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EP0201197B1 - Oléfines sulfurées - Google Patents

Oléfines sulfurées Download PDF

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Publication number
EP0201197B1
EP0201197B1 EP86302488A EP86302488A EP0201197B1 EP 0201197 B1 EP0201197 B1 EP 0201197B1 EP 86302488 A EP86302488 A EP 86302488A EP 86302488 A EP86302488 A EP 86302488A EP 0201197 B1 EP0201197 B1 EP 0201197B1
Authority
EP
European Patent Office
Prior art keywords
accordance
kpa
psi
sulfur
olefin
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
EP86302488A
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German (de)
English (en)
Other versions
EP0201197A1 (fr
Inventor
Frank William Adis
Henry Ashjian
Angeline Baird Cardis
Andrew Gene Horodysky
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mobil Oil AS
ExxonMobil Oil Corp
Original Assignee
Mobil Oil AS
Mobil Oil Corp
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Publication date
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Application filed by Mobil Oil AS, Mobil Oil Corp filed Critical Mobil Oil AS
Priority to AT86302488T priority Critical patent/ATE54663T1/de
Publication of EP0201197A1 publication Critical patent/EP0201197A1/fr
Application granted granted Critical
Publication of EP0201197B1 publication Critical patent/EP0201197B1/fr
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Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M135/00—Lubricating compositions characterised by the additive being an organic non-macromolecular compound containing sulfur, selenium or tellurium
    • C10M135/02—Sulfurised compounds
    • C10M135/04—Hydrocarbons
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2219/00—Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions
    • C10M2219/02—Sulfur-containing compounds obtained by sulfurisation with sulfur or sulfur-containing compounds
    • C10M2219/022—Sulfur-containing compounds obtained by sulfurisation with sulfur or sulfur-containing compounds of hydrocarbons, e.g. olefines

