EP1479752B1 - Emissionsarmes Schmiermittel mit verbessertem Korrosionsschutz - Google Patents

Emissionsarmes Schmiermittel mit verbessertem Korrosionsschutz Download PDF

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Publication number
EP1479752B1
EP1479752B1 EP04252592A EP04252592A EP1479752B1 EP 1479752 B1 EP1479752 B1 EP 1479752B1 EP 04252592 A EP04252592 A EP 04252592A EP 04252592 A EP04252592 A EP 04252592A EP 1479752 B1 EP1479752 B1 EP 1479752B1
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EP
European Patent Office
Prior art keywords
hydrocarbyl
low emission
lubricant composition
emission diesel
diesel lubricant
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.)
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EP04252592A
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English (en)
French (fr)
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EP1479752A2 (de
EP1479752A3 (de
Inventor
Willem Van Dam
Gene Spala
Peter Kleijwegt
Jeroen Van Leeuwen
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Chevron Oronite Technology BV
Chevron Oronite Co LLC
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Chevron Oronite Technology BV
Chevron Oronite Co LLC
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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
    • C10M163/00—Lubricating compositions characterised by the additive being a mixture of a compound of unknown or incompletely defined constitution and a non-macromolecular compound, each of these compounds being essential
    • 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
    • C10M2207/00—Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/10—Carboxylix acids; Neutral salts thereof
    • C10M2207/14—Carboxylix acids; Neutral salts thereof having carboxyl groups bound to carbon atoms of six-membered aromatic rings
    • C10M2207/142—Carboxylix acids; Neutral salts thereof having carboxyl groups bound to carbon atoms of six-membered aromatic rings polycarboxylic
    • 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
    • C10M2207/00—Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/10—Carboxylix acids; Neutral salts thereof
    • C10M2207/14—Carboxylix acids; Neutral salts thereof having carboxyl groups bound to carbon atoms of six-membered aromatic rings
    • C10M2207/144—Carboxylix acids; Neutral salts thereof having carboxyl groups bound to carbon atoms of six-membered aromatic rings containing hydroxy groups
    • 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
    • C10M2215/00—Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant compositions
    • C10M2215/02—Amines, e.g. polyalkylene polyamines; Quaternary amines
    • C10M2215/06—Amines, e.g. polyalkylene polyamines; Quaternary amines having amino groups bound to carbon atoms of six-membered aromatic rings
    • C10M2215/064—Di- and triaryl amines
    • 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
    • C10M2215/00—Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant compositions
    • C10M2215/28—Amides; Imides
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/04—Detergent property or dispersant property
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/12—Inhibition of corrosion, e.g. anti-rust agents or anti-corrosives
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/40—Low content or no content compositions
    • C10N2030/42—Phosphor free or low phosphor content compositions
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/40—Low content or no content compositions
    • C10N2030/43—Sulfur free or low sulfur content compositions
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/40—Low content or no content compositions
    • C10N2030/45—Ash-less or low ash content
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/50—Emission or smoke controlling properties
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2040/00—Specified use or application for which the lubricating composition is intended
    • C10N2040/25—Internal-combustion engines
    • C10N2040/252—Diesel engines
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2060/00—Chemical after-treatment of the constituents of the lubricating composition
    • C10N2060/14—Chemical after-treatment of the constituents of the lubricating composition by boron or a compound containing boron

Definitions

  • the present invention relates to engine lubricants for low emission diesel engines equipped with exhaust gas after-treatment systems that can be sensitive to lubricant constituents.
  • Some of these types of after-treatment systems are known to be sensitive to fuel and lubricant constituents.
  • lubricants have been developed that feature low levels of ash, sulfur, and phosphorus. Ash, sulfur and phosphorus are present in many conventional lubricant additives such as detergents and zinc-dithiophosphates.
  • the low emission diesel lubricant (“LEDL”) of the present invention has been developed using new components and component combinations.
  • the new LEDL additive formulation described in this invention solves the corrosion problem while maintaining good performance in other areas.
  • the formulation can be used in a finished oil blended with Group 1, 2, 3, or 4 base stocks or combinations thereof.
  • the finished oil using this formulation may or may not contain a viscosity modifier, pour point depressant, and any ester added for solubility.
  • JP11-181463 teaches a gear oil that contains (a) 0.5-3 mass % of primary zinc dithiophosphoric acid, (b) 1.2-4 mass % of alkaline earth metal type detergent- dispersant, (c) 1.5-10 mass % of bis type alkenyl succinic acid imide or its derivative, (d) 0.3-3 mass % of amine salt of phosphate ester (e) 0.05-5 mass % of one or more sulfur compounds, and (f) a base oil that has less than 0.1 wt-% sulfur.
  • non-sulfur containing detergents may be employed.
  • the preparation of both sulfur containing and non-sulfur containing hydrocarbyl phenates and hydrocarbyl salicylates is well known in the art.
  • U.S. Pat. No. 3,036,971 discloses preparing detergent dispersant additives based on sulfurized alkylphenates of high basicity alkaline earth metals. These additives are prepared by sulfurization of an alkylphenol, neutralization of the sulfurized alkylphenol with an alkaline earth metal base, then super-alkalization by carbonation of the alkaline earth metal base dispersed in the sulfurized alkylphenate.
  • French patent 1,563,557 discloses detergent additives based on sulfurized calcium alkylsalicylates. These additives are prepared by carboxylation of a potassium alkylphenate, exchange with calcium chloride, then sulfurization of the calcium alkylsalicylate obtained with sulfur in the presence of lime, a carboxylic acid and an alkylene glycol or alkyl ether of alkylene glycol.
  • French patent application 2,625,220 discloses superalkalized detergent-dispersant additives based on alkylphenates and alkylsalicylates. These additives are prepared by neutralization of an alkylphenol with an alkaline earth metal base in the presence of an acid and a solvent, distillation of the solvent, carboxylation, sulfurization and superalkalization by sulfur and an alkaline earth metal base in the presence of glycol and solvent, followed by carbonation and filtration.
  • US Patent No. 5,808,145 discloses a process that is able to improve substantially the performance of alkylphenate/alkylsalicylate additives, particularly in the tests relating to foaming, compatibility and dispersion in a new oil, and in the tests of stability towards hydrolysis.
  • This process comprises neutralization with alkaline earth metal base of a mixture of linear and branched alkylphenols in the presence of a carboxylic acid, carboxylation by the action of carbon dioxide of the alkylphenate, followed by sulfurization and super-alkalization, then carbonation, distillation, filtration, and degassing in air.
  • European Patent Application Publication No. 0933417 discloses an unsulfurized, alkali metal-free detergent-dispersant additive, comprising a mixture of alkaline earth metal salts (alkylphenate/alkylsalicylate) and unreacted alkylphenol. This additive improves antioxidant properties, high temperature deposit control, and black sludge control.
  • U.S. Patent Nos. 6,162,770 and 6,262,001 teach an unsulfurized, alkali metal-free, detergent-dispersant composition having from 40% to 60% alkylphenol, from 10% to 40% alkaline earth alkylphenate, and from 20% to 40% alkaline earth single-aromatic-ring alkylsalicylate, and a process for preparing the same.
  • This composition may have an alkaline earth double-aromatic-ring alkylsalicylate as long as the mole ratio of single-ring alkylsalicylate to double-aromatic-ring alkylsalicylate is at least 8:1.
  • This composition may be produced by the three-step process involving neutralization of alkylphenols, carboxylation of the resulting alkylphenate, and filtration of the product of the carboxylation step.
