US3536738A - Bis(trimethylolpropane diallyl ether) dilinoleate and its phosphonates and lubricant compositions - Google Patents

Bis(trimethylolpropane diallyl ether) dilinoleate and its phosphonates and lubricant compositions Download PDF

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US3536738A
US3536738A US719813*A US3536738DA US3536738A US 3536738 A US3536738 A US 3536738A US 3536738D A US3536738D A US 3536738DA US 3536738 A US3536738 A US 3536738A
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dilinoleate
phosphonated
ester
diallyl ether
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Winfred E Parker
Ronald E Koos
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M1/00Liquid compositions essentially based on mineral lubricating oils or fatty oils; Their use as lubricants
    • C10M1/08Liquid compositions essentially based on mineral lubricating oils or fatty oils; Their use as lubricants with additives
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F9/00Compounds containing elements of Groups 5 or 15 of the Periodic Table
    • C07F9/02Phosphorus compounds
    • C07F9/28Phosphorus compounds with one or more P—C bonds
    • C07F9/38Phosphonic acids [RP(=O)(OH)2]; Thiophosphonic acids ; [RP(=X1)(X2H)2(X1, X2 are each independently O, S or Se)]
    • C07F9/40Esters thereof
    • C07F9/4003Esters thereof the acid moiety containing a substituent or a structure which is considered as characteristic
    • C07F9/4006Esters of acyclic acids which can have further substituents on alkyl
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2203/00Organic non-macromolecular hydrocarbon compounds and hydrocarbon fractions as ingredients in lubricant compositions
    • C10M2203/10Petroleum or coal fractions, e.g. tars, solvents, bitumen
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2203/00Organic non-macromolecular hydrocarbon compounds and hydrocarbon fractions as ingredients in lubricant compositions
    • C10M2203/10Petroleum or coal fractions, e.g. tars, solvents, bitumen
    • C10M2203/102Aliphatic fractions
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/28Esters
    • C10M2207/282Esters of (cyclo)aliphatic oolycarboxylic acids
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/28Esters
    • C10M2207/34Esters having a hydrocarbon substituent of thirty or more carbon atoms, e.g. substituted succinic acid derivatives
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2223/00Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions
    • C10M2223/06Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions having phosphorus-to-carbon bonds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2223/00Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions
    • C10M2223/06Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions having phosphorus-to-carbon bonds
    • C10M2223/061Metal salts
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2223/00Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions
    • C10M2223/06Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions having phosphorus-to-carbon bonds
    • C10M2223/065Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions having phosphorus-to-carbon bonds containing sulfur
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2040/00Specified use or application for which the lubricating composition is intended
    • C10N2040/08Hydraulic fluids, e.g. brake-fluids

Definitions

  • This invention relates to esters of dimer acids and their phosphonates and more particularly to the diallyl ether esters of dimer acids and their phosphonates.
  • An object of the invention is to prepare thermally stable fluids for use as extreme pressure and base oil lubricants,
  • Another object of the invention is to formulate thermally stable compositions for use as extreme pressure, anti-wear lubricants.
  • Etfective lubricants for any type of machinery should be capable of performing their function over long periods of time without appreciable changes in their physical and chemical characteristics.
  • Mineral hydrocarbon lubricating oils are not suitable for many lubrication problems of modern industry. Consequently, synthetic lubricants, such as bis (2 ethylhexyl) sebacate and dibenzyl sebacate, em ployed as controls for evaluating the compounds of the present invention, have been prepared and used as specialty products. There is, however, continued need for better and more effective lubricants and lubricant additives capable of sustained performance under more demanding operating conditions.
  • the 5% by weight of the compounds of the present invention used as additives in the formulation of lubricant mixtures is arbitrary and is not intended to limit the use of the compounds to that amount. Although the amount would usually be about 5% or less, it is obvious to anyone skilled in the art that other amounts would produce desirable results.
  • the smaller value denotes the oil with the better lubricating property.
