US2493216A - Mineral oil composition - Google Patents

Description

Prams Jan. 3, 1950 MINERAL OIL COMPOSITION Henry G. Berger, Glen Rock, and Everett W. I Fuller, Woodbury, N. J., assignors to Socony- Vacuum Oil Company, Incorporated, a corpora- 1 tion of New York No Drawing. Original application June 9, 1944,

Serial No. 539,597.

Divided and this application May 29, 1946, Serial No. 673,150

2 Claims. 252-33.!)

This invention has-to do with a new and novel mineral oil composition and, more particularly, has to do with a mineral oil composition containing minor proportions of an oil-soluble detergent and of an oil-soluble, phosphorusand sulfurcontaining reaction product.

It is well known to those familiar with the art that mineral oils are generally characterized by onevor more undesirable characteristics which limit their use. One such characteristic is their instability under operating conditions normally encountered in present day engines, such that after a relatively short time, metal engine parts become contaminated with sludge, lacquer and resinous materials. In many instances, the said materials form in and about piston rings causing them to stick, the phenomenon being referred to as ring-sticking. As a consequence of the instability of the oil, engine operating emciency is seriously reduced. Another undesirable characteristic of mineral oils is their tendency to oxidize, whereupon acidic materials are formed.

These acidic materials corrode metal engine parts, particularly alloy bearings such as those of the cadmium-silver, copper-lead, etc., type.

It is also well known in the art that numerous materials have been proposed as improving or fortifying agents for use in mineral oils to counteract or retard the aforesaid undesirable characteristics. Of the improving agents pre viously proposed, oil-soluble metal sulfonates have been found to be satisfactory in imparting detergent properties to mineral oils. Unfortunately, however, such sulfonates fail to improve, and in some cases even impair, other characteristics of mineral oils. In some instances, for example, metal sulfonates have increased the formation of acidic materials in mineral oils during use, thus inducing corrosion of metal parts with which the oils come in contact.

It has now been found that the corrosion and oxidation characteristics of an oil containing a small amount of an oil-soluble metal sulionate can be greatly improved by incorporating therewith a small amount of an oil-soluble, phosphorusand sulfur-containing reaction product of a dicyclic terpene and a phosphorus sulfide. More specifically, it has been found that an extremely stable oil having outstanding detergent, oxidation and corrosion characteristics is obtained by incorporating in an oil containing a metal sulfonate, a small amount of a reaction product of the aforesaid type. It has also been found that oils similarly characterized are obtained by incorporating a small amount of the said reaction product into oils containing small amounts of oil-soluble salts of. organic acids, which possess detergent properties.

All oil-soluble metal sulfonates are contemplated herein, typical of which are those obtained from aromatic hydrocarbons or substituted aromatic hydrocarbons, and a sulfonating agent such as strong sulfuric acid, oleum, chlor-'- sulfonic acid and the like. Other typical sulionates are those obtained by treatment of paraffins, naphthenes and various petroleum fractions-paraffinic, naphthenic or aromatic -with the same reagents. Preferred, however, are the metal salts of sulfonic acids of wax-substituted benzene and naphthalene, wherein the wax substituent is a long-chain aliphatic hydrocarbon group containing at least about ,18 carbon atoms and is obtained from paraflin wax.

All metals are contemplated herein as constituents of the said metal sulfonates. Especially suitable, however, are calcium, barium and zinc.

It is to be understood that when the metal sub-.

such materials are described in further detail" hereinafter in the examples.

As indicated hereinabove, oils containing other detergentsoil-soluble salts of organic 'acids possessing cleansing or detergent action in oilare also substantially improved in character when a small amount of the aforesaid oi1- soluble, phosphorusand sulfur-containing reaction product of a phosphorus sulfide and a di-' assure typical salts are well known in the art and may be prepared by any suitable method.

The oil-soluble, phosphorusand sulfur-containing reaction products contemplated herein are those obtained by reacting a dicyclic terpene and a phosphorus sulfide at a temperature above about 100 C. Although any one of the several phosphorus sulfides such as P381 (or P81), P48 (01' P281), P483, P285 (or P4510), P481, etc., may be used in the preparation of the said reaction products, particularly preferred are those reaction products obtained from Pass.