  • the detergent-dispersant produced by the method can be used in an engine lubricating composition to improve antioxidant properties, high temperature deposit control, and black sludge control.
  • EP-A-1167497 describes a lubricating oil composition having a low P content of 0.01 to 0.1 wt.%, and a sulfated ash of 0.1 to 1 wt.%, which is composed of a) a major amount of mineral base oil having a low S content of at most 0.1 wt.%; b) an ashless alkenyl or alkyl-succinimide dispersant; c) a metal-containing detergent (non-sulfurized alkali metal or alkaline earth metal salt of an alkylsalicylic acid and/or non-sulfurized alkali metal or alkaline earth metal salt of an alkylphenol derivative having a Mannich base structure); d) Zn-DTP; e) an oxidation inhibitor (phenol compound and/or amine compound) and wherein the sulfur content is 0.01 to 0.3 wt %.
  • the lubricating oil composition shows good high temperature detergency notwithstanding its low S,
  • EP-A-0675191 describes a petroleum additive containing an alkaline earth metal salt of an aromatic hydroxy-carboxylic acid, wherein the alkaline earth metal salt is substantially free of an alkali metal and the ratio of salicylic acid skeleton to total benzene nuclei is 0.4:1 to 0.95:1.
  • Also described is a process for producing an alkaline earth metal salt of an aromatic hydroxy-carboxylic acid involving: i) reacting an alkaline earth metal salt of a phenol with carbon dioxide; ii) reacting the resulting free phenol with an alkaline earth metal reagent in the presence of 2.0 to 15.0 mol of a dihydric alcohol per 1 mol of the alkaline earth metal reagent (when no water is added) or in the presence of 0.01 to 10.0 mol of water and 1.5 to 10.0 mol of a dihydric alcohol each per 1 mol of the alkaline earth metal reagent; and iii) repeating the reaction with carbon dioxide.
  • EP-A-0370555 relates to a process for the separation of a phenol from a mixture obtained by the carboxylation of the phenol and containing phenol, phenolate and the carboxylation products therefrom characterized in that the separation is carried out by selectively absorbing the phenol into the wall of a membrane, solubilizing the phenol in the membrane matrix, diffusing the phenol through the membrane and desorbing the phenol from the other wall.
  • the LEDL of the current invention is a low sulfur, ash, and phosphorus lubricant with superior corrosion performance.
  • the present invention provides a novel low emission diesel lubricant, or LEDL, comprising low levels of ash, sulfur and phosphorus, and LEDL also contains an unsulfurized, carboxylate-containing hydroxy-aromatic surfactant-based detergent-dispersant additive comprising a mixture of alkaline earth metal salts (hydrocarbyl phenate/hydrocarbyl salicylate) and a reduced amount of unreacted hydrocarbyl phenols.
  • the present invention also relates to additive packages, concentrates and finished oil compositions comprising the same.
  • Said hydrocarbyl salicylate is primarily single-aromatic-ring hydrocarbyl salicylate.
  • Said unsulfurized, carboxylate-containing additive containing said mixture in which said hydrocarbyl salicylate is primarily single-aromatic-ring hydrocarbyl salicylate improves antioxidant properties, high temperature deposit control, BN retention, corrosion control and black sludge control in lubricating oils.
  • This invention is also directed, in part, to methods of preparing and using said novel LEDL.
  • the LEDL of the present invention has the following composition: a major amount of a base oil of lubricating viscosity, a hydroxy-aromatic surfactant-based detergent-dispersant additive containing less than 40 weight percent ("wt. %") free hydrocarbyl phenol; a dispersant; a wear inhibitor; and from 0 wt. % to 1.2 wt. % ash (as measured by ASTM D874); from 0.1 wt. % to 0.5 wt. % sulfur; and from 0.02 wt.% to 0.1 wt. % phosphorus.
  • wt. % weight percent
  • the LEDL of the present invention comprise a major amount of a base oil of lubricating viscosity and from 0.4 wt. % to 1.0 wt. % ash; from 0.05 wt. % to 0.3 wt. % sulfur; and from 0.02 wt. % to 0.08 wt. % phosphorus. More preferably, said LEDL comprises a major amount of a base oil of lubricating viscosity and less than 1.0 wt. % ash; less than 0.3 wt. % sulfur; and less than 0.08 wt. % phosphorus.
  • said LEDL comprises a major amount of a base oil of lubricating viscosity and from 0.4 wt. % to 1.0 wt. % ash; from 0.05 wt. % to 0.15 wt. % sulfur; and from 0.02 wt. % to 0.08 wt. % phosphorus.
  • the hydroxy-aromatic surfactant-based detergent-dispersant additive is unsulfurized.
  • Said additive is a carboxylate-containing additive.
  • Said additive comprises from 10 to 50% alkaline earth metal hydrocarbyl phenate; from 15 to 60% alkaline earth metal single-aromatic-ring hydrocarbyl salicylate; and from 0% to 50% organic diluent; and alkaline earth metal double-aromatic-ring hydrocarbyl salicylate; wherein the mole ratio of single-aromatic-ring hydrocarbyl salicylate to double-aromatic-ring hydrocarbyl salicylate is at least 8:1.
  • the LEDL comprises from 1.8 wt. % to 5.5 wt. % of said unsulfurized, carboxylate-containing, hydroxy-aromatic, surfactant-based, detergent-dispersant additive
  • said LEDL further comprises from 1.0 wt. % to 4.0 wt. % borated dispersant; from 0.2 wt. % to 1.1 wt. % wear inhibitor; and from 0 wt. % to 0.5 wt. % corrosion inhibitor.
  • said dispersant is a succinimide; said wear inhibitor is zinc dithiophosphate; and said corrosion inhibitor is a neutralized terephthalic acid.
  • said LEDL also comprises from 3.0 wt. % to 8.0 wt. % non-borated dispersant; from 0.6 wt. % to 1.4 wt. % calcium-sulfonate; from 0.1 wt.
  • % to 0.5 wt. % molybdenum anti-oxidant from 0 wt. % to 1.0 wt. % phenolic anti-oxidant; from 0.1 wt. % to 1.0 wt. % aminic anti-oxidant; from 0 wt. % to 6.0 wt. % dispersant olefin-copolymer; and from 0 to 25 ppm foam inhibitor.
  • the LEDL of the present invention will contain no sulfur-containing detergent.
  • the hydroxy-aromatic surfactant-based detergent-dispersant additive comprises from 0 to 35% free hydrocarbyl phenol; preferably from 0 to 30% free hydrocarbyl phenol; more preferably from 0 to 20% free hydrocarbyl phenol; most preferably from 0 to 15% free hydrocarbyl phenol.
  • the LEDL of the present invention may advantageously comprise a major amount of a base oil of lubricating viscosity and from 0.4 wt. % to 1.0 wt. % ash; from 0.2 wt. % to 0.4 wt. % sulfur; from 0.04 wt. % to 0.08 wt. % phosphorus; and from 2.7 wt. % to 5.5 wt. % of said unsulfurized carboxylate-containing additive.
  • Said LEDL may further comprise from 1.0 wt. % to 4.0 wt. % borated dispersant; and from 0 wt. % to 0.5 wt. % corrosion inhibitor.
  • said LEDL also comprises from 3.0 wt. % to 8.0 wt. % non-borated dispersant; from 0.6 wt. % to 1.4 wt. % calcium-sulfonate; from 0.2 wt. % to 1.1 wt. % zinc dithiophosphate; from 0.1 wt. % to 0.5 wt. % molybdenum anti-oxidant; from 0 wt. % to 1.0 wt. % phenolic anti-oxidant; from 0.1 wt. % to 1.0 wt. % aminic anti-oxidant; from 0 wt. % to 6.0 wt. % dispersant olefin-copolymer; and from 0 to 25 ppm foam inhibitor.
