbon substituents or WO 89/06683 PCT/US88/04661 9 heteroatoms do not significantly detract from the essentially hydrocarbon nature of the hydrocarbon group.

Suitable non-hydrocarbon substituents include, but are not limited to halo groups, such as chlorine, bromine, etc., mercapto groups, alkoxy groups, etc., and the like.

Heteroatoms include, for example, sulfur, oxygen, nitrogen, and the like. Generally, there will be no.more than one non-hydrocarbon group present per 10 carbon atoms in a hydrocarbon group. More preferably no more than one such substituent or heteroatom is present per 20 carbon atoms.

Preferably, the hydrocarbon groups are purely hydrocarbon; that is, they contain carbon and hydrogen, and are essentially free of non-hydrocarbon substituents or heteroatoms.

As mentioned hereinabove, component the cosulfurized mixture of two or more reactants selected from the group consisting of those identified as reactants and is prepared by reacting the mixture of appropriate reactants with a source of sulfur. The mixture to be sulfurized cortains from about to about 90 parts, more often from about 35 to about parts by weight of Reactant or about 0.1 to about parts, more often about 1 to about 5 parts by weight of Reactant or about 10 to about 90 parts, often from about 15 to about 60 parts, more often from about 25 to about 35 parts by weight of Reactant or from about to' about 90 parts, often from about 1 to about parts, more often from about 5 to about 15 parts, by Sweight of reactant The mixture contains at least two members of this group of reactants. In a preferred embodiment, the mixture contains Reactant and at least one other member of the group of reactants identified as reactants and The sulfurization reaction generally is effected at an elevated temperature, often from about 50 to about 350 C, more preferably, at a temperature of from about 100° to about .210 0 C. The reaction is effected with WO 89/06683 'PCT/US88/04661 10 efficient agitation and often in an inert atmosphere such as nitrogen. If any of the reagents are appreciably volatile at the reaction temperature, the reaction vessel may be sealed and maintained under pressure. Although generally not necessary, the reaction may be effected in the presence of an inert solvent such as an alcohol, ether, ester, aliphatic hydrocarbon, halogenated aromatic.

hydrocarbon, etc., which is a liquid within the temperature range employed for the reaction.

The sulfurizing agents useful in the process of the present invention include elemental sulfur, hydrogen sulfide, sulfur halide, sodium sulfide and a mixture of hydrogen sulfide and sulfur or sulfur dioxide, etc.

Preferably, the sulfurizing agent is elemental sulfur. It is frequently advantageous to add the sulfurizing agent portionwise to the mixture of the other reagents. When elemental sulfur is utilized as a sulfurizing agent, the reaction is in some instances exothermic, which can be utilized as a cost-cutting benefit since no, or at least reduced., external heating may be required. The amount of sulfur or sulfurizing agent added to the reaction mixture can be varied over a wide range although the amount included in the reaction mixture should be an amount sufficient to provide a sulfurized product containing the desired amount of sulfur.

Usually, the amount of sulfur or sulfurizing agent employed in the preparation of the sulfurized component (Component B) of this invention is calculated based on the total olefinic unsaturation of the mixture. A monoolefinic reactant, such as an alpha-olefin or oleic acid, for example, contains one mole of olefinic bonds per mole of reactant. A polyolefinic material contains 2 or more moles of olefinic bonds. For example, 1,4-hexadiene contains 2 moles of olefinic bonds. In general, from about 0.01 to about 6 moles of sulfur, present as elemen-J tal sulfur or as sulfur present in another sulfurizing, reactant, may be employed per mole of olefinic bonds..

WO 89/06683 PCT/US88/04661 11 More often from 0.5 to about 3 moles of sulfur are employed per mole of olefinic bonds.

Accordingly, the sulfur content of any given sulfurized composition useful in this invention depends on the amount of sulfur present in the sulfurization mixture and on the nature and amount of the reactants present in the mixture comprising reactants Compositions containing from 2 to about 40 percent by weight sulfur are common and preferred, are those containing from about 5 to about 25 weight percent of sulfur.

The sulfurization reaction may be conducted in the presence of various catalysts such as amines and other catalysts known to assist sulfurization reactions. A number of useful catalysts are described in U.S, 4,191,659 which is expressly incorporated herein by reference for relevant disclosures in this regard.

Following the sulfurization reaction, it is preferred to remove substantially all low boiling materials, typically by venting the reaction vessel, 1by sparging with an inert gas such as nitrogen, by vacuum distillation or stripping, etc. Insoluble by-products may be removed by filtration if necessary, usually at an elevated temperature (about 50-120QC).

A further optional step in the preparation of the cosulfurized mixture, is treatment of the sulfurized product obtained as described above to reduce any active sulfur which may be present. An illustrative method involves contacting the sulfurized composition with an alkali metal sulfide, Other optional treatments may be employed to improve product quality such as odor, color, and staining characteristics of the sulfurized compositions.

Exemplary cosulfurized compositions meeting the requirements outlined for Component are described in the patents referred to in the BACKGROUND OF THE INVENTION of this specification, particularly the Habiby, Newingham and Recchuite patents. These patents are hereby expressly WO 89/06683 PCT/US88/04661 12 incorporated herein by reference for relevant disclosures contained therein.

The following examples illustrate the preparation of other sulfurized compositions useful as Component of the present invention. These examples are presented for illustrative purposes only, and are not intended to limit the scope of this invention. Unless otherwise indicated in the examples and elsewhere in the specification and claims, all parts and percentages are by weight, and temperatures are in degrees Celsius.