"Dicyclic terpenes are defined herein as those" terpenes which are characterized by the presence of one double bond in the molecule and which are comprised of two ring systems. Typical of such terpenes are pinene, camphene and fenchene. contemplated as coming within this par ticular designation are those materials which are predominantly comprised of one or more dicyclic terpenes; representative of such materials are the essential or volatile oils which are predominantly comprised of such a terpene, or terpenes, and are typified by turpentine oil, the predominant constituent of which is pinene. Preferred of the dicyclic terpene reactants are pinene'and turpentine oil. Accordingly, the preferred reaction prodnets are those obtained from Pass and pinene, and P385 and turpentine oil.

Although a complete understanding of the chemical composition of the reaction products contemplated here is not known at this time, a partial understanding of their composition may be realized by noting the characteristics involved in'the reaction. The reaction between phosphorus pentasulfide and pinene, for example, commences at about 100 C. and is exothermic in nature. During the reaction, the reaction mixture inappreciably in viscosity and little. if any, hydrogen sulfide is evolved therefrom. The reaction product obtained in thisreaction contains phosphorus and sulfur in substantially the same amounts as was added in the phosphorus sulfide It wouldappear, then, that the reaction is one of addition; that is, addition of the phosphorus sulfide to the .one unsaturated bond present in pinene.

While the reaction temperature for the reaction described above should be one of at least about 100 C., the preferred temperatures fall within the range of about 100 C. to about 160 C. The proportions of reactants used herein may be'varied in order to prepare reaction products different degrees of oil solubility and different degrees of oil improving power. It is preferred, however, to use about 1 mol of a phos, phorus sulfide with 4 mols of a dicyclic terpene for the preparation of a reaction product readily soluble in petroleum oils. For example, when 4 by using approximately 1 mol of a phosphorus sulfide for every 4 mols of a dicyclic terpene.

There is, however, still another desirable procedure for preparing thereaction products con-.

templated here. In order to obtain a relatively non-viscous reaction product, a blend of a dicyclic terpene, such as pinene, and a comparatively inert solvent such as a petroleum'oil, may be treated as described above to provide an oil blend of the reaction product. The preferred procedure of this type involves the use of a 1:1 blend of dicyclic terpene and petroleum oil with a phosphorus sulfide, the molar ratio of said terpene to said sulfide being 4:1.

Further details regarding the character of the aforesaid dicyclic terpene-phosphorus sulfide reaction products may be obtained byreferring to copending application Serial No. 482,482, filed April 9, 1943, of Everett W. Fuller et al.

The oil compositions contemplated herein may also contain, in addition to an oil detergent and a dicyclic terpene-phosphorus sulfide reaction product, a small amount of one or more other oil-soluble, phosphorusand sulfur-containing reaction products. One such reaction product is that which is obtained by reaction of approximore than 1 mol of P285 is used with 4 mols of pinene, a viscous gel-like reaction product is obmately 1 mol of phosphorus pentasulfide with 4 mols of oleyl alcohol, or ocenol, at a temperature between about 125 C. and about 150 C. for a relatively short time. These reaction products are described in further detail in copending application Serial No. 524,490, filed February 29, 1944, of Everett W. Fuller et al now U. S. Patent No. 2,411,153, issued November 19, 1946.

In the following examples, typical and preferred metal sulfonates and other oil-soluble metal detergents and dicyclic terpene-phosphorus sulfide reaction products are described in order to further explain the oil addition agents contemplated herein.

EXAMPLE 1 Basic barium diwax benzene suljonate A parafiln'wax having an average of 24 carbon atoms to the molecule and a melting point of 126 1". was chlorinated at about C. with chlorine gas until the weight of the wax had increased about 10%. The chlorowax (10% Cl) thus obtained was then blown with nitrogen to remove any occluded chlorine and hydrogen chloride.

One thousand and twenty (1020) parts of the above chlorowax was then reacted with 458 parts by weight of benzene in the presence of 62 parts of A101: at about 60 C. for about 2 hours. The excess benzene was then distilled ofi by warming to C. with" a stream of N: gas bubbling through the mixture. The monowax benzene thus formed was treated with an additional 1020 parts of chlorowax and the mixture heated to 85 C. until reaction stopped. It was allowed to stand overnight at about 60 C. and then decanted from the settled AlCh sludge and filtered. The product consisted essentially of diwax benzene.