  • the sulfur content of said LEDL is from 0.1 wt. % to 0.3 wt.%.
  • the effective corrosion inhibiting amount of an unsulfurized carboxylate-containing hydroxy-aromatic surfactant-based detergent-dispersant additive is prepared by a method comprising: (a) neutralization of hydrocarbyl phenols using an alkaline earth base in the presence of a promoter, to produce a hydrocarbyl phenate; (b) carboxylation of the hydrocarbyl phenate obtained in step (a) using carbon dioxide under carboxylation conditions sufficient to convert at least 20 mole% of the starting hydrocarbyl phenols to hydrocarbyl salicylate; and (c) separation of at least about 10% of the starting hydrocarbyl phenols from the product produced in step (b) to produce said additive, wherein said composition contains: from 0 wt. % to 1.2 wt. % ash; from 0.1 wt. % to 0.5 wt. % sulfur; and from 0.02 wt. % to 0.1 wt. % phosphorus.
  • said promoter comprises at least one carboxylic acid containing from one to four carbon atoms
  • said neutralization step is carried out in the absence of alkali base, in the absence of dialcohol, and in the absence of monoalcohol.
  • the neutralization step is followed by carboxylation of the hydrocarbyl phenate produced in the neutralization step; and separation of the starting hydrocarbyl phenols from the product of the carboxylation step.
  • the hydrocarbyl phenols may comprise linear and /or branched hydrocarbyl constituents.
  • the hydrocarbyl phenols may be made up entirely of linear hydrocarbyl phenol, entirely of branched hydrocarbyl phenol, or a mixture of both.
  • the hydrocarbyl phenols contain up to 85% of linear hydrocarbyl phenol in mixture with at least 15% of branched hydrocarbyl phenol in which the branched hydrocarbyl radical contains at least nine carbon atoms.
  • the hydrocarbyl phenols are alkylphenols which contain from 35% to 85% of linear alkylphenol in mixture with from 15% to 65% of branched alkylphenol. The ratio of branched versus linear alkylphenol is given by weight.
  • the linear hydrocarbyl radical contains 12 to 40 carbon atoms, more preferably from 18 to 30 carbon atoms, and, if branched hydrocarbyl phenols are present, the branched hydrocarbyl radical contains at least 9 carbon atoms, preferably from 9 to 24 carbon atoms, more preferably 10 to 15 carbon atoms.
  • the alkaline earth base is selected from the group consisting of calcium oxide, calcium hydroxide, magnesium oxide, and mixtures thereof.
  • the carboxylic acid is a mixture of formic acid and acetic acid, more preferably a 50/50 by weight mixture of formic and acetic acid.
  • the neutralization step is carried out at a temperature of at least 200°C, more preferably at least 215°C.
  • the pressure is reduced gradually below atmospheric in order to remove the water of reaction, in the absence of any solvent that may form an azeotrope with water.
  • the quantities of reagents used correspond to the following molar ratios:
  • the neutralization step is carried out at a temperature of at least 240°C with a gradual reduction in pressure below atmospheric so as to reach a pressure of no more than 7,000 Pa (70 mbars) at 240°C.
  • the hydrocarbyl phenate obtained in the neutralization step is carboxylated in order to convert at least 20 mole % of the starting hydrocarbyl phenols to hydrocarbyl salicylate using carbon dioxide under carboxylation conditions.
  • at least 22 mole % of the starting hydrocarbyl phenols is converted, and this conversion occurs at a temperature between 180°C and 240°C, under a pressure within the range of from above atmospheric pressure to 15 ⁇ 10 5 Pa (15 bars) for a period of one to eight hours.
  • the starting hydrocarbyl phenols are alkylphenols and at least 25 mole % of the starting alkylphenols is converted to alkylsalicylate using carbon dioxide at a temperature equal to or greater than 200°C, under a pressure of 4 ⁇ 10 5 Pa (4 bars).
  • the hydrocarbyl salicylate produced in the carboxylation step comprises both single-aromatic-ring hydrocarbyl salicylate and double-aromatic-ring hydrocarbyl salicylate.
  • the mole ratio of single-aromatic-ring hydrocarbyl salicylate to double-aromatic-ring hydrocarbyl salicylate is at least 8:1.
  • the product of the carboxylation step is then filtered to remove any sediment formed in the carboxylation step.
  • the product of the carboxylation step is then subjected to a separation procedure such as solvent extraction, distillation, membrane filtration, and the like wherein at least 10% of the starting hydrocarbyl phenols are separated from the product of the carboxylation step.
  • a separation procedure such as solvent extraction, distillation, membrane filtration, and the like wherein at least 10% of the starting hydrocarbyl phenols are separated from the product of the carboxylation step.
  • at least 30% up to 55% of the starting hydrocarbyl phenols are separated. More preferably, at least 45% to 50% of the starting hydrocarbyl phenols are separated from the product of the carboxylation step.
  • hydrocarbyl phenols may advantageously be recycled to be used as starting materials in the process of the present invention or in any other process.
  • the separation step is performed via distillation, more preferably via falling film distillation or short path distillation, most preferably via wiped film evaporator distillation.
  • Said distillation is carried out at a temperature of from 150°C to 250°C and at a pressure of 0.1 to 4 mbar; more preferably from 190°C to 230°C and at 0.5 to 3 mbar; most preferably from 195°C to 225°C and at a pressure of 1 to 2 mbar.
  • the unsulfurized, carboxylate-containing hydroxy-aromatic surfactant-based detergent-dispersant additive may advantageously be blended with an effective viscosity improving amount of organic diluent.
  • an effective viscosity improving amount of organic diluent Preferably, enough diluent is added so that said diluent makes up from 10% to 50% by weight of the blended product. More preferably, said diluent makes up from 20% to 50% by weight of the blended product.
  • Suitable diluents include Group 1 or Group 2 base oils such as 100N base oil; organic solvents such as pentane, heptane, benzene, toluene and the like; and other suitable organic compounds such as hydrocarbyl phenols which may advantageously be recycled from the distillation step of the present invention.
  • the unsulfurized, carboxylate-containing hydroxy-aromatic surfactant-based detergent-dispersant additive produced by the above described method has the following composition:
  • Said unsulfurized, carboxylate-containing hydroxy-aromatic surfactant-based detergent-dispersant additive also comprises an alkaline earth metal double-aromatic-ring hydrocarbyl salicylate, but the mole ratio of single-aromatic-ring hydrocarbyl salicylate to double-aromatic-ring hydrocarbyl salicylate will be at least 8:1.
  • the LEDL of the present invention may be used as an engine lubricating oil composition containing a major part of lubricating oil, a hydroxy-aromatic surfactant-based detergent-dispersant additive and preferably at least one other additive.
  • other additives include metal-containing detergents; ashless dispersants; borated and non-borated dispersants, including ethylene carbonate treated dispersants; low overbased ("LOB”), medium overbased (“MOB”), high overbased (“HOB”) and high-high overbased (“HHOB”) calcium sulfonates; oxidation inhibitors, rust inhibitors, demulsifiers, extreme pressure agents, friction modifiers, multifunctional additives, viscosity index improvers, pour point depressants, and foam inhibitors.
  • LOB low overbased
  • MOB medium overbased
  • HOB high overbased
  • HHOB high-high overbased
  • the high temperature deposit control performance, corrosion control and oxidation inhibition performance of a lubricating oil can be improved by adding to the lubricating oil an effective amount of the LEDL composition of the present invention. Accordingly, the corrosion protection in any internal combustion engine may be improved by contacting said engine with the LEDL of the current invention.