Example 2 To a 2-liter, 4-necked flask equipped with a stirrer, thermowell, reflux condenser to Dean-Stark trap and a sub-surface sparge tube is charged 330 parts of a mixture of C 16 1 8 alpha-olefins (Ethyl Corporation) and 670 parts of a mixture comprising, by analysis, 56 percent by weight glycerol monooleate (51.5% alpha-onooleate), 40.7% glycerol dioleate and 3.3 percent by weight glycerol trioleate and which has an iodine number of 74.60. The materials are heated, with stirring, to 150° under a nitrogen sparge. The nitrogen sparge is discontinued and 117 parts sulfur are added in two increments, 15 minutes apart. The temperature is increased to 195*C and held at 195-199 0 C for 2 hours. The nitrogen sparge is resumed and heaoing is continued at 195-199 C for 2 hours. The reaction mixture is cooled and filtered through a diatomaceous earth filter aid. The filtrate, containing 9.94s sulfur by analysis, is the product.

Example 3 A 3-liter, 4-necked flask equipped with a stirrer, thermowell, reflux condenser to Dean-Stark trap and sub-surface gas sparge tube is charged with 2000 parts of the glycerol oleate mixture described in Example 2. The material is heatod under a nitrogen sparge to 145 0 C. The nitrogen sparge is discontinued and 116 parts sulfur are ,Tk.

WO 89/06683 PCT/US88/04661 13 1 added in two increments, 20 minutes apart. The mixture is heated to 195 0 C and held at 195 0 C for 2 hours. The nitrogen sparge is resumed and the reaction mixture is held for 3 additional hours at 195 0 C. The reaction mixture is filtered through diatomaceous earth at 75 0

C.

The filtrate, containing 5.40% sulfur by analysis, is the product.

Example 4 Following a procedure essentially the same as that of Example 2, 425 parts of a glycerol oleate mixture comprising about 60% glycerol monooleate (57.1% alpha-monooleate) and having an iodine number of 72.9, 75 parts of a mixture

TM

of C 16 18 alpha-olefins (Neodene TM 16-18, Shell) and 58.7 parts sulfur are reacted yielding a sulfurized product containing 9.85% sulfur by analysis.

Example A 1-liter, 4-necked flask equipped with a stLrrer, thermowell, reflux condenser to Dean-Stark trap and sub-surface gas inlet tube is charged with 75 parts of the C,68 aipha-olefin rmixture of Example 4, 50 parts oleic ae-id (Pamplyn 100) and 375 parts of the glycerol oleate mixture described in Example 4. The mixhure is heated to 1450C, 58.7 parts sulfur are added in two increments, minutes apart, and heating is continued while the temperature increases to 195 0 C. The reetion is continued at 195CC for 1.5 hours followed by an additional 2 hours at 195° with a nitrogen sparge. The materials are filtered at 906C tl.rough a diatomaceous' earth filter aid. The filtrate, containing 9.54% sulfur by analysis, is the product.

Example 6 Following a procedure essentially the same as that for Example 5, 50 parts, of oleic acidt 150 parts of t16-18 alpha-olefin mixture, and 300 parts glycerol oleate WO 89/06683 PCT/US88/04661 14 mixture (each reactant as described in Examples 4 and hereinabove) are reacted with 58.7 parts sulfur yielding a sulfurized material containing 10.05% sulfur by analysis.

Example 7 A 1-liter, 4-necked flask equipped with a stirrer, thermowell, reflux condenser to Dean-Stark trap and a sub-surface gas inlet tube is charged with 45 parts soybean oil, 75 parts of a mixture of C 1 6 -18 alpha-olefins

TM

(Neodene T 16-18, Shell), 50 parts oleic acid (Pamolyn 100) and 330 parts of the glycerol oleate mixture described in Example 4. This mixture is heated to 145 0

C

under a nitrogen sparge. Nitrogen is discontinued, and 58.7 parts sulfur are added in two increments, 15 minutes apart. The materials are heated to 195°C and held at 195°C for 1.5 hours. A nitrogen sparge is resumed and heating is continued at 195 0 C for 2 hours. The reaction mixture is filtered at 95 0 C through a diatomaceous earth filter aid. The filtrate, containing 9.95% sulfur by analysis, is the product.

Example 8 A I-liter, 4-necked flask equipped :ith a stirrer, thermowell, reflux condenser to Dean-Stark trap and a sub-surface gas inlet tube is charged with 75 parts of a mixture of C 16 18 alpha-olefins (Neodene 16-18, Shell), 95 parts soybean oil and 330 parts of the glycerol oleate mixture described in Example 4. This mixture is heated to 145°C under a nitrogen sparge. The nitrogen sparge is Sdisdontinued, and 58.7 parts sulfur is added in two increments, 15 minutes apart. The mixture is heated to 195°C and held at 195 C for 1.5 hours. The nitrogen sparge is resumed and the reaction is continued at 195°C for 2 hours. The mixture is filtered at 90 0 C through a diatomaceous earth filter aid. The filtrate, containing 9.74% sulfur by analysis, is the product.

WO 89/06683 PCT/US88/04661 15 Example 9 Following essentially the same procedure as described in Example 8 and employing ingredients described in that example, 330 parts soybean oil,. 95 parts glycerol oleate mixture and 75 parts C 16 18 alpha-olefin mixture are reacted with 58.7 parts sulfur. The resulting product contains 10.2% sulfur by analysis.

Example The glycerol oleate mixture described in Example 2 is distilled employing a thin-film evaporator at 240 0 -25 0

°C

at 0.25 millimeters mercury pressure. The distillate obtained contains 95.8 percent by weight glycerol monooleate and 4.2 percent by weight glycerol dioleate by analysis. A mixture of 425 parts of this distillate, 425 parts soybean oil and 150 parts of a C 16 1 8 alpha-olefin mixture (Ethyl) is heated to 145°C followed by the addition of 117 parts sulfur in three increments over 0.25 hour. The temperature is increased to 195 0 C and held at 195°C for 1.5 hours. A nitrogen sparge is begun and heating is continued for 2.5 hours at 195 0 C. The reaction mixture is filtered at 75 C through a diatomaceous earth filter aid. The filtrate, containing 9.66% sulfur by analysis, is the product.