Five thousand two hundred (5200) parts of the diwax benzene, prepared as described above, were treated with successive 250 parts of oleum.

containing 15% S03, while maintaining the temperature at 35-55 C. After 2600 parts of oleum had been added and the reaction had ceased,

3000 partsof water were added while the mix-.p ture was thoroughly stirred. An S. A. E. 30"

diwax benzene sultonic acid in the upper layer. This upper layer was treated with 3170 parts by weight of barium hydroxide octahydrate (Ba (OH) 3 BHIO) which represents an excess of barium hydroxide over that required to neutralize the diwax benzene sulfonic acid and any free sulfuric acid occluded therein. The reaction mixture thus formed was heated to about 140 C. for about 6 hours with nitrogen gas bubbling through it to remove water and it was then filtered through a layer of clay. The product-product A-consisted of an approximately 50% oil blend of basic barium diwax benzene sulfonate (analysis: 5.17% barium and 1.5% sulfur).

EXAMPLE 2 Zinc diwax benzene suljonate A diwax benzene sulfonic acid was prepared as described in Example 1 above and this was then treated with zinc acetate. After distilling oil the acetic acid, the product was filtered through clay leaving a material-product B--that contained 3.36% zinc and 1.6% sulfur.

EXAMPLE 3 Basic barium diwax naphthalene sulfonate Five hundred (500) parts of chlorowax, containing 12% chlorine, were added to 500 parts of Stoddard solvent and 108 parts of naphthalene. The mixture was warmed to 5060 C. and 30 grams of AlCls were added gradually. When the reaction stopped the mixture was heated to 90 C. and blown with N2 gas to remove HCl. It was then allowed to stand overnight at room temperature. The lower sludge layer was removed and the oil layer was filtered through clay. This consisted essentially of diwax naphthalene.

The diwax naphthalene was treated with 250 parts of oleum (15% S03) by adding the latter slowly so as to keep the temperature at 40-50 C. One thousand (1000) parts of water were then added with stirring and this was followed by 500 parts of an S. A. E. 30 grade motor oil. The mixture was allowed to stand at 6070 C. overnight and the oil layer was then withdrawn. This consisted essentially of 50% diwax naphthalene sulfonic acid in motor oil. This acid was treated with an excess of barium hydroxide and the mixture was heated to a maximum temperature of 150 C. in the presence of a stream of nitrogen to remove the water. After filtering, the Stoddard solvent was removed by heating to 170 C. at a vacuum of 5 mm. This left an approximately 50% solution of the basic barium diwax naphthalene sulfonate in the petroleum motor oil, which is identified herein as product C. It contained Ba and 2.0% S.

EXAMPLE4 Barium salt of petroleum oil sulfonate A Mid-Continent distillate of 95 seconds Saybolt viscosity at 100 F. was treated with oleum, the sludge was settled and removed, and the oil layer was neutralized with caustic soda solution. The sodium sulfonates thus formed were recovered by adding ethyl alcohol, separating the alcohol layer, and then evaporating off the alcohol. This left a mixture of oil and sodium sulfonates. This was contacted with a water solution of barium chloride and, after separation of the oil layer and drying, the latter-product D-was found to contain 6.9% Ba and 2.5% 8.

EXAMPLE 5 Barium triwax phenol carboxulate A barium salt of a triwax phenol carboxylateproduct E- -was prepared by the method described in U. S. Patent 2,197,835. It was formed in an oil blend and contained 4.0% Ba.

EXAMPLE 6 Sulfurized barium triwaa: phenol carborylate responding to the barium salt above (product E). This cobalt salt contained 1.83% Co.

EXAMPLE 8 Vanadyl oleyl phthalate A mol of oleyl alcohol was reacted with 2. mol of phthalic anhydride to give the half ester of oleyl phthalate. This was neutralized with sodium hydroxide and the sodium salt thus formed was treated with vanadyl chloride to give the vanadyl salt of oleyl phthalate (3.94% vanadium), which is identified herein as product H.