  • the present invention provides a LEDL composition comprising low levels of ash, sulfur and phosphorus.
  • said LEDL contains an unsulfurized, carboxylate-containing hydroxy-aromatic surfactant-based detergent-dispersant additive comprising hydrocarbyl phenol, alkaline earth metal hydrocarbyl phenate, and alkaline earth metal single-aromatic-ring hydrocarbyl salicylate useful for improving BN retention, corrosion performance, bulk oxidation, high temperature deposit control, black sludge control, thermal oxidation stability, and other properties of a lubricating oil.
  • an unsulfurized, carboxylate-containing hydroxy-aromatic surfactant-based detergent-dispersant additive comprising hydrocarbyl phenol, alkaline earth metal hydrocarbyl phenate, and alkaline earth metal single-aromatic-ring hydrocarbyl salicylate useful for improving BN retention, corrosion performance, bulk oxidation, high temperature deposit control, black sludge control, thermal oxidation stability, and other properties of
  • hydrocarbyl phenols are neutralized in the presence of a promoter.
  • said hydrocarbyl phenols are neutralized using an alkaline earth metal base in the presence of at least one C 1 to C 4 carboxylic acid.
  • this reaction is carried out in the absence of alkali base, and in the absence of dialcohol or monoalcohol.
  • the hydrocarbyl phenols may contain up to 100% linear hydrocarbyl groups, up to 100% branched hydrocarbyl groups, or both linear and branched hydrocarbyl groups.
  • the linear hydrocarbyl group if present, is alkyl
  • the linear alkyl radical contains 12 to 40 carbon atoms, more preferably 18 to 30 carbon atoms.
  • the branched hydrocarbyl radical if present, is preferably alkyl and contains at least nine carbon atoms, preferably 9 to 24 carbon atoms, more preferably 10 to 15 carbon atoms.
  • the hydrocarbyl phenols contain up to 85% of linear hydrocarbyl phenol (preferably at least 35% linear hydrocarbyl phenol) in mixture with at least 15% of branched hydrocarbyl phenol.
  • alkylphenol containing at least 35% of long-chain linear alkylphenol is particularly attractive because a long linear alkyl chain promotes the compatibility and solubility of the additives in lubricating oils.
  • the presence of relatively heavy linear alkyl radicals in the alkylphenols can make the latter less reactive than branched alkylphenols, hence the need to use harsher reaction conditions to bring about their neutralization by an alkaline earth metal base.
  • Branched alkylphenols can be obtained by reaction of phenol with a branched olefin, generally originating from propylene. They consist of a mixture of monosubstituted isomers, the great majority of the substituents being in the para position, very few being in the ortho position, and hardly any in the meta position. That makes them relatively more reactive towards an alkaline earth metal base, since the phenol function is practically devoid of steric hindrance.
  • linear alkylphenols can be obtained by reaction of phenol with a linear olefin, generally originating from ethylene. They consist of a mixture of monosubstituted isomers in which the proportion of linear alkyl substituents in the ortho, para, and meta positions is more uniformly distributed. This makes them less reactive towards an alkaline earth metal base since the phenol function is less accessible due to considerable steric hindrance, due to the presence of closer and generally heavier alkyl substituents.
  • linear alkylphenols may contain alkyl substituents with some branching which increases the amount of para substituents and, resultantly, increases the relative reactivity towards alkaline earth metal bases.
  • the alkaline earth metal bases that can be used for carrying out this step include the oxides or hydroxides of calcium, magnesium, barium, or strontium, and particularly of calcium oxide, calcium hydroxide, magnesium oxide, and mixtures thereof.
  • slaked lime calcium hydroxide is preferred.
  • the promoter used in this step can be any material that enhances neutralization.
  • the promoter may be a polyhydric alcohol, dialcohol, monoalcohol, ethylene glycol or any carboxylic acid.
  • a carboxylic acid is used. More preferably, C 1 to C 4 carboxylic acids are used in this step including, for example, formic, acetic, propionic and butyric acid, and may be used alone or in mixture.
  • a mixture of acids is used, most preferably a formic acid/acetic acid mixture.
  • the molar ratio of formic acid/acetic acid should be from 0.2:1 to 100:1, preferably between 0.5:1 and 4:1, and most preferably 1:1.
  • the carboxylic acids act as transfer agents, assisting the transfer of the alkaline earth metal bases from a mineral reagent to an organic reagent.
  • the neutralization operation is carried out at a temperature of at least 200°C, preferably at least 215°C, and more preferably at least 240°C
  • the pressure is reduced gradually below atmospheric in order to distill off the water of reaction. Accordingly the neutralization should be conducted in the absence of any solvent that may form an azeotrope with water.
  • the pressure is reduced to no more than 7,000 Pa (70 mbars).
  • the hydrocarbyl phenate obtained is kept for a period not exceeding fifteen hours at a temperature of at least 215°C and at an absolute pressure of between 5,000 and 10 5 Pa (between 0.05 and 1.0 bar). More preferably, at the end of this neutralization step the hydrocarbyl phenate obtained is kept for between two and six hours at an absolute pressure of between 10,000 and 20,000 Pa (between 0.1 and 0.2 bar).
  • the neutralization reaction is carried out without the need to add a solvent that forms an azeotrope with the water formed during this reaction.
  • the carboxylation step is conducted by simply bubbling carbon dioxide into the reaction medium originating from the preceding neutralization step and is continued until at least 20 mole % of the starting hydrocarbyl phenols is converted to hydrocarbyl salicylate (measured as salicylic acid by potentiometric determination). It must take place under pressure in order to avoid any decarboxylation of the alkylsalicylate that forms.
  • At least 22 mole % of the starting hydrocarbyl phenols is converted to hydrocarbyl salicylate using carbon dioxide at a temperature of between 180°C and 240°C, under a pressure within the range of from above atmospheric pressure to 15 ⁇ 10 5 Pa (15 bars) for a period of one to eight hours.
  • At least 25 mole % of the starting hydrocarbyl phenols is converted to hydrocarbyl salicylate using carbon dioxide at a temperature equal to or greater than 200°C under a pressure of 4 ⁇ 10 5 Pa (4 bars).
  • the product of the carboxylation step may advantageously be filtered.
  • the purpose of the filtration step is to remove sediments, and particularly crystalline calcium carbonate, which might have been formed during the preceding steps, and which may cause plugging of filters installed in lubricating oil circuits.
  • At least 10% of the starting hydrocarbyl phenol is separated form the product of the carboxylation step.
  • the separation is accomplished using distillation. More preferably, the distillation is carried out in a wiped film evaporator at a temperature of from 150°C to 250°C and at a pressure of 0.1 to 4 mbar; more preferably from 190°C to 230°C and at 0.5 to 3 mbar; most preferably from 195°C to 225°C and at a pressure of 1 to 2 mbar.
  • At least 10% of the starting hydrocarbyl phenol is separated. More preferably, at least 30% of the starting hydrocarbyl phenol is separated. Most preferably, up to 55% of the starting hydrocarbyl phenol is separated.
  • the separated hydrocarbyl phenol may then be recycled to be used as starting materials in the novel process or in any other process.
  • the unsulfurized, carboxylate-containing hydroxy-aromatic surfactant-based detergent-dispersant additive formed by the above process can be characterized by its unique composition, with much more alkaline earth metal single-aromatic-ring hydrocarbyl salicylate and less hydrocarbyl phenol than produced by other routes.