  • the compounds of the present invention (Nos. 1, 2 and 3 in Table I) and the lubricant compositions (Nos. 10, 11, 13, l5, l7 and 19 in Table I) formulated by the addition of the fully phosphonated ester (No. 3 in Table I) to the reference lubricants (Nos. 4, 5, 12, l4, l6 and 18 in Table I) show a very marked improvement in anti-wear lubricant properties over the reference compounds.
  • the 2-ethylhexyl) sebacate (No. 4, Table I) was used without additive the diameter of the wear scar measured 0.830 mm.
  • Incipient seizure is defined as the load at which a sudden sizeable increase in wear scar diameter occurs
  • welding is the load at which motion of the upper rotating ball in relation to the other three is no longer possible.
  • the samples were run at room temperature under available loads for a one minute period. A fresh sample was used for each load. Rotation of the upper ball was 1700 r.p.m.
  • Tables II and III show that the fully phosphonated bis (trimethylolpropane diallyl ether) dilinoleate can perform its lubricat ing function under much greater pressures than can the reference lubricants (Nos. 1, 2, 3, 4, Table II).
  • the extreme seizure load for a commercial built lubrication oil (No. 3, Table II) was 110 kg. while that of the fully phosphonated ester (No. 5, Table II) was 300 kg.
  • the pressure Weld load for the same commercial oil (No. 3, Table II) was 190 kg. while that of the fully phosphonated ester of this invention (No. 5, Table II) was 350 kg.
  • Thermal stability was determined by the thermogravimetry, heating the compound in a specially designed sample holder suspended from a weighing mechanism. This procedure has been described by Parker, et al., J. Am. Oil Chem. Soc. 42, 792, (1965). The Onset of De- 4 cant additives. The kinematic viscosity, viscosity index, and the ASTM slope were determined according to ASTM D445-60 and ASTM D56753 using Cannon- Manning semi-micro viscometers.
  • the compounds of the present invention have several other desirable features: (1) they are relatively high molecular weight compounds, 'yet they are monomers, not polymers; (2) their molecular weights can be varied in the range between about 953 and 2179 depending on the extent of phosphonation, thus allowing the production of tailor-made compounds with predetermined physical and chemical properties; (3) they could be expected to have the lubricating properties of an ether, an alkane or alkene and a dibasic ester and when phosphonated, those of an alkyl phosphonate; (4) they should be compatible or soluble in base oils that contain any of the above named functional groups; (5) that portion of the molecule represented by R in the unphosphonated compound has four reactive sites which may be reacted with any compound that usually adds across a double bond.
  • composition for these compounds is in the range 410- moved, and the crude product purified by molecular distil- 490 F. Phosphonated compounds decompose in the lower temperature range to the original dilinoleate ester. Bis- (trimethylolpropane diallyl ether) dilinoleate starts to decompose at 490.
  • P.D.E. 150 0. 596 P.D.E. 200 0. 693 P.D. E. 250 0. 710 P.D.E. 300 P.D.E. 350
  • the compounds have a wide range of viscosity characteristics as shown in Table IV.
  • the viscosity of the fully phosphonated ester is similar to that of commercial lubrilation.
  • phosphonated esters In the preparation of the phosphonated esters, about one mole of the above ester was reacted with about nine moles of a dialkyl phosphonate (dialkyl hydrogen phosphite) in the presence of a peroxide catalyst. The catalyst was added in one-quarter portions at four hour intervals. The excess phosphonate was distilled 01f under reduced pressure, and the phosphonated ester was purified by molecular distillation. The extent of reaction was determined by infrared spectra, iodine number and percent phosphorus.
  • dialkyl phosphonate dialkyl hydrogen phosphite
  • the alkyl radical of the dialkyl phosphonate can be any straight or branched chain aliphatic alkyl radical containing 1 to 8 carbon atoms such as methyl, ethyl, propyl, butyl, amyl, hexyl, heptyl, octyl and any of their isomers.