EXAMPLE 9 Pinene-P2S reaction product Eight hundred (800) parts by weight of pinene and an equal weight of a motor oil (Saybolt Universal viscosity of 45 seconds at 210 F.) were heated to C. with stirring. Three hundred and twenty-six (326) parts of Pass (a ratio of 4 mols of pinene to 1 mol of P285) were added slowly the temperature rising to C. because of the exothermic reaction. The mixture was then heated to C. for 1 hour, 20 parts of clay were added and the resultant mixture filtered. The filtrate, consisting of 1842 parts by weight, was then vacuum topped at 5 mm. pressure to a pot temperature of 150 C. The residue consisting of 1693 parts by weight was a clear, viscous f oil-product X-containing 12.5% sulfur and 5.1% phosphorus.

EXAMPLE 10 Oleyl alcohol-P285 reaction product Approximately 4 mols of ocenol, a commercial material consisting essentially of oleyl alcohol, and 1 mol of P285 were reacted at about 150 C. for 2 hours. The resulting product-product Y- contained 5.0% phosphorus and 9.8% sulfur.

The following test results are provided to demonstrate the properties of mineral oils containing small amounts of oil detergents and the outstandingly superior properties of mineral oils containing small amounts of the said detergents and of the aforesaid dicyclic terpene-phosphorus sulfide reaction products, which may also have in combination small amounts of other oilsoluble, phosphorusand sulfur-containing reaction products such as the oleyl alcohol-P285 product.

7 EXAMPLE 11 An accelerated oxidation test has been used in order to determine the corrosive nature of lubrieating oils under simulated operating conditions.

various time intervals and the top bearing is weighed to determine the corrosion loss thereof. The corrosion loss is plotted against the test time interval and each run is continued until a loss The apparatus used consists of a circulating 333332 3: 3 3: 1 :1 zi z g g: system whereby oil at 325 F. under a pressure of f 11 m m the time (in hours) pounds per square inch, is sprayed against a a z i'g 0 e 1 a b on that standard cadmium-nickel bearing for a period of a 22 1 y p it. 5 hours. The amount of oil under constant cir- A t n u to culation in the system is 1500 cc. In passing m g 1 md through the system, the oil comes into contact fi a an i g used m teel stainless steel copper and s an 0 super are Ihe with cast s i mcke1 bahng and is the test is a solvent-refined oil having an S. U. V. s zgg g Jz a g The on use; in this of 318 seconds at 100 F. The results are prea test contains a small amount 01' an accelerator, seated in Table II i g; I namely iron naphthenate (commercially desig- G I nated as Nuodex, 6% FezOa) which greatly increases the rate of oxidation of the oil. The Detergent PEI'WCZmt 8mm Perwficnt Emu degree of oxidation suffered by the oil is shown by the development of acidity therein as meas- 29 Product A 4 M ured by the neutralization number (N. N.), the a g a loss in weight of the cadmium-nickel bearing g ggg 3 M and the percentage viscosity increase. Do 2 g :3

The oil used was a solvent refined oil having a Do 1 s I w saybolt Universal viscosity of 65 seconds at 210 F. and containing 0.17% Of Nuodex. The results The results presented above in Table n demon- Of these are Shown in Table I belOW- state that an oil containing a small amount of Table 1 Percent Brg. t For t Detergent W Stabilizer ff N.N InVis. m