Definitions

  • This invention is directed to sulfurized products which are useful as additives to lubricant compositions, various greases and liquid hydrocarbyl fuels. This invention is particularly directed to a process of preparing these sulfurized products, the products so prepared and lubricating and fuel compositions containing them.
  • Sulfurized olefins have been extensively used in many lubricant applications requiring extreme pressure/antiwear activity. It is well known that many methods have been used for producing organic sulfides by treating olefins. It is also well known that many sulfurized organic compositions are useful as lubricant additives.
  • the prior art processes provide sulfurized products having undesirably high levels of thiones, such as dithiol-thiones, and high levels of thiones in combination with various complex sulfurized mixtures.
  • these processes which are expensive and difficult to control, provide products having a highly disagreeable odor.
  • This invention relates to a process of preparing sulfurized organic additive products. These products consist essentially of mixtures of polysulfides, oligomers and dithiol-thione type compounds.
  • the additive products are prepared under pressure by the reaction of olefinic compounds with elemental sulfur within a relatively narrow range of temperatures, pressures and ratio of reactants to form products containing sulfur.
  • the additive product is suitable for use in an oil of lubricating viscosity or grease thereof or a liquid hydrocarbyl fuel and is prepared in a process comprising reacting in a suitable reaction zone an olefinic hydrocarbyl compound having at least one olefinic double bond with elemental sulfur in a molar ratio of sulfur to olefin of from 1.9:1 to 2.1:1 under pressures of from 2070 kPa (300 psi) to 6200 kPa (900 psi) at temperatures ranging from 140 to 180°C for a time sufficient and until the reaction pressure drops to 340 kPa (50 psi) to 690 kPa (100 psi) thereby producing a sulfurized additive product containing at least 45 weight percent of sulfur, preferably 45 to 55 weight percent sulfur, and consisting essentially of a major- amount of polysulfides and a minor amount of dithiol-thione type compounds.
  • Sulfurized additive products of enhanced extreme pressure/antiwear activity and improved corrosivity are obtained.
  • This invention is also directed to the additive products themselves and to compositions comprising oils of lubricating viscosity or greases prepared therefrom or liquid hydrocarbyl fuels containing the same.
  • the specific and significantly improved discrete compositions produced by the narrowly defined processing conditions disclosed herein provide thermally and oxidatively stable, noncorrosive, low-odor, extreme pressure/antiwear additives for lubricating oils, greases and fuels.
  • the invention in a particular aspect is directed to lubricant oil additives prepared in a one step-one pot process comprising reacting in a suitable reaction zone an olefinic hydrocarbyl compound having at least one olefinic double bond with elemental sulfur.
  • olefinic substances may be utilized in the process in accordance with the invention. This includes olefins with terminal or internal double bonds and containing from about 2 to 8 or more carbon atoms per molecule in either straight, branched chain or cyclic compounds and these may be exemplified by ethylene, propylene, 1-butene, cis and trans-2-butene, isobutylene, diisobutylene, triisobutylene, pentene, cyclopentene, hexene, cyclohexene, octene, 1-decene, etc.
  • diolefins for example butadiene, isoprene, divinyl benzene, pinene, p-menthene and limonene.
  • C 3 to C 6 olefins or mixtures thereof are preferred and more preferably butylenes are desirable for preparing the sulfurized products embodied herein because the combined sulfur content of the product decreases with increasing carbon content and the miscibility of the product with oil is lower in the case of propylene and ethylene derivatives.
  • isobutylene is particularly preferred as the predominant olefinic reactant, but it may be employed, desirably in major proportions, in mixtures containing one or more other olefins.
  • substantial proportions of saturated aliphatic hydrocarbons as exemplified by methane, ethane, propane, butane, pentane, etc. may be contained in the olefinic feed.
  • alkanes are preferably present in minor proportions in most instances to avoid unnecessary dilution of the reaction since they neither react nor remain in the product, but are expelled in the off-gases or by subsequent distillation.
  • such mixed feed can substantially improve the economics of the process since such streams are of lower value than a stream of, for example, relatively pure isobutylene.
  • Volatile olefins are often readily available in liquid form, and it is usually desirable to utilize olefinic liquids which are vaporized by the heat of reaction, as such evaporation provides a substantial cooling effect that permits the flowing of water for cooling the reactor to be reduced considerably for greater economy. Also, there are indications that the use of a volatile liquid olefin reactant has the unexpected and desirable effect of lowering the viscosity of the final product.