  • the di-Z-ethylhexyl phosphonate derivatives are used to exemplify this invention.
  • the dimer acid employed in the preparation of the esters contained dilinoleic acid, 4% trimer acid, and 1% monobasic acid and had the following characteristics: Acid number, 191.2; neutralization equivalent, 293.4; and molecular weight, 565.
  • the dialkyl phosphonate dialkyl hydrogen phosphite
  • was redistilled before use Best results were obtained with use of naphthalene-Z-sulfonic acid as the esterification catalyst.
  • Naphthalene-l-sulfonic acid, methane sulfonic acid, and sulfuric acid can also be used in the catalyst, but give poorer results than naphthalene-2-sulfonic acid.
  • the catalyst used for the dialkyl phosphonate addition was t-butyl perbenzoate.
  • the crude product was purified by molecular distillation, the main fraction being collected above 225 C. at 7 micron pressure. This fraction weighed 101 g.
  • the purified product, bis(trimethylolpropane diallyl ether) dilinoleate, a medium amber liquid had the following characteristics: n 1.4782; iodine number 135.1; saponification number 121.1, calcd., 117.7; saponification equivalent 465.5, calcd., 476.8; percent carbon 75.78, calcd., 75.88; percent hydrogen, 11.08 calcd. 10.99; molecular weight, 931, calcd., 953.
  • the reaction mixture was degassed in a molecular still at room temperature under a partial pressure.
  • the excess phosphonate was distilled 01f at 120-150 C. at microns pressure.
  • the main fraction, a viscous amber liquid, was collected above 200 C. at 7 microns.
  • the purified product weighed 64.0 g.; percent carbon, 71.42, calcd., 68.34; percent hydrogen, 11.15, calcd., 11.29; percent phosphorus, 3.03, calcd., 5.68; iodine number, 75.7.
  • the infrared spectra, iodine number, and the percent phosphorus indicated that the compound had attained 5 3% 0f the maximum amount of dialkyl phosphonate addition.
  • Example 3 The procedure of Example 2 was repeated except that the reaction time was increased to 32 hours and 1.1 g. Catalyst was added at 4 hour intervals (total amount, 9 g.). Molecular distillation, above 240 C. at 7 microns pressure, yielded a very pale amber viscous liquid. The purified product weighed 60.0 g.; percent yield, 52.6; iodine number 20.7; n 1.4755; percent carbon, 67.82, calcd., 68.34; percent hydrogen, 10.99, calcd., 11.29; percent phosphorus, 5.64, calcd., 5.68; molecular weight (calcd.), 2179.
  • R" is 2-ethylhexyl.

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Description

United States Patent Office 3,536,738 Patented Oct. 27, 1970 U.S. Cl. 260-403 Claims ABSTRACT OF THE DISCLOSURE This invention provides diallyl ether esters of dimerized linoleic acid useful as lubricant compositions.
This application is a division of Ser. No. 573,428, filed Aug. 18, 1966, now Pat. No. 3,423,319.
A non-exclusive, irrevocable, royalty-free license in the invention herein described, throughout the World for all purposes of the US. Government, with the power to grant sublicenses for such purposes, is hereby granted to the Government of the United States of America.
This invention relates to esters of dimer acids and their phosphonates and more particularly to the diallyl ether esters of dimer acids and their phosphonates.
An object of the invention is to prepare thermally stable fluids for use as extreme pressure and base oil lubricants,
lubricant additives, hydraulic fluids and the liquid phase of gas-liquid chromatographic columns.
Another object of the invention is to formulate thermally stable compositions for use as extreme pressure, anti-wear lubricants.
Other objects and a fuller understanding of the invention may be had by referring to the following description and claims.
Etfective lubricants for any type of machinery should be capable of performing their function over long periods of time without appreciable changes in their physical and chemical characteristics. Mineral hydrocarbon lubricating oils are not suitable for many lubrication problems of modern industry. Consequently, synthetic lubricants, such as bis (2 ethylhexyl) sebacate and dibenzyl sebacate, em ployed as controls for evaluating the compounds of the present invention, have been prepared and used as specialty products. There is, however, continued need for better and more effective lubricants and lubricant additives capable of sustained performance under more demanding operating conditions.