Ni! 1.39 as 1.200 2 on 10.67 183 .710 2 ProductX-.- .25 205 16 .165 2 .do .35 1.60 e .002 2 -do .so .15 a .000 2 {*Qifififififii: 1%3 g 22 w .25 2 .so 7 4m 2 u 5.01 is 1.195 2 Product x .50 2.40 11 .158 5 Nil.- 5.31 so .119 1.5 ProductX .26 0.72 7 013 It will be apparent from inspection of the rean oil detergent is more corrosive than the oil sults presented in Table I that the blank oil is alone. When a smal amount of a reaction produnsatisfactory in view of its corrosivity as shown not of the type defined above is add t such an by the neutralization number value and the oil, the corrosive nature of the oil is greatly bearing weight loss. The viscosity increase is co tera t d, also high. when a detergent alone is added to the oil there is little or no improvement in any 13 of these factors. However, when a small amount Tests of an oil, of 011 blends containing only an of the pinene-Pzss reaction product, product x, 011 detergent, and of oil blends containing an oil is added to the oil containing any one of the detergent and an oil-soluble, phosphorusand detergents, both the neutralization number forsulfur-wutainmg reaction product as defined mation and the bearing weight loss are greatly ve. were carried out to determine further the decreased. There also is less increase in viscosity. A corresponding improvement is obtained when small amounts of a pinene-PzS: reaction product and of an oleyl alcohol-Pass reaction product are added to an oil containing one of the detergents.

EXAMIPLEIZ The corrosivity of an oil and of an oil containing an oil detergent toward alloy bearings is demonstrated by the following test. Also demonstrated is the non-corrosive nature of the oil compositions contemplated herein, which contain small amounts of a phosphorusand sulfurcontaining reaction product of the aforesaid type, and an oil detergent.

comparative behavior of the unblended oil, the

oil containing only the detergent and the oil containing a detergent and said reaction product, under actual operating conditions.

.0 In this test a single-cylinder Lauson engine 06 F. (kinematic viscosity 5.75 at 210 F.).

comparing the neutralization number of the oil This test involves operating a single-cylinder C. F. R. engine containing copper-lead bearings, at an ,oil temperature of 285 F. and a Jacket blend with the neutralization number of the blank oil, which is run in the engine preceding the run with the oil blend. Ratings of greater than 1 indicate that the oil blend is less acidic temperatm'eofairl'. Thoenginehstoppedat than the blank oil and, therefore, superior 9 thereto, and ratings or less than 1 indicate that the oil blend is more acidic than the blank oil and, therefore, inferior thereto. The. results of these tests are set forth in Table 111 below.

The above results show that our oil compositions are highly eflective in improving the quality of an oil used in the General Motors type of Diesel ensine.

Table III Hours W are We k v N.N.

Results--. 10.0 10.6 l od lt t l Pi )d ctx 9.0 11.19 0.77

r u 2 Pmducty 1.0 0.41 1.0 4 rgguc 8.3 LN 8.7

r uc 4 Product? 1.: 6.52 1.0 2 Product .gg 2 no i were g a a: a P t rc uc P fi t 4 ProductX .50 1.8 0.29 3.4 Product H 03 2o. 9 32. 47 0. 62 Do .05 ProductX .50 3.0 7.11 8.7

EXAMPLE 14 As indicated hereinabove, preference is given A single cylinder Caterpillar Diesel engine was run for 96 hours at 19.8 brake horsepower and 1000 R. P. M. The oil temperature and the water temperature were both maintained at 195 F. The piston was then removed and rated for cleanliness. The results of several engine tests are presented in Table IV below.

Table I V A solvent refined s. A. E. grade Mid-Continent oil was used in the following tests.

Oil alone-test stopped due to ring sticking at 48 hours.

Oil+4% product A+0.5% product X-pistcn in excellent condition.

Oil+2% product A+0.25% product X+0.5%

product Y-piston in good condition.

Oil+2% product (H-0.5% product X-piston in excellent condition.

A three cylinder General Motors 3-71 Diesel engine was run at 2000 R. P. M. with an oil temperature of 230 F. and a jacket temperature of 180 F. When the air box pressure increased more than 3 inches of mercury over the original pressure, the ports were considered sufficiently closed to stop the test. In Table V below the time in hours to reach this condition is noted. A solvent refined S. A. E. 30 grade Mid-Continent oil was used in these tests.

Table V Hours to port closure Oil alone 122 Oil+4% product A+0.5% productX 285 Oil+2% product A+0.25% product X+0.5%

product Y 196 Oil+l.5% product E+0.75% product X 240 herein to those 011 detergents defined as metal sulfonates or wax-substituted aromatic hydrocarbons. This preference is infiuenced'by-their outstanding pour depressing properties as illustrated below in Table VI which gives results for products A and C, barium salts of diwax benzene sulfonic acid and diwax naphthalenesulfonic acid respectively, and for product D,- a barium salt of a sulfonic acid derived from petroleum ojll. The two former materials are efiective in lowering the pour point while the latter is ineffective. These tests were made on a solvent refined S. A. E.