  • the specifically narrow molar ratio of sulfur to olefin may range from 1.9:1 to 2.1:1. In the case of butylene, the optimum ratio preferably is from 1.95:1 to 2.05:1.
  • the reaction temperature may range from 140 to 180°C, preferably from 158 to 165°C and most preferably from 159 to 161°C. The preferred temperature is 160°C.
  • the reaction pressure is allowed to seek its own optimum level and may range from 2070 kPa (300 psi) to 6200 kPa (900 psi). The preferred pressures are from 5170 kPa (750 psi) to 5860 kPa (850 psi).
  • a critical aspect of the pressure parameter is the pressure at which the reaction is stopped.
  • the reaction begins to seek its own pressure level and is held at a specific temperature most preferably 160°C until the pressure begins to drop.
  • the pressure at the reaction temperature must not be allowed to drop out of the range of from 340 kPa (50 psi) to 690 kPa (100 psi). Any conventional means known in the art for accomplishing this may be used.
  • the final pressure is indicative of the cited stoichiometry in accordance with the invention whereby the optimum product containing 45 to 61.5 weight % sulfur, preferably 45 to 55 weight % sulfur with no more than 10 to 20 weight % dithiol-thione type compounds based upon total weight of the additive product, is obtained.
  • the weight percent of sulfur to unsaturated olefin is preferably 59 to 61.5 weight percent for a C 3 olefin (propylene), 52 to 54.5 weight percent for a C 4 olefin (butylene) and 46.5 to 49 weight percent for a C s olefin (pentane).
  • the reaction may be catalyzed with a rate accelerating catalyst.
  • Alkylamine catalysts such as n-butylamine, di-n-butylamine, n-octylamine, triethylamine, di-cyclohexylamine and the like are suitable.
  • any suitable rate acceleration catalyst known in the art may be used, as for example quiholine and attapulgite acid clay.
  • the reaction between the sulfur and the olefinic compound may be conducted in any suitable reaction vessel.
  • the sulfur may be heated to a predetermined temperature in the reaction vessel prior to contacting it with the olefinic reactant, which may be chilled in order to liquify it and get it into the reactor.
  • the olefin is charged to the reaction zone substantially about as rapidly as it is consumed.
  • compositions hereof may comprise any oleaginous materials that require lubricativ6;-peoperties under extreme pressure conditions and require protection against excessive wear under operating conditions, but normally exhibit insufficient anti-corrosion properties.
  • liquid hydrocarbon oils of lubricating viscosity are suitable for use with the additives of this invention.
  • Lubricant oils improved in accordance with the present invention, may be of any suitable lubricating viscosity.
  • the lubricant compositions may comprise any mineral or synthetic oil of lubricating viscosity or mixtures thereof.
  • the additives of this invention are especially useful in greases and in automotive fluids such as brake fluids and power brake fluids, transmission fluids, power steering fluids, various hydraulic fluids and gear oils and in liquid hydrocarbyl fuels.
  • synthetic oils are desired in preference to refined petroleum or mineral oil they may be employed alone or in combination with a mineral oil. They may also be used as the vehicle or base of grease compositions.
  • Typical synthetic lubricants include polyisobutylene, polybutenes, hydrogenated polydecenes, polypropylene glycol, polyethylene glycol, trimethylol propane esters, neopentyl and pentaerythritol esters of carboxylic acids, di(2-ethylhexyl) sebacate, di(2-ethylhexyl) adipate, dibutyl phthalate, fluorocarbons, silicate esters, silanes, esters of phosphorus-containing acids, liquid ureas, ferrocene derivatives, hydrogenated mineral oils, chain-type polyphenols, siloxanes and silicones (polysifoxanes), alkyl-substituted diphenyl ethers typified by a butyl-substitute
  • the aforementioned additives can be incorporated as additives in grease compositions.
  • mineral oils having a viscosity of at least 40 SSU at 65.6°C (150°F) are useful. Otherwise, those falling within the range of from about 60 SSU to about 6,000 SSU at 37.8°C (100°F) may be employed.
  • the lubricating compositions of the improved greases of the present invention are combined with a grease forming quantity of a thickening agent.
  • a thickening agent for this purpose, a wide variety of materials can be dispersed in the lubricating oil in grease-forming quantities in such degree as to impart to the resulting grease composition the desired consistency.
  • the thickening agents that may be employed in the gease formulation are metal soaps as well as non-soap thickeners, such as surface-modified clays and silicas, aryl ureas, calcium complexes and similar materials.