The compounds of the present invention are represented by the formula:
C2115 C1120 CHr-R'] B wherein R is the diacyl radical derived from dimerized linoleic acid or the hydrogenated product thereof, R' represents CH=CH or CHzO CHg-R' Anti-wear properties were determined using the Shell Four Ball Wear Tester as described by Peale et al., American Society of Lubrication Engineers Transactions 3, 48 (1960). Approximately 10 ml. of the test oil were placed in the test cup so that the three bottom stationary balls were covered to about a 2 mm. depth, After positioning the cup on its stand in contact with the fourth ball, the oil was heated to 120 C., a 50' kg. load was placed on the weight tray, and the upper ball was allowed to rotate at 600 rpm. for 1 hour. The diameters of the circular scars worn on the three stationary balls were measured by means of a low power microscope. The results are shown in Table I.
The 5% by weight of the compounds of the present invention (lubricants 1, 2 and 3 in Table I) used as additives in the formulation of lubricant mixtures is arbitrary and is not intended to limit the use of the compounds to that amount. Although the amount would usually be about 5% or less, it is obvious to anyone skilled in the art that other amounts would produce desirable results.
In the wear tests, the smaller value denotes the oil with the better lubricating property. The compounds of the present invention (Nos. 1, 2 and 3 in Table I) and the lubricant compositions (Nos. 10, 11, 13, l5, l7 and 19 in Table I) formulated by the addition of the fully phosphonated ester (No. 3 in Table I) to the reference lubricants (Nos. 4, 5, 12, l4, l6 and 18 in Table I) show a very marked improvement in anti-wear lubricant properties over the reference compounds. For example, when his (2-ethylhexyl) sebacate (No. 4, Table I) was used without additive the diameter of the wear scar measured 0.830 mm. However by adding 5% by weight of the fully phosphonated ester (No. 3, Table I) to the his (2-ethylhexyl) sebacate, the diameter of the wear scar was reduced almost 50% to 0.442 mm. (No. 10, Table I). Another example is the paraffin oil (No. 5, Table I). Without additive, the wear scar measured 0.803 mm. in diameter. With the fully phosphonated ester (No. 3, Table I) added to it, the wear scar was Only 0.460 mm. in diameter (No. 11, Table I). Other examples showing similar improvement in lubricating properties can be found in Table I.
TABLE I.LUBRICATION AS MEASURED BY WEAR SCAR Lubricant Additive Wear scar,
No. Name (5% by weight) die. mm;
1. Dilinoleate ester None I 0. 760 "2- 53% phosphonated .do 0. 483
dilinoleate ester. 3 phosphonated di- -do 0. 410
linoleate ester. 4 Bis(2-ethy1hexyl) .do 0. 830
sebacate. 5 100 paraffin oil ..do 0. 803 6 Bis (2-ethylhexy1)- Dilinoeete ester 0. 778
sebacate. 7 100 paraffin oil- "do 0. 597 8- Bis (2-ethylhexyl) 53% phosphonated di- 0. 455
sebacate. linoleate ester. 9. 100 paraflin oil do 0. 460 10- Bis(2-ethylhexyl) 100% phosphonated di- 0. 442
sebacate. linoleate ester. 1l 100 paraffin oil ..do 0. 460 12 BisCbenzyl) dilinoleate- None 0. 653 13 -do 100% phosphouated di- 0. 470
linoleate ester. 14 Hydrogenated bis (ben- None 0. 748
zyl)-di1i.uoleate. .do 100% phosphonated di- 0. 447
linoleate ester. 16 Bis-(p-isopropyl benzyl)-None 0. 843 17 do 10 phosphonated di- 0. 587
linoleate ester. 18. Dibenzyl sebacate None 0. 950 19 .do 100% phosphonated di- 0. 620
linoleate ester.