30 grade of seconds Saybolt Universal viscosity at 210 F.

Table VI Detergent Percent agi g 82,323.". 1.0 it? Product 0--.- 1.0 l5 Product D; l. 0 +20 The results set forth in Tables I through V above demonstrate the outstanding qualities of the mineral oil compositions contemplated herein.

As shown in the said tables, they possess a high degree of resistance to oxidation and particularly desirable detergent properties. The results presented in Table VI above further demonstrate the superior quality of the preferred oil detergents, metal salts of wax-substituted aromatic hydrocarbon sulfom'c acids, as evidenced by their pour depressant properties.

As contemplated by the present invention, concentrations of from about 0.5% to about 10% of an oil detergent are used in an oil fraction, but concentrations of the order of about 4% have been found to be satisfactory for most purposes. The concentration of an oil soluble, phosphorusand sulfur-containing reaction product of a dicyclic terpene and a phosphorus sulfide may be varied from about 0.1% to about 3.0%; in general, however, about 0.5 will be satisfactory.

As indicated hereinabove, the mineral oil compositions of this invention may also contain one or more other oil-soluble, phosphorusand sulfurcontaining reaction products, such as those obtained from oleyl alcohol and P285, as defined above. Oils of excellent quality are obtained with Oil +2% product F+0.25% product X...-... 272 from about 0.25% to about 2.0% of such a reac- 11' tion product, incorporated with the aforesaid quantities of an oil detergent and of a dicyclic terpene reaction product of the type defined above.

Mineral oil concentrates are also contemplated herein. such concentrates containing substantially larger concentrations of an oil detergent and of a dicyclic terpene-phosphorus sulfide reaction product, than those enumerated above. That is, relatively large amounts of the said materials may be incorporated in an oil fraction in which they are readily soluble, and the oil concentrate so obtained may thereafter be diluted with a suitable quantity of the said oil fraction prior to use. It is to be understood that these mineral oil concentrates may also contain one or more of the aforesaid other oil-soluble, phosphorusand sulfur-containing reaction products, such as those obtained from oleyl alcohol in amounts substantially in excess of those described above.

In preparing th mineral oil compositions and concentrates contemplated herein, an oil detergent and a dicyclic terpene-phosphorus sulfide reaction product, as defined hereinabove, may be incorporated in a mineral oil in any one of several ways. For example, the dicyclic terpene reaction product may be added to an oil fraction containing an oil detergent; also, an oil detergent may be added to the reactants (dicyclic terpene and phosphorus sulfide) used in the preparation of the said reaction product and, in such case, will be present during the reaction. It is possible that the oil detergent may react with the dicyclic terpene and phosphorus sulfide to form a complex reaction product under the reaction conditions enumeratedabove; the product obtained in this manner may then be added to an oil fraction. Accordingly, it will be apparent that the mineral oil compositions and concentrates of this invention are complex in nature, for it is possible that an oil detergent and a dicyclic terpene-phosphorus sulfide reaction product may be present individually in an oil fraction, or may also be present therein as a physical combination or, further, may be present therein in the form of a single chemical composition. In the same connection, it will also used as a lubricant under certain conditions, such for example, as a lubricant in an engine operating at relatively high temperatures.

In view of the foregoing, the term mineral oil composition," as used herein, and as recited in all of the appended claims, is inclusive of all mineral oil fractions containing an oil detergent and a dicyclic terpene-phosphorus sulfide reaction product of the type defined above, in the concentrations previously enumerated, and is inclusive of oil compositions obtained or prepared by any of the aforesaid several procedures. Correspondingly, the term mineral oil concentra is inclusive of all mineral oil fractions containing relatively large amounts of the said 011 detergent and said reaction product.