Example 11 Following essentially the procedure of Example 190 parts of the glycerol monooleate distillate described in Example 10, 660 parts soybean oil and 150 parts of

SC

16 i- 8 alpha-olefin rmixture 4 (Ethyl) are reacted with 117 parts sulfur. The product obtained contains 9.84% sulfur by analysis.

Example 12 Following essentially the procedure of Example 660 parts of the glycerol oleate distillate described in Example 10, 190 parts soybean oil and 150 parts of C16 1b~18 i' WOd 89/06683 PCT/US88/04661 16 alpha-olefin mixture (Ethyl) are reacted with 117 parts sulfur. The product obtained contain- 9.7% sulfur by analysis.

Example 13 A 2-liter, 4-necked flask equipped with a stirrer, thermowell, reflux condenser and sub-surface sparge tube is charged with 1000 parts soybean cil, 454 parts of a glycerol oleate mixture' prepared according to the procedure of Example 1 and 53 parts oleic acid (Pamolyn 100) The materials are heated to 145 0 C under a nitrogen sparge.

Nitrogen sparging is discontinued, and 176 parts sulfur are added in three increments at 145°C. The mixture is heated to 195°C and held at 195°C for 1.5 hours. Nitrogen sparging is resumed and the reaction is continued at 1950C for 5 hours. The materials are cooled and filtered through a diatomaceous earth filter aid. The filtrate, containing 9.34% sulfur by analysis, is the product.

Example 14 A 2-liter, 4-necked flask equipped with a stirrer, thermowell, reflux condenser and sub-surface gas inlet tube is charged with 500 parts soybean oil, 500 parts of a glycerol oleate mixture prepared according to the procedure of Example 1, 454 parts of a C 1 6 1 8 alpha-olefin mixture (Shell) and 53 parts oleic acid (Pamolyn 100).

The materials are heated to 145°C under a nitrogen sparge.

The nitrogen sparge is then discontinued and 176 parts sulfur are added in three increments over a period of 0.25 hours. The reaction mixture is heated to 195 0 C and held at 195 0 C for 1.5 hours. The nitrogen sparge is resumed and the reaction is continued for 3 hours at 1950C. The reaction mixture is then cooled and filtered through a diatomaceous earth filter aid. The filtrate, containing 9.71% sulfur by analysis, is the product.

WO 89/06683 PCT/US88/04661 17 Example A 2-liter, 4-necked flask equipped with a stirrer, thermowell, reflux condenser to a Dean-Stark trap and a sub-surface sparge tube is charged with 1000 parts sunflower seed oil similar to that used in Example 1, 500 parts of the glycerol oleate mixture described in Example 14 and 53 parts oleic acid (Pamolyn 100). The materials are heated to 145 0 C under a nitrogen sparge, then the nitrogen sparge is discontinued. In three increments, 176 parts sulfur are added at 145°C. The materials are heated to 195 0 C and held at 195 0 C for 1.5 hours. The nitrogen sparge is restarted and the reaction is continued at 195 0

C

for 3 hours. The reaction mixture is cooled and filtered through a diatomaceous earth filter aid. The filtrate, containing 9.25% sulfur by analysis, is the product.

Example 16 Following essentially the same procedure as employed in Example 15, 1000 parts of the glycerol oleate mixture of Example 1, 454 parts of C 1 6_ 8 alpha-olefin mixture (Shell) and 53 parts oleic acid (Pamolyn 100) are reacted with 176 parts sulfur. The product obtained contains 9.40% sulfur by analysis.

Examples 17-24 Examples 2-9 are repeated, replacing the glycerol oleate mixtures with commercial pentaerythritol dioleate described as having an acid number of less than 1.5, a hydroxyl value of 120-130 and an iodine number of 81-87.

Example A mixture of 1000 parts soybean oil, 52.4 parts tall oil fatty acid and 454 parts of a mixture of C 15 1 8 alpha olefin is heated to 138 0 C. To this mixture is added 178 parts sulfur. The mixture is heated to 146°C whereupon an exothermic reaction takes place with the temperature rising to 193 0 C. The reaction is continued for 4 hours WO 89/06683 PCT/US88/04661 18 while the temperature drops to 171 0 C. The materials are blown with nitrogen for 2 hours at 163-170 0 C, then filtered at 93°C. The sulfurized composition contains 10.3% sulfur, by analysis.

Example 26 Following essentially the procedure of Example 1000 parts soybean oil, 464 parts of C15-1 8 alpha olefin and 53.8 parts of tall oil fatty acid are reacted with 247 ,arts sulfur, Example 27 Following essentially the procedure of Example 1000 parts of peanut oil are reacted with 600 parts of

C

16 18 alpha olefin and 175 parts of sulfur.

The following Examples illustrate compositions of this invention. All parts are parts by weight Example Composition I 100 parts glycerol oleate mixture (Emerest 2421) and 100 parts of the sulfurized product of Example II 50 parts Emerest 2421 and 150 parts of the product of Example 7 III 100 parts of the glycerol monooleate containing product of Example 1 and 150 parts of the product of Example IV 50 parts of commercial pentaerythritol dioleate described in Examples 17-24 and 150 parts of the product of Example The compositions of this invention are useful as oil-soluble lubricant additives providing friction modification, anti-wear and extreme pressure performance. They S WO 89/06683 PCT/US88/04661 -19 also impart energy conserving properties to lubricants containing them. Thus, they are useful in automotive lubricants, such as engine oils and drivetrain lubricants, which are intended for use when it is desired to reduce fuel consumption. These energy conserving properties are also useful in industrial applications when it is desired to reduce the power requirements, such as electrical power requirements, and consequently the cost, of operating industrial machinery. Depending on the particular nature of the individual components comprising the compositions, additional benefits such as anti-oxidancy, corrosion inhibition, and the like may be obtained. The compositions of this invention have been shown to improve wear and extreme pressure properties of manual transmission fluids without sacrificing friction i.odification. The lubricating oil compositions of this invention comprise a major amount of an oil of lubricating viscosity and a minor amount of the compositions of this invention. By a major amount is meant more than 50%. Thus, 51%, 80% and "9 99% are major amounts. A minor amount is 'ess than Examples of minor amounts are 25% and 49%. Amounts of the composition of this invention used as additives for lubricating compositions of this invention will, of course, depend in part on whether the composition contains a diluent and on other characteristics of the composition.