  • grease thickeners are employed which do not melt or dissolve when used at the required temperature within a particular environment; however, in all other respects, any material which is normally employed for thickening or gelling oleaginous fluids or forming greases may be used in the present invention.
  • the lubricants and fuels of the present invention contain an amount of the sulfurized product effective to improve extreme pressure properties and antiwear and oxidation characteristics. Normally this amount will be 0.01 to 20% and preferably 0.01 to 10% of the total weight of the lubricant.
  • the invention also contemplates the use of other additives in combination with the sulfurized olefin product.
  • additives include, for example, detergents and dispersants of the ash-producing or ashless type, corrosion-inhibiting agents, auxiliary oxidation-inhibiting agents, pour point depression agents, auxiliary extreme pressure agents, color stabilizers and anti-foam agents.
  • This Example was prepared in accordance with the invention using a molar ratio of sulfur to isobutylene of 2.0:1.
  • a 1-gallon stirred autoclave (reactor) was charged with 1,344 g sulfur and 1.2 g n-butylamine (0.05% of the total charge). The reactor was sealed and purged three times with nitrogen to remove oxygen. The reactor was then charged with 1,176 g isobutylene under pressure. The reactor agitator was activated and heated to 160°C and held at that temperaturee until the pressure dropped from its maximum of 4830 kPa (700 psi) to below 520 kPa (75 psi). The reactor was cooled to 100°C and vented to a caustic scrubber. The product was then sparged with nitrogen for three hours at 100°C to remove gaseous contaminates, cooled to less than 30°C and then filtered through diatomaceous earth. The product yield was about 99% of the total reactants charged.
  • This Example is outside the scope of the invention and was prepared using a molar ratio of sulfur to isobutylene of 1.8:1.
  • Example 1 The procedure for Example 1 was used, but a lower sulfur:isobutylene mole ratio was charged. The charge consisted of: 1,300 sulfur, 1.2 g n-butylamine and 1,264 g isobutylene. Maximum pressure achieved was 5790 kPa (840 psi) with a pressure drop to less than 520 kPa (50 psi). Total reaction time was about eleven hours.
  • This Example was prepared using a molar ratio of sulfur to isobutylene of 1.0:1. It accordingly is outside the scope of the invention.
  • Example 2 The procedure for Example 2 was used, but a lower sulfur:isobutylene mole ratio was charged. The charge consisted of: 739 g sulfur, 1.2 g n-butylamine, and 1,249 g isobutylene. The product yield was only 86.5% of reactants charged and minimum pressure did not drop below about 1380 kPa (200 psi), indicating an excess of unreacted olefin which was removed during the venting and sparging steps.
  • Example 1 The products of Example 1, Comparative Example A, and Comparative B were blended into a fully formulated gear lubricant with a standard detergent/antirust/antioxidant package.
  • the EP/antiwear activity was determined by evaluations using CRC (Coordination Research Counsel) L-42 gear testing as well as Four Ball testing.
  • CRC L-42 Test is referred to in U.S. Patent 4,431,552, and is further identified as ASTM D-2782 modified January 1983. Test data is summarized in Table 1.
  • U.S. Patent 3,423,316 A prior art sulfurized olefin prepared in accordance with U.S. Patent 3,703,504, Comparative Example C, was used for comparison with Example 1 of the invention and was evaluated at 3.79% in the identical package and oil blend.
  • U.S. Patent 3,703,504 is directed to a process for producing sulfurized olefins comprising sulfohalogenating an olefin with a sulfur halide to form a sulfohalogenated organic intermediate and thereafter sulfurizing and dehalogenating with aaueous alkali metal monosulfide.
  • Example 1 in accordance with the invention, significantly outperforms the very similar Comparative Example A and even outperforms the product of Example B, even though Comparative Example B was tested at a much higher concentration.
  • Example 1 in accordance with the invention significantly outperforms the very similar Example at 4% concentration. In fact, 2% of Example 1 is almost as good as twice the concentration of Comparative Example C. Also, as can be seen from Table 2, % of Example 1 significantly outperforms Comparative Example A.
  • the products of this invention provide exceptional and highly improved extreme pressure/ antiwear activity coupled with improved copper corrosion performance.
  • the use of the novel sulfurized additives in premium quality automotive and industrial lubricants provide an unexpected significant combination of improved extreme pressure/antiwear activity and anticorrosion characteristics as well as reduced costs.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Lubricants (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Liquid Carbonaceous Fuels (AREA)