  • the unsulfurized, carboxylate-containing additive has the following composition;
  • this unsulfurized, carboxylate-containing additive composition can be characterized by having only minor amounts of an alkaline earth metal double-aromatic-ring alkylsalicylates.
  • the mole ratio of single-aromatic-ring alkylsalicylate to double-aromatic-ring alkylsalicylate is at least 8:1.
  • Out-of-aromatic-ring-plane C-H bending vibrations were used to characterize the unsulfurized carboxylate-containing hydroxy-aromatic surfactant-based detergent-dispersant additive employed in the present invention.
  • Infrared spectra of aromatic rings show strong out-of-plane C-H bending transmittance band in the 675-870 cm -1 region, the exact frequency depending upon the number and location of substituents.
  • transmittance band occurs at 735-770 cm -1 .
  • transmittance band occurs at 810-840 cm -1 .
  • Infrared spectra of reference chemical structures relevant to the present invention indicate that the out-of-plane C-H bending transmittance band occurs at 750 ⁇ 3 cm -1 for ortho-alkylphenols, at 760 ⁇ 2 cm -1 for salicylic acid, and at 832 ⁇ 3 cm -1 for para-alkylphenols.
  • Alkaline earth alkylphenates known in the art have infrared out-of-plane C-H bending transmittance bands at 750 ⁇ 3 cm -1 and at 832 ⁇ 3 cm -1 .
  • Alkaline earth alkylsalicylates known in the art have infrared out-of-plane C-H bending transmittance bands at 763 ⁇ 3 cm -1 and at 832 ⁇ 3 cm -1 .
  • the unsulfurized carboxylate-containing hydroxy-aromatic surfactant-based detergent-dispersant additive employed in the present invention shows essentially no out-of-plane C-H bending vibration at 763 ⁇ 3 cm -1 , even though there is other evidence that alkylsalicylate is present. This particular characteristic has not been fully explained. However, it may be hypothesized that the particular structure of the single aromatic ring alkylsalicylate prevents in some way this out-of-plane C-H bending vibration. In this structure, the carboxylic acid function is engaged in a cyclic structure, and thus may generate increased steric hindrance in the vicinity of the aromatic ring, limiting the free motion of the neighbor hydrogen atom.
  • the unsulfurized carboxylate-containing hydroxy-aromatic surfactant-based detergent-dispersant additive employed in the present invention can thus be characterized by having a ratio of infrared transmittance band of out-of-plane C-H bending at about 763 ⁇ 3 cm -1 to out-of-plane C-H bending at 832 ⁇ 3 cm -1 of less than 0.1:1.
  • the unsulfurized, carboxylate-containing hydroxy-aromatic surfactant-based detergent-dispersant additive formed by the above method, being non-sulfurized, would provide improved high temperature deposit control performance over sulfurized products while meeting the low sulfur requirements for LEDLs. Being alkali-metal free, this additive can be employed as a detergent-dispersant in applications, such as marine engine oils, where the presence of alkali metals have proven to have harmful effects.
  • Hydroxy-aromatic surfactant-based detergent-dispersant additives are well known in the art. Examples of such additives include phenates, phenate-carboxylates, salicylates, carboxy-stearates, and the unsulfurized carboxylate-containing additive described above.
  • the phenates which may be used in the present invention are typically hydrocarbyl substituted phenates in which the hydrocarbyl substituent or substituents of the phenate are preferably one or more alkyl group, either branched or unbranched. Suitable alkyl groups contain from 4 to 50, preferably from 9 to 28 carbon atoms. Particularly suitable alkyl groups are C 12 groups derivable from propylene tetramer.
  • the hydrocarbyl substituted phenates are typically sulfurized.
  • overbased sulfurized alkylphenates of alkaline earth metals are prepared by neutralizing a sulfurized alkylphenol with an alkaline earth base in the presence of a dilution oil, a glycol, and halide ions, the glycol being present in the form of a mixture with an alcohol having a boiling point above 150 °C, removing alcohol, glycol, water, and sediment, carbonating the reaction medium with CO 2 in the presence of halide ions, and again removing alcohol, glycol, water, and sediment.
  • an overbased, sulfurized hydrocarbyl phenate is prepared by a process comprising the steps of:
  • the alkaline earth bases useful in the above process include the oxides and hydroxides of barium, strontium, and calcium, particularly lime.
  • Alcohols with a boiling point above 150°C useful in the process include alcohols of C 6 to C 14 such as ethylhexanol, oxoalcohol, decylalcohol, tridecylalcohol; alkoxyalcohols such as 2-butoxyethanol, 2-butoxypropanol; and methyl ethers of dipropylene glycol.
  • the amines useful in the process include polyaminoalkanes, preferably polyaminoethanes, particularly ethylenediamine, and aminoethers, particularly tris(3-oxa-6-amino-hexyl)amine.
  • the glycols useful in the process include alkylene glycols, particularly ethylene glycol.
  • the halide ions employed in the process are preferably Cl - ions which may be added in the form of ammonium chloride or metal chlorides such as calcium chloride or zinc chloride.
  • the dilution oils suitable for use in the above process include naphthenic oils and mixed oils and preferably paraffinic oils such as neutral 100 oil.
  • the quantity of dilution oil used is such that the amount of oil in the final product constitutes from about 25% to about 65% by weight of the final product, preferably from about 30% to about 50%.
  • the phenate-carboxylates which may be used in the present invention are typically hydrocarbyl substituted phenate-carboxylates in which the hydrocarbyl substituent or substituents of the phenate are preferably one or more alkyl group, either branched or unbranched. Suitable alkyl groups contain from 4 to 50, preferably from 9 to 28 carbon atoms. Particularly suitable alkyl groups are C 12 groups derivable from propylene tetramer.
  • the hydrocarbyl substituted phenate-carboxylates may be sulfurized or unsulfurized.
  • the overbased hydrocarbyl phenate-carboxylate is prepared from an overbased hydrocarbyl phenate which has been treated, either before, during, or subsequent to overbasing, with a long-chain carboxylic acid (preferably stearic acid), anhydride or salt thereof. That process comprises contacting a mixture of a hydrocarbyl phenate, at least one solvent, metal hydroxide, aqueous metal chloride, and an alkyl polyhydric alcohol containing from one to five carbon atoms, with carbon dioxide under overbasing reaction conditions.
  • an aqueous metal chloride instead of a solid metal chloride, reduces the viscosity of the product.
  • the metals are alkaline earth metals, most preferably calcium.
  • the alkyl polyhydric alcohol is ethylene glycol.
  • the overbased hydrocarbyl phenate-carboxylate is produced by overbasing a hydrocarbyl phenate and treating the phenate (before, during, or after overbasing) with a long-chain carboxylic acid (preferably stearic acid), anhydride or salt thereof.
  • overbasing reaction conditions include temperatures of from 250 to 375°F (120 to 191°C) at approximately atmospheric pressure.
  • the overbased hydrocarbyl phenate is a sulfurized alkylphenate.
  • the metal is an alkaline earth metal, more preferably calcium.
  • the alkyl polyhydric alcohol is ethylene glycol.
  • the carboxylate treatment (treatment with long-chain carboxylic acid, anhydride, or salt thereof) can occur before, during, or after the overbasing step. It is unimportant when the treatment with long-chain carboxylic acid, anhydride, or salt thereof occurs relative to the overbasing step.
  • the phenate can be sulfurized or unsulfurized. Preferably, the phenate is sulfurized. If the phenate is sulfurized, the sulfurization step can occur anytime prior to overbasing. More preferably, the phenate is sulfurized before the overbasing step but after the carboxylate treatment.