The compositions of this invention are used in an effective amount to provide the above-described properties.

Typically, the compositions of this invention are employed in an oil of lubricating viscosity in amounts, on a neat 30 chemical basis, ranging from about 0.1 to about 20% by weight of the composition in the lubricating oil composition. More often, the composition is used at about 0.25 to about 10%o, preferably from about 0.5 to about 5% by weight of the lubricating oil composition.

The lubricating oil compositions may be prepared by dissolving or suspending the compositions of this invention, and any other additives which may be desired, WO 89/06683 PCT/US88/04661 directly into the base oil. More often, the composition of this invention is a component of an additive concentrate which may contain other additives -and which often contains an inert organic diluent. Such additive concentrates usually comprise from about 1 to about 90% by weight of the compositions of this invention. Alternatively, Components and may be added individually, with or without other additives, as desired, to an oil of lubricating viscosity in order to prepare lubricating composition of this invention.

Component and Component may be incorporated over a wide range of proportions into the compositions of this invention. Preferably, the compositions of this invention contain Component and Component in weight ratios of to ranging irom about 0.05 to to about 5 to 0.1, more preferably from about 0.25 to 2 to about 2 to 0.25.

Ccrqponent is generally present in the lubricating oil compositions of this invention in amount ranging from about 0.0005 to about 20 percent by weight, preferably from about 0.25 to aboiit 10, more preferably from about to about 2 percent by weight. Component is generally present in amounts ranging from about 0.01 to about 20 percent by weight, preferably from about 0.1 to about 5e more preferably from about 0.25 to about 2 perc~ent by weight. Often, Component constitutes from~ about 10 to about 90% by weight of the compositions of this invention. Accordinglyj component often constitutes from about 90; to about 10% by weight of the composition. Frequenty Component and,\ Component are used in approximately equal weight propotions.

The lubricating compositions of thisineto mpv an oil of lubricating viscosity, in~cluding natural or synthetic lubricating oils and mixtures thereof.

'Natural oils include animal oils and vegetable oils castor oil, lard oil) as well as r-neral lubricating A oils such as liquid petroleum oils and solvent-treated or WO 89/06683 PCUS8804661 21 acid-treated mineral lubricating oils of the paraffinic, naphthenic or mixed paraffinic-naphthenic types. Oils of lubricating viscosity derived from coal or shale are also useful. Synthetic lubricating oils include hydrocarbon oils and halosubstituted hydrocarbon oils such as polymerized and interpolymerized olefins, etc. and mixtures thereof, alkylbenzenes, polyphenyl biphenyls, terphenyls, alkylated polyphenyls, etc.), alkylated diphenyl ethers and alkylated diphenyl sulfides and the derivatives, analogs and homologs thereof and the like.

Alkylene oxide polymers and interpolymers and derivatives thereof where the terminal hydroxy, groups have been modified by esterification, etherification, etc., constitute another class of known synthetic lubricating oils that can be used.

Another suitable class of synthetic lubricating oils that can be used comprises the esters of dicarboxylic acids and those made from C to C 12 monocarboxylic acids and polyols and polyol ethers.

Other synthetic lubricating oils include liquid esters of phosphorus-containing acids, polymeric tetrahydrofurans and the like, silicon-based oils such as the polyalkyl-, polyaryl-, polyalkoxy-, or polyaryloxyoiloxane oils and silicate oils.

Unrefined, refined and rerefined oils, either natural or synthetic (as "ell as mixtures of two or more of any of these) of the type disclosed hereinabove can be used in the lubricating compositions of the, present invention.

Unrefined oils are those obtained directly from a natural or synthetic source without further purification treatment. Refined oils are similar to the unrefined oils except they have been treated in one or more purification steps to improve one or more properties. Rerefined oils are obtained by processes similar to those used to obtain refined oils applied to refined oils which have been already used in service. Such rerefined oils often are I ~rr II I WO 89/06683 PCT/US88/04661 22 additionally processed by techniques directed to removal of spent additives and oil breakdown products.

Specific examples of the above-described oils of lubricating viscosity are given in Chamberlin III, U.S.

4,326,972 and European Patent Publication 107,282, both of which are hereby incorporated by reference for relevant disclosures contained therein.

A basic, brief description of lubricant base oils appears in an article by D. V. Brock, "Lubrication Engineering", Volume 43, pages 184-5, March, 1987, which article is expressly incorporated by reference for relevant disclosures contained therein.

Other Additives As mentioned, the compositions, additive concentrates and lubricating compositions of this invention may contain other additives. The use of such additives is optional, and the presence thereof in the compositions, additive concentrates and lubricating compositions of this invention will depend on the particular use and level of performance required. One optional additive is a zinc salt of a dithiophosphoric acid. Zinc salts of dithiophosphoric acids are often referred to as zinc dithiophosphates, zinc 0,0-dihydrocarbyl dithiophosphates, and by other commonly used names. They are sometimes referred to by the abbreviation ZDP. One or more zine salts of dithiophosphoric acids may be present in a minor amount to provide additional extreme pressure, anti-wear and anti-oxidancy properties.

SIn addition to zinc salts of dithiophosphoric acids discussed hereinabove, other additives that may optionally be used in the compositions, additive concentrates and lubrictiAg compositions of this invention include, for example, detergents, dispersants, viscosity improvers, oxidation inhibiting agents, pour point depressing agents, extreme pressure agents, anti-wear agents, color stabilizers and anti-foam agents.