The extreme pressure properties were determined with a Shell Four Ball Extreme Pressure Tester also described by Peale et al. This is similar to the Wear Tester except that it is more rigidly built and made to accommodate higher loads.
This instrument was used to determine loads at incipient seizure and at welding. Incipient seizure is defined as the load at which a sudden sizeable increase in wear scar diameter occurs, and welding is the load at which motion of the upper rotating ball in relation to the other three is no longer possible. The samples were run at room temperature under available loads for a one minute period. A fresh sample was used for each load. Rotation of the upper ball was 1700 r.p.m. The results, Tables II and III, show that the fully phosphonated bis (trimethylolpropane diallyl ether) dilinoleate can perform its lubricat ing function under much greater pressures than can the reference lubricants (Nos. 1, 2, 3, 4, Table II). For example, the extreme seizure load for a commercial built lubrication oil (No. 3, Table II) was 110 kg. while that of the fully phosphonated ester (No. 5, Table II) was 300 kg. Also, the pressure Weld load for the same commercial oil (No. 3, Table II) was 190 kg. while that of the fully phosphonated ester of this invention (No. 5, Table II) was 350 kg.
Thermal stability was determined by the thermogravimetry, heating the compound in a specially designed sample holder suspended from a weighing mechanism. This procedure has been described by Parker, et al., J. Am. Oil Chem. Soc. 42, 792, (1965). The Onset of De- 4 cant additives. The kinematic viscosity, viscosity index, and the ASTM slope were determined according to ASTM D445-60 and ASTM D56753 using Cannon- Manning semi-micro viscometers.
The compounds of the present invention have several other desirable features: (1) they are relatively high molecular weight compounds, 'yet they are monomers, not polymers; (2) their molecular weights can be varied in the range between about 953 and 2179 depending on the extent of phosphonation, thus allowing the production of tailor-made compounds with predetermined physical and chemical properties; (3) they could be expected to have the lubricating properties of an ether, an alkane or alkene and a dibasic ester and when phosphonated, those of an alkyl phosphonate; (4) they should be compatible or soluble in base oils that contain any of the above named functional groups; (5) that portion of the molecule represented by R in the unphosphonated compound has four reactive sites which may be reacted with any compound that usually adds across a double bond.
In a typical procedure for the preparation of the esters about a 2 to 1 molar ratio of alcohol to dimer acid and a small amount of an acid catalyst were dissolved in an inert organic solvent such as benzene and refluxed until the reaction was complete, as indicated by the amount of water collected. The benzene solution was washed until free of acid, dried over calcium sulfate, the benzene re- TABLE IV.VISCOSITY CHARACTERISTICS OF BIS(METHYLOLPROPANE DIALLYL ETHER) DILINOLEATE AND ITS PHOSPHONATED ESTER WHEN USED AS BASE OIL AND AS ADDITIVE Kinematic viscosity eentistokes at C.
Viscosity A.S.T.M. Sample 37. 8 54. 3 98. 8 index slope Dilinoleate ester (D.E.) 257. 8 115. 58 24. 6 118. 1 0. 602 100% phosphonated dilinoleate ester (PDE) 752. 4 255. 8 40. 3 105. 5 0. 638 Bis(2-ethylhexyl sebacate) (D.O S 12. 7 8.08 3. 34 154 0.710 100 paratfin oil 51. 3 24. 7 6. 80 94. 0 0. 742 D.O.S.+5% DE (as additive) 14. 8 9. 12 3. 76 175 0. 729 100 parafiin oil+5% DE (as additive)- 50. 4 24. 2 6. 78. 8 0. 778 D.O.S.+5% P.D.E.(as additive) 17. 8 10. 9 4. 28 170 0. 672 100 parafiin oil+5% P.D.E. (as additive) 73. 8 33. 8 8. 70 97. 9 733 D.O.S.+5% P.D.E.-53 (as additive) 14. 6 9. 10 3. 66 158. 8 0. 688 100 paralfin oil+5% P.D.E.-53 1 (as additive 50. 7 23. 8 6. 36 75. 6 0. 783
1 53% phosphonated dilinoleate ester. composition for these compounds is in the range 410- moved, and the crude product purified by molecular distil- 490 F. Phosphonated compounds decompose in the lower temperature range to the original dilinoleate ester. Bis- (trimethylolpropane diallyl ether) dilinoleate starts to decompose at 490.