Claims (15)

1. Un procédé pour préparer un additif utilisable dans des huiles de viscosité convenable pour le graissage ou des graisses préparées à partir de celles-ci ou dans des combustibles hydrocarbyles liquides, caractérisé en ce qu'il comprend la réaction dans une zone réactionnelle convenable, d'un composé hydrocarbyle oléfinique ayant au moins une double liaison.oléfinique avec du soufre élémentaire selon un rapport molaire de soufre à oléfine de 1,9:1 à 2,1:1, sous des pressions de 2070 kPa à 6200 kPa (300 à 900 psi), à des températures comprises entre 140 et 180°C.pendant une période de temps suffisante et jusqu'à ce que la pression réactionnelle tombe à une valeur comprise entre 340 kPa et 690 kPa (50 et 100 psi), produisant ainsi un additif sulfuré contenant au moins 45% en poids de soufre, de préférence de 45 à 55% en poids de soufre, et consistant essentiellement en une quantité majeure de polysulfures et en une quantité mineure de composés de type dithiol-thione.
2. Le procédé suivant la revendication 1, caractérisé en ce que l'additif produit contient de 44 à 55% en poids de soufre.
3. Le procédé suivant la revendication 1, caractérisé en ce qu'il est un procédé réalisé en une seule étape et dans un seul récipient.
4. Le procédé suivant la revendication 1, caractérisé en ce que la pression varie de 5170 à 5860 kPa (750 à 850 psi), que la température varie de 158 à 165°C et que le rapport molaire du soufre réactif à l'oléfine varie de 1,95:1 à 2,05:1.
5. Le procédé suivant la revendication 4, caractérisé en ce que la température varie de 159 à 161°C.
6. Le procédé suivant la revendication 1, caractérisé en ce qu'il est effectué en présence d'un catalyseur accélérant la vitesse.
7. Le procédé suivant la revendication 6, caractérisé en ce que ce catalyseur accélérant la vitesse est choisi dans le groupe comprenant la n-butylamine, la di-n-butylamine, la n-octylamine, la triéthylamine, la diisopropylamine, la cyclohexylamine, la di-cyclohexylamine, la quinoléine et une argile acide de type attapulgite.
8. Le procédé suivant la revendication 7, caractérisé en ce que ce catalyseur accélérant la vitesse est la n-butylamine.
9. Le procédé suivant la revendication 1, caractérisé en ce que l'oléfine est choisie dans le groupe comprenant l'éthylène, le propylène, le 1-butène, le cis- et le trans-2-butène, l'isobutylène, le diisobutylène, le triisobutylène, le pentène, le cyclopentène, l'hexène, le cyclohexène, l'octène, le 1-décène, le butadiène, l'isoprène, le divinylbenzmène, le pinène, le p-menthène et le limonène.
10. Le procédé suivant la revendication 9, caractérisé en ce que l'oléfine est l'isobutylène.
11. Le procédé suivant la revendication 1, caractérisé en ce que le produit est préparé en l'absence de toute addition de H2S.
12. Une composition de graissage, caractérisée en ce qu'elle comprend une quantité majeure d'une huile de viscosité convenable pour le graissage ou d'une graisse préparée à partir de celle-ci et une quantité mineure suffisante pour conférer à celle-ci une activité de pression extrème/antiusure et des caractéristiques d'anticorrosion, d'un additif préparé selon un procédé suivant l'une quelconque des revendications 1 à 11.
13. La composition de graissage suivant la revendication 12, caractérisée en ce que cette quantité majeure est une huile de viscosité convenable pour le graissage.
14. La composition de graissage suivant la revendication 13, caractérisée en ce que cette huile est choisie parmi des huiles minérales, des huiles de synthèse et leurs mélanges.
15. La composition de graissage suivant la revendication 12, caractérisée en ce que cette quantité majeure est une graisse.
EP86302488A 1985-04-08 1986-04-04 Oléfines sulfurées Expired - Lifetime EP0201197B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT86302488T ATE54663T1 (de) 1985-04-08 1986-04-04 Geschwefelte olefine.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US72125185A 1985-04-08 1985-04-08
US721251 1985-04-08

Publications (2)

Publication Number Publication Date
EP0201197A1 EP0201197A1 (fr) 1986-11-12
EP0201197B1 true EP0201197B1 (fr) 1990-07-18

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EP86302488A Expired - Lifetime EP0201197B1 (fr) 1985-04-08 1986-04-04 Oléfines sulfurées

Country Status (7)

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EP (1) EP0201197B1 (fr)
JP (1) JPS61233092A (fr)
AT (1) ATE54663T1 (fr)
AU (1) AU578353B2 (fr)
CA (1) CA1306757C (fr)
DE (1) DE3672675D1 (fr)
ZA (1) ZA862362B (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7414013B2 (en) 2003-01-30 2008-08-19 Chevron Oronite Company Llc Sulfurized polyisobutylene based wear and oxidation inhibitors