WO 89/06683 PCT/US88/04661 23 Auxiliary extreme pressure agents and corrosion and oxidation inhibiting agents are exemplified by chlorinated aliphatic hydrocarbons, organic sulfides and polysulfides, phosphorus esters including dihydrocarbon and trihydrocarbon phosphites, molybdenum compounds, and the like, Viscosity improvers (also sometimes referred to as viscosity index improvers) are usually polymers, including polyisobutenes, polymethacrylic acid esters, diene polymers, polyalkyl styrenes, alkenylarene-conjugcated diene copolymers and polyolefins. Multifunctional viscosity improvers which also have dispersant and/or antioxidancy properties are known and may optionally be used.

Pour point depressants are a particularly useful type of additive. See for example, page 8 of "Lubricant Additives" by C, V. Smalheer and R. Kennedy Smith (Lezius-Hiles Company Publishers, Cleveland, Ohio, 1967).

Pour point depressants useful for the ,purpose of this invention, techniques for their preparation and their use are described in U.S. Patent numbers 2,387,501; 2,015,748; 2,655,479; 1,815,022; 2,191,498; 2,666,748; 2,721,877; 2,721,878; and 3,250,715 which are expressly incorporated by reference for their relevant disclosures.

Anti-foam agents used to keduce or prevent the formation of stable foam include silicones or organic polymers. Examples of these and additional anti-foam compositions are described in "Foam Control Agents", by Henry T. Kerner (Noyes Data Corporation, 1976) pages 125-162.

Detergents and dispersants may be of the ash-producing or ashless type. The ash-producing detergents are exemplified by :il soluble neutral and basic salts of alkali or alkaline earth metals with sulfonic acids, carboxylic acids, phenols or organic phosphorus acids characterized by at least one direct carbon-to-phosphorus linkage.

~,r..lrl WO 89/06683 PCT/U$8/04661 24 The term 'basic salt" is used to designate metal salts wherein the metal is present in stoichiometrically larger amounts than the organic acid radical. Basic salts and techniques for preparing and using them are well known to those skilled in the art and need not be discussed in detail here.

Ashless detergents and dispersants are so-called despite the fact that, depending on its constitution, the detergent or dcrspersant may upon combustion yield a non-volatile residue such as boric oxide or phosphorus pentoxide; however, it does not ordinarily contain metal and therefore does not yield a metal-contaiining ash on combustion. Many types are known in the art, and any of them are suitable for use in the lubricants of this invention. The following are illustrative: Reaction products of carboxylic acids (or derivatives thereof) containing at least about 34 and preferably at least about 54 carbon atoms with nitrogen containing compounds such as amine, 'organic hydroxy compounds such as phenols and alcohols, and/or basic inorganic materials. Examples of these "carboxylic dispersants" are described in British Patent number 1,306,529 and in many U.S. patents including the following: r1 WO 89/06683 PCT/US88/04661 25 3,163,603 3,184,474 3,215,707 3,219,666 3,271,310 3,272,746 3,281,357 3,306,908 3,311,558 3,316,177 3,340,281 3,341,542 3,346,493 3,351,552 3,381,022 3,399,141 3,415,750 3,433,744 3,444,170 3,448,048 3,448,049 3,451,933 3,454,607 3,467,668 3,501,405 3,522,179 3,541,012 3,541,678 3,542,680 3,567,637 3,574,101 3,576,743 3,630,904 3,632,510 3,632,511 3,697,428 3,725,441 4,194,886 4,234,435 4,491,527 RF, 26,433 Reaction products of relatively high molecular weight aliphatic or alicyclic halides with amines, preferably polyalkylene polyamines, These may be characterized as "amine dispersants" and examples thereof are described fqr example, in the following U.S. patents: 3,275,554 3,438,757 3,454,555 3,565,804 Reaction products of alkyl phenols in which the alkyl groups contains at least about 30 carbon atoms with aldehydes (especially formaldehyde) and amines (especially polyalkylene polyamines), which may be characterized as "Mannich dispersants". The materials described in the following U.S. patents are illustrative: 3,413,347 3,697,574 3,725,277 3,725,480 3,726,882

I

WO 89/06683 PCT/US88/04661 26 Products obtained by post-treating the carboxylic amine or Mannich dispersants with such reagents as urea, thiourea, carbon disulfide, aldehydes, ketones, carboxylic acids, hydrocarbon-substituted succinic anhydrides, nitriles, epoxides, boron compounds, phosphorus compounds or the like. Exemplary materials of this kind are described in the following U.S. patents: 3,036,003 3,087t936 3,200,107 3,216,936 3,254,025 3,256,185 3,278,550 3,280,234 3, 2$11 428 3,282,955 3,312,619 3,366,569 3,367,943 3r ,373 111 3,403,102 314 2,808 3,455,831 3,455,832 3,493,520 3,502r677 3,513,093 31533,945 3,539,633 3,573,010 3,579,450 3,591,598 31600,372 3,639,242 3,649,229 3,649,659 3,658,836 3,697,574 3,702,757 3 ,03,536 3,704,308 3,708,522 4f234,435 Interpolpyters of oil-solubilizing monomers such as decyl. methaorylato, vinyl decyl ether and high molecular weight olefins with monomers containding polar substituents, e-go, aninoalkyl acryJlates or inethacrylatse acrylamides and poly~- (oyethylene) -substituited acrylates.

These may be characterized as "PolYmeric dispersants" and examples thereof are disclosed in the following U.S.

patentq4 4 3,32,9,58 3,449,250 315191$65 3 66, 730 3,687,849 3,702,300 The, above-noted, patents are incotpo:rated by reference herein for their disclosures o4 ashleos dizpe-rsants.