It is to be understood that the examples. procedures and oil compositions described hereinabove are illustrative only and are not to be construed as limiting the scope of this invention thereto. For example, all dicyclic terpenes as broadly recited above may be used in place of pinene shown in the examples: however, pinene is preferred. Similarly, any phosphorus sulfide may be used in place of phosphorus pentasulfide shown in the examples, but the latter sulfide is preferred. Also, while the sulfonates and other illustrative oil detergents are preferred of their class, all compounds coming within the aforesaid definition of an oil detergent may be used. Furthermore, the mineral oil fractions disclosed above are but typical of the fractions which may be used.

This application is a division of our copending application Serial No. 539,597, filed June 9, 1944, now U. 8. Patent No. 2,416,281; issued February 25, 1947.

We claim:

1. An improved mineral oil composition comprising a viscous mineral oil fraction having in admixture therewith: a minor proportion, from about 0.5 per cent to about 10 per cent, of an oilsoluble metal sulfonate; a minor proportion, from about 0.1 per cent to about 3.0 per cent, of an oil-soluble, phosphorusand sulfur-containing reaction product obtained by reaction of a phosphorus sulfide and amaterial selected from the group consisting of a dicyclic terpene and an essential oil predominantly comprised of a dicyclic terpene, at a temperature greater than about C. and a minor proportion, from about 0.25 per cent to about 2.0 per cent. of an oil-soluble, phosphorusand sulfur-containing reaction product obtained by reaction of substantially one moi of phosphorus pentasulfide and four mols of oleyl alcohol at a temperature from about C. to about C. for a relatively short time.

2. An improved mineral oil composition comprising a viscous mineral oil fraction having in admixture therewith: a minor proportion, from about 0.5 per cent to about 10 per cent, of an oilsoluble, metal petroleum sulfonate; a minor proportion, from about 0.1 per cent to about 3.0 per cent, of an oil-soluble, phosphorusand sulfur-containing reaction product obtained by reaction of a phosphorus sulfide and a material selected from the group consisting of a dicyclic terpene and an essential oil predominantly comprised of a dicyclic terpene, at a temperature greater than about 100 C.; and a minor proportion, from about 0.25 per cent to about 2.0 per cent, of an oil-soluble, phosphorusand sulfurcontaining reaction product obtained by reaction of substantially one moi of phosphorus pentasulflde and four mols of oleyl alcohol at a temperature from about 125 C. to about 150". C. for a relatively short time.

HENRY G. BERGER. EVEREI'I W. FULLER.

REFERENCES CITED The following references are of record in the file of this patent:

UNITED STATES PATENTS Number Name Date 2,375,222 Grifiln et al. May 8, 1945 2,379,453 Noland July 3, 1945 2,411,153 Fuller et a1. Nov. 19, 1946 2,416,281 Berger Feb. 25, 1947

Claims (1)

1. AN IMPROVED MINERAL OIL COMPOSITION COMPRISING A VISCOUS MINERAL OIL FRACTION HAVING IN ADMIXTURE THEREWITH: A MINOR PROPORTION, FROM ABOUT 0.5 PER CENT TO ABOUT 10 PER CENT, OF AN OILSOLUBLE METAL SULFONATE; A MINOR PROPORATION, FROM ABOUT 0.1 PER CENT TO ABOUT 3.0 PER CENT, OF AN OIL-SOLUBLE, PHOSPHOROUS-AND SULFUR-CONTAINING REACTION PRODUCT OBTAINED BY REACTION OF A PHOSPHORUS SULFIDE AND A MATERIAL SELECTED FROM THE GROUP CONSISTING OF A DICYCLIC TERPENE AND AN ESSENTIAL OIL PREDOMINANTLY COMPRISED OF A DICYCLIC TERPENE, AT A TEMPERATURE GREATER THAN ABOUT 100* C.; AND A MINOR PROPORTION, FROM ABOUT 0.25 PER CENT TO ABOUT 2.0 PER CENT, OF AN OIL-SOLUBLE, PHOSPHORUS- AND SULFUR-CONTAINING REACTION PRODUCT OBTAINED BY REACTION OF SUBSTANTIALLY ONE MOL OF PHOSPHORUS PENTASULFIDE AND FOUR MOLS OF OLEYL ALCOHOL AT A TEMPERATURE FROM ABOUT 125*C. TO ABOUT 150*C. FOR A RELATIVELY SHORT TIME.