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CA2021224A1 (fr) * 1989-08-03 1991-02-04 Scott Anthony Culley Polyolefines sulfurees solubles dans des huiles lubrifiantes a base de poly(alpha-olefine)
FR2712824B1 (fr) * 1993-11-26 1996-02-02 Inst Francais Du Petrole Procédé de régénération de catalyseur.
FR2727425A1 (fr) * 1994-11-28 1996-05-31 Inst Francais Du Petrole Hydrocarbures ethyleniques sulfures par le soufre elementaire en presence d'eau et d'hydroxyde alcalin ou alcalino-terreux, leur preparation et leur utilisation
FR2727427B1 (fr) * 1994-11-28 1997-04-25 Inst Francais Du Petrole Hydrocarbures ethyleniques sulfures par le soufre elementaire en presence d'alkyleneglycols ou de derives d'alkyleneglycols et d'hydroxydes de metaux alcalins ou alcalino-terreux, leur preparation et leur utilisation
EP0714970A1 (fr) * 1994-11-28 1996-06-05 Institut Français du Pétrole Hydrocarbures éthyléniques sulfurés par le soufre élémentaire en présence d'hydroxydes de métaux alcalins ou alcalino-terreux et en présence de glycols, polyglycols ou de leurs éthers alkyliques et/ou en présence d'eau
FR2729154A1 (fr) * 1995-01-10 1996-07-12 Inst Francais Du Petrole Hydrocarbures ethyleniques sulfures par le soufre elementaire en presence de carbonate ou d'hydrogenocarbonate alcalin, leur preparation et leurs utilisations
US5849677A (en) * 1995-12-27 1998-12-15 Exxon Chemical Patents Inc Sulfurized olefin composition and its method of preparation
FR2808272B1 (fr) 2000-04-28 2002-06-14 Atofina Procede de fabrication d'olefines sulfurees
FR2808273B1 (fr) 2000-04-28 2002-06-14 Atofina Procede de fabrication d'olefines sulfurees
RU2423413C2 (ru) * 2009-07-15 2011-07-10 Учреждение Российской Академии Наук Институт Нефтехимии И Катализа Ран Способ получения серусодержащей присадки
CN104968645A (zh) * 2013-01-29 2015-10-07 巴斯夫欧洲公司 聚硫化物多元醇、其制备及在合成聚氨酯中的用途
US10590012B2 (en) 2014-10-24 2020-03-17 The University Of Tulsa Sulfur-limonene polysulfide
CN104844772B (zh) * 2015-04-28 2017-11-10 中科院广州化学有限公司 一种具有可溶性的单质硫/脂环烯烃共聚物及其制备方法
DE202021002910U1 (de) 2021-09-08 2021-11-26 Metall-Chemie Technologies Gmbh Limonensulfid
CN115873185B (zh) * 2022-10-26 2025-08-26 常州大学 一种含硫聚合物及其制备方法

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US2237625A (en) * 1938-10-07 1941-04-08 Sharples Solvents Corp Sulphurization of sulphur-containing organic conpounds
US3703504A (en) * 1970-01-12 1972-11-21 Mobil Oil Corp Process for producing sulfurized olefins
US3703505A (en) * 1970-08-31 1972-11-21 Mobil Oil Corp Preparation of sulfurized olefins
US3796661A (en) * 1971-07-19 1974-03-12 Texaco Inc Sulfurized triisobutylene
GB1599288A (en) * 1977-07-22 1981-09-30 Cooper & Co Ltd Edwin Sulphurized olefins and their use as lubricant additives
US4153563A (en) * 1978-05-24 1979-05-08 Mobil Oil Corporation Lubricant compositions containing benzotriazole-allyl sulfide reaction products
JPS5538820A (en) * 1978-09-09 1980-03-18 Lubrizol Corp Producing lubricant composition* adding agent concentrate material * and sulfide composition
US4331564A (en) * 1980-10-15 1982-05-25 Ferro Corporation Catalyzing the sulfurization of olefins by tertiary phosphines, and an oil based material containing an additive amount of a sulfurized olefin so produced
CA1208208A (fr) * 1982-05-07 1986-07-22 Kirk E. Davis Compositions a base d'olefine sulfuree

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7414013B2 (en) 2003-01-30 2008-08-19 Chevron Oronite Company Llc Sulfurized polyisobutylene based wear and oxidation inhibitors

Also Published As

Publication number Publication date
ATE54663T1 (de) 1990-08-15
AU578353B2 (en) 1988-10-20
AU5573086A (en) 1986-10-16
EP0201197A1 (fr) 1986-11-12
CA1306757C (fr) 1992-08-25
DE3672675D1 (de) 1990-08-23
ZA862362B (en) 1987-11-25
JPS61233092A (ja) 1986-10-17

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