The above- i lus trated additives may each be present in lubricating compositions at a concentration of as li\.tle as 0.001% by weight usUally ranging from about WO 89/06683 PCT/US88/O4661 -27 Q. 01% ab o 1t0 20% by weight. In most instances, they e a a, present at fropi about 0.1% to, about 10% by weight.

The various additives and compositions described herein can be added directly to the ,Lubricating oil.

Prefecably, however, thney are diluted with a substantially inert, normally liquid organic diluent such as mineral oil, napj'thaj benzene, toluenip or :Kylene, to form an additive conp~entrate. Theso additive concentrates usually comprise abc~it 1 to about 9O% by weight of the compositions of this invention and may coatain,~ in addition, one or ,(ore other additives kno~wn ir, the art or described herexnabove. Chemjii<~vil concent:ration- such as 209., o.i 50~% ot. higher may be employed, The lilbricating compositions of this invention find -'ti2ity in many areas. Ex~mple; includ~e, but are not limited to, lubricants for internal combustion engines, especiall2y fuel economy improving oils, power transmission fluids such as automatic transmission fluids, hydraulic fluids, power shift, oils and tractor oils. Tractor oils 2O frequ~ently serve multiple parposes c.uch as hydraulic fluids, wet brake lubricant,., engine lubricants, etc., all employing a lubricant from a ccmxnon sump. Other areas of application incdlude industrial applications such as metal-working fluids and industrial gear oils. ~'e compositions of this inve~itlon also find utility in various aqueous systems s'ueh as are de~cribed by 7'orsberg in U.S. 40f29,4A29, 4,368,133, U.S. 4,448,703, and i~n other aqueous, compositions.

Typicail additiVe concentrates and 1ubrit 4ating oil ,,re~re by ombningthespecfie ing-,eien s, dividuoi," ofIt.I~rcatng iscsit tomak 'te ttal100pa-ts by we4,ght. 'The amounts shown are parts by weight and, unlass indicated otherwise, are amounts of chem.cal prse~ton ain oil-fe ~s thus, for example, n WO 89/06683 PCT/US88/04661 28 additive comprising 50% oil used at 10% by weight in a blend, provides 5% by weight of chemical. These examples are presented for illustrative purposes only, and are not intended to limit the scope of this invention.

I-

Table 1:

A

Lubricating Oil Compositions ExamnplIe Parts by B C Weight

D

Farm Tractor

E

Farm Tractor Lubricant type: Gear Gear Farm Tractor Mineral oil basestock SAE 80W (Texaco) SAE 8OW (SIPCO) Sun Tulsa J20B (Sun Oil) Balance Balance Balance Balance Balance Ingredient Alkylated benzene Acrylate polymer viscosity improver (Texaco TC 10124) Amine treated styrenealkyl maleate copolymer Silicone Antifoam (Mixture with hydrocarbopn solvent) zinc salt- zf mixed alkyl carboxylic acid--dialkyl phosphorodith joate Reaction product of N,N-dialkylalkanol amine with 'polyisobutenyl succini c anhydride ,Basic calcium sulfonate, 0.4 0-~02 2.12 0-31 0,4 0 .01 2.12 0.31 2 .03 0.02 2.12 0.31 2 .03 0.02 2.12 0.31 2.03 0 .02 1.-87 0.30- 1.43 1.43 1.43 1.43 17 1.72 Table 1: Lubricating Oil Compositions (continued) Parts by Weight A B C D Example Ingredient Basic borated alkali metal sulfonate Product of Example 25 Fatty oil containing glycerol monooleate (EmerE st 2421) 0 .75 0.50 0.50 0.75 0.50 0.50 0.38 0.50 0.50

E

0.75 0.50 0.50 0.50 0.50 0 Table II: Lubricating Oil Compositions 00 Example F G Lubricant type: ATF ATF MiLieral oil basestock 100 Neutral Oil (CitCon) Balance Balance Ingredient Alkylated benzene 5.0 Amine treated styrene- 1.98 1.98 alkyl maleate copolymer Silicone Antifoam 0.042 0.042 Product of Example 25 0.50 0.50 Fatty oil containing 0.70 0.3 glycerol monooleate (Emerest-24121) CS 2 post-treated polyisobutenyl 1.45 1.16 succinic, 4ahydride-ethylene polyamine reaction product 00~ 00

LIN

Table II: Lubricating Oil Compositions (continued)0 Parts by Weight Exawinple F G 00 Ingredient Borated polyisobutenyl succinic 0.34 0.67 anhydride-ethylene polyamine reaction product Sodium petroleum sulfonate 0.54 0.54 Alkylated diphenylamine 0.08 0.08 Alkyl, thio alkanol, 0,.5 Dibutyl phosphite 0.11 0.11 Zinc salt of di (sec-alkyl) 0.06 0.06 dithiophosphate Ethoxylated fatty amine 0.1 Alkylated naphithalene 0.2 0.2 Mercaptobenzothiazole 0.025 0.025 Di-fatty alkyiphosphite, 0.3 00 00 00 Table III: Additive Concentrates 0 00 %0 L 0

LW

Example: Parts H I by Weight J K Ingredient Diluent Oil Zinc salt of alkyl carboxylic acid-dialkyl phosphorodithioate mixture Fatty oil containing 65% glycerol monoleate (Emerest 2421) Product of Example 25, Reaction product of N,Ndialkyl alkanolamine with polyisobutenyl succinic anhydride Basic calcium sulfonate Borated basic alkali metal sulfonate

CS

2 post-treated polyisobutenyl succinic anhydride-ethylene polyamine reaction.product Balance Balance Balance Balance Balance 27.51 31.61 6.49 6.49 1.82 3.03 7.46 7.46 4.63 29.42 6.94 6.94 4.31 23.36 6.25 6.25 3.75 21.45 9.38 4.03 18.57 21.35 9.74 5.23 7.03 4s Table III: Additive Concentrates (continued) Parts by Weight H I J K L Example: Ingredient Borated polyisobutenyl anhydride-ethylene polyamine reaction product Sodium petroleum sulfonate Alkylated diphenyl amine Alkylthio alkanol Dibutyl phosphite Zinc salt of di(secondary alkyl) dithiophosphate Ethoxylated f atty amine Alkyla ted nap~hthalene Di-fattv alkyl phosphite Alkylated benzene Amine-treated styrene-inaleate, copolymer 4.06 3.27 0.51 3.03 0.67 0.38 1.21 1.82 30.30 11.9 WO 89/06683 PCT/US88/04661 S- 35 As noted hereinabove, lubricating compositions comprising Components and display unexpectedly enhanced performance compared to lubricating, compositions comprising either Component or Component (B) individually.