TABLE II.COMPARATIVE FOUR BALL EXTREME PRESSURE TEST DATA 1 l Tests conducted at room temperature for one minute.
TABLE III.-FOUR BALL EXTREME PRESSURE TEST DATA ON PHOSPONATED BIS(METHYLOLPROPANE DIALLYL ETHER) DILINOLEATE (PDE) P.D.E. Load, kg. Sear dia., mm.
P.D.E. 150 0. 596 P.D.E. 200 0. 693 P.D. E. 250 0. 710 P.D.E. 300 P.D.E. 350
l Tests run at room temperature for one minute.
2 Incipient seizure. 3 Weld10 sec.
The compounds have a wide range of viscosity characteristics as shown in Table IV. The viscosity of the fully phosphonated ester is similar to that of commercial lubrilation.
In the preparation of the phosphonated esters, about one mole of the above ester was reacted with about nine moles of a dialkyl phosphonate (dialkyl hydrogen phosphite) in the presence of a peroxide catalyst. The catalyst was added in one-quarter portions at four hour intervals. The excess phosphonate was distilled 01f under reduced pressure, and the phosphonated ester was purified by molecular distillation. The extent of reaction was determined by infrared spectra, iodine number and percent phosphorus.
The alkyl radical of the dialkyl phosphonate can be any straight or branched chain aliphatic alkyl radical containing 1 to 8 carbon atoms such as methyl, ethyl, propyl, butyl, amyl, hexyl, heptyl, octyl and any of their isomers. The di-Z-ethylhexyl phosphonate derivatives are used to exemplify this invention.
The dimer acid employed in the preparation of the esters contained dilinoleic acid, 4% trimer acid, and 1% monobasic acid and had the following characteristics: Acid number, 191.2; neutralization equivalent, 293.4; and molecular weight, 565. The dialkyl phosphonate (dialkyl hydrogen phosphite) was redistilled before use. Best results were obtained with use of naphthalene-Z-sulfonic acid as the esterification catalyst. Naphthalene-l-sulfonic acid, methane sulfonic acid, and sulfuric acid can also be used in the catalyst, but give poorer results than naphthalene-2-sulfonic acid. The catalyst used for the dialkyl phosphonate addition was t-butyl perbenzoate.
Preparation of the esters is illustrated by the following examples which are not intended to be in limitation of the scope of the present invention:
solved in 450 ml. benzene in a two-liter 3-neck flask. The flask was equipped with a magnetic stirrer, thermometer,
' and a Dean and Stark tube with a water-cooled condenser. The mixture was heated at 90 C. reflux temperature until 7.5 ml. of water was taken 01f in 7 hours reaction time. Since the amount of water collected indicated that the reaction had not gone to completion, an additional 1.4 g. catalyst was added to the reaction mixture, and the rejuvenated reaction gave ofi an additional 1.5 ml. water in 2 hours. Total reaction time: 9 hours; total weight of catalyst, 4.2 g. After cooling, the reaction mixture was washed with water until acid-free. The benzene solution was dried over calcium sulfate, filtered, and the benzene evaporated under vacuum. The crude product, a dark amber fluid, weighed 233.5 g., percent yield, 96.6; acid number, 5.5; n 1.4776.
The crude product was purified by molecular distillation, the main fraction being collected above 225 C. at 7 micron pressure. This fraction weighed 101 g. The purified product, bis(trimethylolpropane diallyl ether) dilinoleate, a medium amber liquid had the following characteristics: n 1.4782; iodine number 135.1; saponification number 121.1, calcd., 117.7; saponification equivalent 465.5, calcd., 476.8; percent carbon 75.78, calcd., 75.88; percent hydrogen, 11.08 calcd. 10.99; molecular weight, 931, calcd., 953.