  • salicylates which may be used in the present invention include medium and high overbased salicylates including salts of polyvalent or monovalent metals, more preferably monovalent, most preferably calcium.
  • medium overbased (MOB) is meant to include salicylates with a TBN of about 31 to 170.
  • High overbased (HOB) is meant to include salicylates with a TBN from about 171 to 400.
  • High-high overbased (HHOB) is meant to include salicylates with a TBN over 400.
  • salicylates may be prepared, for instance, starting from phenol, ortho-alkylphenol, or para-alkylphenol, by alkylation, carboxylation and salt formation.
  • the alkylating agent preferably chosen is an olefin or a mixture of olefins with more than 12 carbon atoms to the molecule.
  • Acid-activated clays are suitable catalysts for the alkylation of phenol and ortho- and para- alkylphenol.
  • the amount of catalyst employed is, in general, 1 - 10 wt%, in particular, 3-7 wt%, referred to the sum of the amounts by weight of alkylating agent and phenol to be alkylated.
  • the alkylation may be carried out at temperatures between 100 and 250°C, in particular, between 125 and 225°C.
  • the alkylphenols prepared via the phenol or ortho- or para-alkylphenol route may be converted into the corresponding alkylsalicylic acids by techniques well known in the art. For instance, the alkylphenols are converted with the aid of an alcoholic caustic solution into the corresponding alkylphenates and the latter are treated with CO 2 at about 140°C and a pressure of 10 to 30 atmospheres (10.13 to 30.40 bar). From the alkylsalicylates so obtained, the alkylsalicylic acids may be liberated with the aid of, for example, 30% sulfuric acid.
  • the alkylsalicylic acids may be treated with an excess amount of a metal compound, for instance, calcium in the form of Ca(OH) 2 .
  • alkylsalicylic acids may be treated with 4 equivalents of calcium in the form of Ca(OH) 2 with introduction of 1.6 equivalents of CO 2 .
  • carboxy-stearates which may be used in the present invention are typically alkaline earth metal single-aromatic-ring hydrocarbyl salicylates that have been treated with a long-chain carboxylic acid, anhydride or salt thereof.
  • the carboxy-stearate is prepared from a mixture of alkaline earth metal single-aromatic-ring salicylate, at least one solvent, and alkaline earth metal hydroxide.
  • the mixture is overbased by contacting the mixture with carbon dioxide in the presence of an alkyl polyhydric alcohol, wherein the alkyl group of the alcohol has from one to five carbon atoms.
  • alkyl polyhydric alcohol is ethylene glycol.
  • the base oil of lubricating viscosity used in such compositions may be mineral oil or synthetic oils of viscosity suitable for use in the crankcase of an internal combustion engine.
  • Crankcase base oils ordinarily have a viscosity of about 1300 cSt (1300 mm 2 /second) at 0°F (-18°C) to 3 cSt (3 mm 2 /second) at 210°F (99°C).
  • the base oils may be derived from synthetic or natural sources.
  • Mineral oil for use as the base oil in this invention includes paraffinic, naphthenic and other oils that are ordinarily used in lubricating oil compositions. Synthetic oils include both hydrocarbon synthetic oils and synthetic esters.
  • Useful synthetic hydrocarbon oils include liquid polymers of alpha olefins having the proper viscosity. Especially useful are the hydrogenated liquid oligomers of C 6 to C 12 alpha olefins such as 1-decene trimer. Likewise, alkyl benzenes of proper viscosity, such as didodecyl benzene, can be used.
  • Useful synthetic esters include the esters of monocarboxylic acids and polycarboxylic acids, as well as monohydroxy alkanols and polyols.
  • Typical examples are didodecyl adipate, pentaerythritol tetracaproate, di-2-ethylhexyl adipate, dilaurylsebacate, and the like.
  • Complex esters prepared from mixtures of mono and dicarboxylic acids and mono and dihydroxy alkanols can also be used.
  • Blends of mineral oils with synthetic oils are also useful. For example, blends of 10 to 25% hydrogenated 1-decene trimer with 75 to 90% 150 SUS (100°F (38°C)) mineral oil make excellent lubricating oil bases.
  • the LEDL of the present invention can be added to Group 1, 2, 3, or 4 base stocks or combinations thereof.
  • the LEDL of the present invention has been found to provide improved bulk oxidation and corrosion control performance when contacted with an internal combustion engine.
  • Embodiments of the LEDL may contain detergents.
  • Detergents help control varnish, ring zone deposits, and rust by keeping insoluble particles in colloidal suspension.
  • Metal-containing (or ash-forming detergents) function both as detergents to control deposits, and as acid neutralizers or rust inhibitors, thereby reducing wear and corrosion and extending engine life.
  • Detergents generally comprise a polar head with a long hydrophobic tail; with the polar head comprising a metal salt of an acidic organic compound.
  • the salts may contain a substantially stoichiometric amount of the metal in which case they are usually described as normal or neutral salts, and would typically have a total base number (as measured by ASTM D2896) of from 0 to 10.
  • overbased detergents may have a total base number of about 15 to 30 (low overbased (“LOB”)); 31 to 170 (medium overbased (“MOB)); 171 to 400 (high overbased (“MOB”)); or above 400 (high-high overbased (“HHOB)).
  • LOB low overbased
  • MOB medium overbased
  • HHOB high overbased
  • HHOB high-high overbased
  • the LEDLs of this invention may comprise one or more dispersants including nitrogen containing dispersants of the type generally represented by succinimides (e.g., polyisobutylene succinic acid/anhydride (PIBSA)-polyamine having a PIBSA molecular weight of about 700 to 2500).
  • the dispersants may be borated or non-borated, ashless or ash containing.
  • Lubricating oils of this invention may comprise about 1 wt. % to about 12 wt. % or more dispersants.
  • Preferred dispersants for this invention comprise one or more dispersants having an average molecular weight (mw) of about 1000 to about 10,000.
  • Dispersants prepared from polyisobutylene (PIB) having a mw of about 1000 to about 5000 are such preferred dispersants.
  • a preferred dispersant of this invention may be a one or more succinimides.
  • succinimide is understood in the art to include many of the amide, imide, etc. species that are also formed by the reaction of a succinic anhydride with an amine and is so used herein. The predominant product, however, is succinimide and this term has been generally accepted as meaning the product of a reaction of an alkenyl- or alkyl-substituted succinic acid or anhydride with a polyamine.
  • Alkenyl or alkyl succinimides are disclosed in numerous references and are well known in the art. Certain fundamental types of succinimides and related materials encompassed by the term of art "succinimide" are taught in U.S. Pat.
  • This invention may comprise one or more succinimides, which may be either a mono, poly, or bis-succinimide.
  • This invention may comprise lubricating oil involving one or more succinimide dispersants that have or have not been post treated.
  • Borated dispersants useful in the present invention may be derived from the reaction product of a polyisobutenylsuccinic anhydride with a polyamine.
  • the borated dispersant is derived from polybutenes having a molecular weight of from 1200 to 1400, most preferably about 1300.
  • Ethylene carbonate treated, or EC-treated, dispersants useful in the present invention may be derived from the reaction product of a polyisobutenylsuccinic anhydride with a polyamine.
  • the polyisobutene has a number average molecular weight (M n ) of at least 1800.
  • the EC-treated dispersant is a polybutene succinimide derived from polybutenes having a molecular weight of from 2000 to 2400.
  • a prefered EC treated succinimide of this invention is described in U.S. Patent Nos. 5,334,321 and 5,356,552 .
  • Corrosion inhibitors which may advantageously be used in the LEDL of this invention are, for example, succinimide salts of one or more aromatic dicarboxylic acids, and dispersed aromatic dicarboxylic acid corrosion inhibitors.