The unexpected benefits provided by the compositions of this invention are illustrated by the test results presented below. The Timken test is a well-known procedure used to determine the load-carrying ability of a lubricant. It is described in the American Society for Testing and Material procedure ASTM D-2782-77.

Gear lubricants are prepared from an SAE basestock (Texaco) to which is added 15% of an alkylated benzene, 10% of an acrylate polymer viscosity improver (Texaco TC10124), 0.4% of an amine treated styrene-alkyl maleate copolymer, 100 ppm of a silicone antifoam and an additive concentrate contributing a mineral oil diluent, 2.12% of a zinc salt of an alkyl carboxylic acid-dialkyl phosphorodithioate mixture, 0.31% of the reaction product of a N,N-dialkyl alkanolamine with polyisobutenyl succinic anhydride, 1.43% of basic calcium sulfonate, 0.75% of basic borated alkali metal sulfonate, and the additives listed below: Timken (ASTM-2782)

OK

Example Additive Load PSI M 1% of product of 55 lb. 32,850 psi Example 25, 60 lb. 35,825 psi N 1% of commercial 13' lb. 8,775 psi glycerol monooleate 13 lb. 8,250 psi (Emerest 2421-Emery) additional 0.52% basic calcium sulfonate A 0.50% of product of 65 lb. 34,725 psi Example 25, 65 lb. 34,725 psi 0.50% Sf Emerest 2421 The instant invention is shown and described herein in what is considered to be the most practical, and the i i -i i 1_ -I- WO 89/06683 PCT/US88/04661 36 preferred embodiments. It is recognized, however, that departures may be made therefrom which are within the scope of the invention, and that obvious modifications will occur to one skilled in the art upon reading this disclosure.

tr

Claims (1)