EXAMPLE 2 Bis(trimethylolpropane diallyl ether) dilinoleate, 50 g.; di-Z-ethylhexyl phosphonate, 144 g., and one-quarter of the total amount (4.6 g.) of t-butyl perbenzoate were mixed in a 500 ml. 3-neck flask. The flask was equipped with a magnetic stirrer, Water condenser, thermometer, and gas inlet tube. The reaction mixture was blanketed with nitrogen until the reaction was completed. While the reaction mixture was heated at 110 C. for 16 hours, one-quarter portions of the catalysts were added at four hour intervals. After each catalyst addition, except the last, the reaction temperature rose 5-6 degrees. The last addition resulted in only a two-degree rise. The reaction mixture was degassed in a molecular still at room temperature under a partial pressure. The excess phosphonate was distilled 01f at 120-150 C. at microns pressure. The main fraction, a viscous amber liquid, was collected above 200 C. at 7 microns. The purified product weighed 64.0 g.; percent carbon, 71.42, calcd., 68.34; percent hydrogen, 11.15, calcd., 11.29; percent phosphorus, 3.03, calcd., 5.68; iodine number, 75.7. The infrared spectra, iodine number, and the percent phosphorus indicated that the compound had attained 5 3% 0f the maximum amount of dialkyl phosphonate addition.
EXAMPLE 3 The procedure of Example 2 was repeated except that the reaction time was increased to 32 hours and 1.1 g. Catalyst was added at 4 hour intervals (total amount, 9 g.). Molecular distillation, above 240 C. at 7 microns pressure, yielded a very pale amber viscous liquid. The purified product weighed 60.0 g.; percent yield, 52.6; iodine number 20.7; n 1.4755; percent carbon, 67.82, calcd., 68.34; percent hydrogen, 10.99, calcd., 11.29; percent phosphorus, 5.64, calcd., 5.68; molecular weight (calcd.), 2179. The iodine number and percent phosphorus indicated that the ester had been phosphonated Since both the 53% and the 100% phosphonated derivatives are markedly improved lubricants over the unphosphonated compound and over the reference lubricants (Table I), it is considered that any products in the range of about from 50% to 100% phosphonated compounds are operative in the present invention.
We claim:
1. A compound of the formula:
CQH; GHZO GHQ-R i:
R- OCH2 CHzOCHz-R 2 wherein R is selected from the group consisting of the diacyl radical of dimerized linoleic acid and the diacyl radical of hydrogenated dimerized linoleic acid, R is selected from the group consisting of --CH=CH and 5. The compound of claim 4 in which R" is 2-ethylhexyl.
References Cited UNITED STATES PATENTS 2/ 1969 Furey et al. 260-407 X 2/ 1968 Nordgren 260-407 X LEWIS GOTTS, Primary Examiner C. L. MILLS, Assistant Examiner US. Cl. X.R.
US719813*A 1966-08-18 1968-01-29 Bis(trimethylolpropane diallyl ether) dilinoleate and its phosphonates and lubricant compositions Expired - Lifetime US3536738A (en)

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US20050227877A1 (en) * 2004-04-07 2005-10-13 Shiming Wo Polyoxyalkylene phosphonates and improved process for their synthesis

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NL8702018A (en) * 1987-08-28 1989-03-16 Dsm Resins Bv RESIN COMPOSITION BASED ON A POLYMER AND AN ESTER.

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KR100482671B1 (en) * 2002-02-05 2005-04-13 주식회사 태평양 The derivatives of dilinoleic acid and a method for preparation thereof and complex containing it
US20050227877A1 (en) * 2004-04-07 2005-10-13 Shiming Wo Polyoxyalkylene phosphonates and improved process for their synthesis
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