  • Preferred aromatic dicarboxylic acids may comprise one or more terephthalic acids.
  • Certain corrosion inhibitors including dispersed aromatic dicarboxylic acid corrosion inhibitors, are described, for example, in U.S. Patent Nos. 3,287,271 ; 3,692,681 ; and 3,374,174 .
  • One embodiment of the dispersed aromatic dicarboxylic acid corrosion inhibitor may be synthesized by reacting about 1100 to about 1500, preferably about 1300 molecular weight polyisobutenyl succinic anhydride (PIBSA) with one or more polyamines, preferably one or more heavy polyamines (HPA) at an amine/PIBSA CMR of about 0.4 to about 0.6, preferably about 0.45. This produces a reaction product that may then be reacted with terephthalic acid.
  • PIBSA polyisobutenyl succinic anhydride
  • HPA heavy polyamines
  • Another embodiment of the dispersed aromatic dicarboxylic acid corrosion inhibitor of this invention may be synthesized as follows.
  • One or more PIBSAs may be reacted with one or more polyamines to produce one or more succinimides by heating the mixture, with or without diluent, at a temperature of from about 110°C to about 200°C, preferably about 150°C to about 170°C, for 1 to 20 hours. Heating for about 3 to about 6 hours is preferred.
  • Reactants may be mixed and then heated or heating may occur while the reactants are being mixed. During the heating period, water of the reaction may be removed by any means known in the art. Any PIBSA may be used.
  • a mixture of PIBSA and a copolymer may also be used.
  • An amine/PIBSA charge mole ratio (CMR) of about 0.4 to 0.6 may be used.
  • a preferred CMR may be about 0.4 to about 0.5.
  • the reaction mixture may be cooled to about 110°C to about 150°C, preferably about 130°C to about 135°C.
  • Terephthalic acid may then be added.
  • terephthalic acid preferably about 2.5% to about 3.5% by weight, based on the succinimide weight
  • This mixture may then be heated for about 1 to about 10 hours, preferably about 2 to about 4 hours.
  • the mixture may then be filtered.
  • Another embodiment of this invention may comprise one or more corrosion inhibitors synthesized by reacting 1000 molecular weight polyisobutenesuccinic anhydride (PIBSA) with tetraethylenepentamine (TEPA) using an amine/PIBSA charge mole ratio (CMR) of 0.71. This produces a reaction product, which may then be reacted with terephthalic acid to form a dispersed aromatic dicarboxylic acid corrosion inhibitor.
  • PIBSA polyisobutenesuccinic anhydride
  • TEPA tetraethylenepentamine
  • CMR charge mole ratio
  • Traditional wear inhibitors may be used in this invention. As their name implies, these agents reduce wear of moving metallic parts. Examples of such agents include, but are not limited to phosphates, phosphites, carbamates, esters, sulfur containing compounds, and molybdenum complexes.
  • the LEDL of this invention comprises one or more wear inhibitors such metal dithiophospates and metal dithiocarbamates or mixtures thereof.
  • a preferred wear inhibitor for use in this invention comprises zinc dithiophosphate.
  • additive components are examples of some components that can be favorably employed in the present invention. These examples of additives are provided to illustrate the present invention, but they are not intended to limit it:
  • the LEDL of the present invention is useful for its improved detergency over other engine lubricating oil compositions.
  • a lubricating oil composition comprises a major part of a base oil of lubricating viscosity and from 0 wt. % to 1.2 wt. % ash; from 0.1 wt. % to 0.5 wt. % sulfur; and from 0.02 wt. % to 0.1 wt. % phosphorus.
  • Said LEDLs provide improved detergency while at the same time providing compatibility with exhaust gas after-treatment systems.
  • the LEDL would contain:
  • LEDLs containing said additive provide superior corrosion protection to LEDLs containing commercially available salicylates at constant ash, sulfur and phosphorus levels.
  • LEDLs of the instant invention may be prepared such that they contain very low sulfur.
  • Very low sulfur is defined to mean about 0.05 wt. % to about 0.3 wt. % sulfur.
  • very low sulfur LEDLs prepared according to the instant invention provide superior corrosion protection when used in an internal combustion engine.
  • the LEDL is produced by blending a mixture of the above components.
  • the LEDL produced by that method might have a slightly different composition than the initial mixture, because the components may interact.
  • the components can be blended in any order and can be blended as combinations of components.
  • a charge of 875 g of branched dodecylphenol (DDP) having a molecular mass of 270, (i.e. 3.24 moles) and 875 g of linear alkylphenol having a molecular mass of about 390 (i.e. 2.24 moles) was placed in a four-necked 4 liter glass reactor above which was a heat-insulated Vigreux fractionating column.
  • the isomeric molar repartition of para versus ortho alkylphenol was:
  • the agitator was started up and the reaction mixture was heated to 65°C, at which temperature 158 grams of slaked lime Ca(OH) 2 (i.e. 2.135 moles) and 19 g of a mixture (50/50 by weight) of formic acid and acetic acid were added.
  • the reaction medium underwent further heating to 120°C at which temperature the reactor was placed under a nitrogen atmosphere, then heated up to 165°C and then the nitrogen introduction was stopped. Distillation of water commenced at this temperature.
  • the temperature was increased to 240° C and the pressure was reduced gradually below atmospheric until an absolute pressure of 5,000 Pa (50 mbars) was obtained.
  • the reaction mixture was kept for five hours under the preceding conditions.
  • the reaction mixture was allowed to cool to 180°C, then the vacuum was broken under a nitrogen atmosphere and a sample was taken for analysis.
  • the total quantity of distillate obtained was about 120 cm 3 ; demixing took place in the lower phase (66 cm 3 being water).
  • Step (A) The product obtained in Step (A) was transferred to a 3.6-liter autoclave and heated to 180°C.
  • the autoclave was closed, leaving a very small leak, and the introduction of CO 2 was continued so as to maintain a pressure of 3.5 ⁇ 10 5 Pa (3.5 bars) for 5 hours at 200° C.
  • the amount of CO 2 introduced was in the order of 50 grams.
  • the pressure was restored to atmospheric (1013 mbar) and the reactor was then purged with nitrogen.
  • SAI is a measure of the quantity of alkylsalicylate formed in the detergent-dispersant. It was determined by acidification of the product by a strong acid (hydrochloric acid) in the presence of diethyl ether, followed by a potentiometric titration on the organic fraction (tetra n-butyl ammonium hydroxide was used as a titration agent). Results are expressed in equivalent mg KOH per gram of product (Base Number unit).
  • the intermediate product was fed at a rate of 70 kg/hr to a wiped film evaporator (WFE) which had a surface area of 0.39 m 2 .
  • the WFE had an internal condenser and entrainment separator along with a hot oil jacket.
  • the hot oil temperature in the jacket was about 250°C.
  • the pressure within the WFE was 1.3 mbar.
  • the feed temperature to the WFE was 135°C.
  • Final product temperature exiting the WFE was 222°C.
  • the product was cooled to less than 100°C before diluting with 100N base oil. Approximately 47.5 % (by weight) of the feed to the WFE was collected as distillate. The amount of distillate collected may vary from 10% up to about 55% by weight of the feed to the WFE.
  • Dialysis was performed on about 15 gm of product from Example 3 using a Soxhlet extraction apparatus (pentane solvent) and a Latex membrane condom for about 24 hours to afford a dialysate fraction (the material that passes through the membrane) and a residue fraction (the material left in the latex membrane bag).