1. 2. 17. The cormposition of cJ.a.im 14 wherein componrent 2 comprises a cosulfurizec mixture comprising 3 from 10 to abH 90 parts by weight 4 of at least one fatty acid ester of a polyhydric alcohol, and 6 from -ab4 15 to a4l i-t--60 parts by weight 7 of at least one olefin. 1 18. The composition of claim 14 wherein compciieit 2 comprises a cosulfurized mixture comprising fro-" I to "Gw-t- 5 parts by weight of 4 at least one fatty acid. from 1* 15 to e- 60 parts by weight 6 of at least one olefin. 1 19i The composition of claiim 14 wherein component 2 comprises a cosult:2urized mit:;ure comprising 3 from &bou-20 to -404- 60 Parts by weight 4 of at least one ol.efin, and from Abvwt-1 to a4 90 parts by weight 6 of at least onre fatty acid ester qvf a monohydric alcohol, 1 20. The compositioni of claim 14 wherein component 2 (f3) oompr-ies a cosulfuriZed Mixture comprising 3 from eA-u 3$ to 4be** 65 parts by weight 4 of at' Jleast, one fatty acid e rtr of a polyhydric alcohol, from, I 1 to A-u4-5 parts by weight of 6 at least Oo fatty acid, and 7 from -bi 15 to o4~ewt 60 parts by wcliqht 8 0! at least one olofini WO 89/06683 PCT/US88/04661 1 21. The composition of claim 14 wherein component 2 comprises a cosulfurizei mixture comprising 3 fj;om abeit 35 to abut 65 parts by weight 4 of at I:st one fatty acid ester of a polyhydric alcohol, from ab4uat- 15 to abut.L 60 parts by weight 6 if at least one olefin, and 7 from abe-t- 10 to-ab-t- 90 parts by weight 8 of at least ono fatty acid ester of a monohydric alcohol. 1 22. The composition of claim 20 wherein the mixture 2 further comprises 3 from about 10 to about 90 parts by weight 4 1 at least one fatty acid ester of a monohydric alcohol. 1 23. The composition of claim 15 wherein the mixture 2 further comprises 3 from a-eet- 10 to abou-t 90 parts by eight 4 of at least one fatty acid ester of a monohydric alcohol. 1 24. The ccmposition of claim 18 wherein the mixture 2 further comprises 3 from ve4- 10 to--a)ht- 90 parts by weight 4 of at 'east one tatty acid ester of a monohydric alcohol. 1 25, A composition comprising 2 from 10 to 90 rercent by weight of a 3 partial fatty acid ester of a polyhydric alcohol and 4 from 90 to 10 percent by weight of a sulfurized composition prepared by reacting at 100-210 0 c a 6 sulfurizing agent comprising elemental asulfur with a 7 ixtul o f 2 or more reactants selected from the :roup 8 q.onsistirg Of 9 at least one fatty acid ester of f polyhydric Alcchol, 11 at least one fatty acid, 12 at least one olefin, and WO 89/06683 PCT/US88/04661 41 13 at least one fatty acid ester of a 14 monohydric alcohol. 1 26. The composition according to claim 25 wherein 2 component comprises a fatty acid ester of glycerol. 1 27. The composition of claim 26 wherein component 2 comprises glycerol monooleate. 1 28. The composition of claim 26 wherein component 2 comprises a mixture of glycerol monooleate, glycerol 3 dioleate and glycerol trioleate. 1 29. The composition according to claim 25 wherein 2 reactant is present as a component of a fatty oil, 3 said oil containing at least ai.;-50% by weight of a full 4 fatty acid ester of a polyhydric alcohol. 1 30. The composition, according to claim 25 wherein 2 reactant is at least one aliphatic olefin contain- 3 ing from a4t 4 to abei 40 carbon atoms. 1 31. The composition according to claim 26 wherein 2 reactant comprises oleic aciu. 1 32. The composition according to claim 25 wherein 2 reactant comprises methyl olente. 1 33. The composition of claim 1 wherein the 2 cosulfurized mixture, is prepared by reacting at an 3 elevated temperature, a sulfurizing agent with two or more 4 members of the group consisting of at least one fatty acid ester of a 6 polyhydric alcohol, 7 at least one fatty acid, 8 t3) at least one olefin, and WO 89/06683 PCT/US88/04661 42 9' at least one fatty acid ester of a monohydric alcohol. 1 34. The composition of claim 33 wherein the 2 sulfurizing agent comprises sulfur. 1 35. The composition of claim 34 wherein the 2 sulfurizing agent further comprises hydrogen sulfide. 1 36. An additive concentrate for use in preparing 2 1 lubricating compositions, comprising a substantially 3 inert, normally liquid organic diluent and abeti- 1 to 4 -a&bet- 90% by weight of the composition of claim 1. 1 37. An additive concentrate for use in preparing 2 lubricating compositions, comprising a substantially 3 inert, normally liquid organic diluent and abe-- 1 to 4 abazt-90% by weight of the composition of claim 1 38. An additive concentrate for use in preparing 2- lubricating composition,^. comprising a substantially 3 inert, normally liquid organic diluent and -abou-t- 1 to 4 -aboti--90% by weight of the composition of claim 33. 1 39. A lubricating composition comprising a major 2 amount of an oil of lubricating viscosity and a minor 3 amount of the composition of claim 1. 1 40. A lubricating composition comprising a major 2 amount of an oil of lubricating viscosity cnd a minor 3 amount of the composition of claim 3 41. A lubricating composition comprising a major 2 amount of an oil of lubricating viscosity and a minor 3 amount of the composition of claim 33. /I V^7 0 1 M t^ 1 WO 89/06683 PCT/US88/04661 43 1 42. A lubricating composition comprising a major 2 amount of an oil of lubricating viscosity and a minor 3 amount of the additive concentrate of claim 36. 1 43. A lubricating composition comprising a major 2 amount of an oil of lubricating viscosity and minor 3 amounts, effective to impart extreme pressure or friction 4 modifying properties, of a partial fatty acid ester of a polyhydric 6 alcohol and 7 a cosulfurized mixture of 2 or more 8 ';eactants selected from the group consisting of 9 at least one fatty acid ester of a polyhydric alcohol, 11 at least one fatty acid, 12 at least one olefin, and 13 at least one fatty acid ester of a 14 monohydric alcohol. pp. H-L INTERNATIONAL SEARCH REPORT International Application No PCT/US 88 /04661 1. CLASSIFICATION OF SUBJECT MATTER (it several ciaslflic~tion symbols apply, indicate all) According to International Patent Classification (IPC) or to both National Classification and IPC IPC 4 C 10 M 141/08; C 10 M 135/02; C 07 C 149/00 11, FIELDS5 SEARCHED Minimum Documentation Searched Classification System I Classification Symbols 4 IPC Cl10M; C 07 C Documentation Searched other than Minimum Documentation to the Extent that such Documents are Included In the Fields SearchedI I1l. DOCUMENTS CONSIDERED TO BE RELEVANT' Category I Citation of Document, 11 with Indication, where anproprIate, of the rele vant Passages 12 Relevant to Claim No. 13 Y US, A, 2527889 MOORE) 1-43 31 October 1950 see column 2, line 6 column 3, line 24; column 5, lines 14-25 Y US, A, 3112267 PRICE) 1-43 26 November 196~3 see claims 6-10; column 4, line 22 column 5, Y WO, A, 86/06371 (LUBRIZOL) I1-43 6 November 1986 see page 32, claim 1 page 39, claimi cited in the application Y EP, A, 0009701 (RHiEIN-CH-EMIE RUEINAU 1-43 IGmbH) 16 April 1980 see claims 1-6; page 2, line 21- page 5, line 7 Y US, A, 3926822 UABIBY) 1-43 16 December 1975 *Special categories of cited documental ic later document published after the International fling date "All document doinlna the general state of the art which Is rnot or priority date and not In conlIct with the application but considered to be of particular relevanc, cited to understand the principle or theory underlying the Invention earlier document but published on or atear the Internatiorial doumn of particular reieva:..al the claimed Invention filing date cannot be considered novel or cannot be considered to "Ll document which may throw doubts on priority claim(s) or Involve an Inventive step which Is cited to establish the pliblicatlon date of another documetft of particular relevance;' the claimed Invention citation or other speciel reason (axs specified) cannot 0.0 conuideored to Involve an Inventive stoo, when the "0D" document referring to an oral disclosure, uie, exhibition or document Is combined with one or more other such docU. other means manta, such combination being obvious to a person skilled 1IP" document Published prior to the International fi'ling date but in the art, later then the priority date claimed document member of the same patent family Date of the Actual Completion of the iternational Search Date of Mailing of this International Search Report March 1989 10, 04, 89 International Searching ok=Itrlty Slrauo-tuo f~o EURQ0~tAN PA TENT OFFICEPTN Form PCTIISA/210 44et ond slheet) IJanuary 016) -2- tIternationat Application No. PCT/US 88 /04661 II11. -00CU~.'NTS CONSIDERED TO BE RELEVANT (CONTINUED FROM THE SECOND SHEET) Category II Citation of Docuiment, with indication', tobme appropiate, of t"e re~event pasages IRelevant to Claim No see claims 1-11' cited in the application Foom PCT ISA'2tQ (exits sheet) January 4S65I