  • Soxhlet extraction apparatus penentane solvent
  • Latex membrane condom for about 24 hours to afford a dialysate fraction (the material that passes through the membrane) and a residue fraction (the material left in the latex membrane bag).
  • the dialysate fraction from the dialysis procedure was separated into two fractions using silica gel chromatography (0.2 - 0.25 gm on two Silica Gel Cartridges - Waters Part No. 051900) first using 12 ml of hexane to yield Fraction 1 followed by reversing the Cartridges and flushing with 12 ml of 80:20 Ethyl Acetate: Ethanol to afford Fraction 2.
  • Fraction 1 was comprised of diluent oil and Fraction 2 was comprised of free alkylphenols.
  • Fraction 2 obtained from the chromatographic separation procedure was analyzed using supercritical chromatography (SFC) to determine the amount of branched alkylphenol and linear alkylphenol present. Quantification was performed using a calibration curve of known mixtures of branched and linear alkylphenol.
  • Dialysis results are as follows: Dialysate 51.1 wt % of starting sample weight Residue 48.9 wt% of starting sample weight
  • Dialysate Composition Dodecylphenol 1.0 wt% Linear Alkylphenol 26.7 wt% 100N Base Oil 72.3 wt%
  • Residue Composition Calcium 9.3 wt% TBN 259 mg KOH/gm SAI 78 mg KOH/gm % SA 50
  • Example 3 The following composition of the product produced in Example 3 was calculated from the composition of the dialysate and residue fractions: Total Alkylphenol Content 14.1 wt% Oil 36.9 wt% Single Aromatic Ring Alkylsalicylate 24.5 wt% Calcium Alkylphenate 24.5 wt%
  • This test method is used to test diesel engine lubricants to determine their tendency to corrode various metals, specifically alloys of lead and copper commonly used in cam followers and bearings.
  • Four metal specimens of copper, lead, tin, and phosphor bronze are immersed in a measured amount of engine oil. The oil, at an elevated temperature, is blown with air for a period of time. When the test is completed, the copper specimen and the stressed oil are examined to detect corrosion and corrosion products, respectively.
  • the lubrication oil formulations used in the present example were designed for Low Emission Diesel Lubricants (LEDL) intended for use in Low Emission Diesel Engines and had the following compositions: Baseline Formulation A A B B C C Sulfated Ash, % 0.95 0.95 1.0 1.0 1.0 1.0 Sulfur, % 0.10 0.10 0.12 0.12 0.10 0.10 Phosphorus, % 0.05 0.05 0.05 0.05 0.05 Borated Dispersant Y Y Y Y Y Y Y Non-Borated Dispersant Y Y Y Y Y LOB Ca-Sulfonate N N Y Y N N LOB Salicylate N N N N Y Y Y Commercially Available 4.5 N 4.5 N 4.5 N 4.5 N Salicylate, wt% Unsulfurized Carboxylate-Containing additive prepared according to Example 1, wt% N 5.0 N 5.0 N 5.0 Secondary ZnDTP Y Y Y Y Y Diphenyl
  • LEDL formulations each pair with the same levels of ash, sulfur and phosphorus.
  • an LEDL containing the unsulfurized, carboxylate-containing hydroxy-aromatic surfactant-based detergent-dispersant additive employed in the present invention was compared to an LEDL containing a commercially available salicylate for corrosion performance.
  • the LEDL of the present invention containing the carboxylate-containing additive displayed superior corrosion control performance. Surprisingly, even at very low sulfur levels, acceptable performance was obtained.
  • the lubrication oil formulations used in the present example were designed for Low Emission Diesel Lubricants (LEDL) intended for use in Low Emission Diesel Engines and had the following compositions: Description A B C D E Sulfated Ash, % 0.54 0.86 0.47 0.68 0.90 Sulfur, % 0.18 0.18 0.12 0.12 0.12 Phosphorus, % 0.08 0.08 0.05 0.05 0.05 Borated Dispersant Y Y Y Y Y Y Non-Borated Dispersant Y Y Y Y Y Co-Detergent Y Y Y Y Y Unsulfurized Carboxylate-Containing additive prepared according to Example 1, wt% 2.0 3.9 1.9 3.2 4.4 Secondary ZnDTP, wt% 1.04 1.04 0.66 0.66 0.66 Diphenylamine Anti-Oxidant Y Y Y Y Y Phenolic Anti-Oxidant Y Y Y Y Y Molybdenum Anti
  • the LEDL displayed superior corrosion control performance. Said performance is not degraded by decreasing the wt. % ZnDTP. Even at very low sulfur levels, the LEDL of the present invention displayed superior corrosion control performance.

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Claims (29)

  1. Schmiermittelzusammensetzung für emissionsarme Dieselmotoren, umfassend
    eine größere Menge Basisöl mit Schmierviskosität;
    von 1,8 Gew.-% bis 5,5 Gew.-% eines nicht sulfurierten, carboxylathaltigen Detergensdispergierungs-Zusatzmittels auf Basis eines hydroxy-aromatischen Tensids, mit weniger als 40 Gew.-% freiem Hydrocarbylphenol;
    ein Dispergiermittel; und
    einen Verschleißhemmer,
    wobei das nicht sulfurierte, carboxylathaltige Detergensdispergierungs-Zusatzmittel auf Basis eines hydroxy-aromatischen Tensids zudem umfasst
    (a) von 10 bis 50 Gew.-% Alkalierdmetall-Hydrocarbylphenat;
    (b) von 15 bis 60 Gew.-% Alkalierdmetall-Hydrocarbylsalicylat mit einem einzelnen aromatischen Ring, wobei der Begriff "Alkalierdmetall-Hydrocarbylsalicylat mit einem einzelnen aromatischen Ring" ein Alkalierdmetallsalz einer Hydrocarbyl-Salicylsäure bedeutet, wobei nur ein Hydrocarbyl-Salicyl-Anion pro Alkalierdmetall-Basenkation vorliegt;
    (c) von 0 Gew.-% bis 50 Gew.-% organisches Verdünnungsmittel; und
    (d) Alkalierdmetall-Hydrocarbylsalicylat mit doppeltem aromatischen Ring, wobei der Begriff "Alkalierdmetall-Hydrocarbylsalicylat mit doppeltem aromatischen Ring" ein Alkalierdmetallsalz einer Hydrocarbyl-Salicylsäure bedeutet, wobei zwei Hydrocarbyl-Salicyl-Anionen pro Alkalierdmetall-Basenkation vorliegen;
    wobei das Molarverhältnis von Alkalierdmetall-Hydrocarbylsalicylat mit einem einzelnen aromatischen Ring zu Alkalierdmetall-Hydrocarbylsalicylat mit doppeltem aromatischen Ring mindestens 8:1 ist; und
    wobei die Zusammensetzung enthält:
    von 0 Gew.-% bis 1,2 Gew.-% Asche;
    von 0,1 Gew.-% bis 0,5 Gew.-% Schwefel; und
    von 0,02 Gew.-% bis 0,1 Gew.-% Phosphor.
  2. Schmiermittelzusammensetzung für emissionsarme Dieselmotoren gemäß Anspruch 1, wobei die Zusammensetzung enthält
    weniger als 1,0 Gew.-% Asche;
    weniger als 0,3 Gew.-% Schwefel; und
    weniger als 0,08 Gew.-% Phosphor.
  3. Schmiermittelzusammensetzung für emissionsarme Dieselmotoren gemäß Anspruch 1, wobei die Zusammensetzung enthält
    von 0,4 Gew.-% bis 1,0 Gew.-% Asche;
    von 0,05 Gew.-% bis 0,3 Gew.-% Schwefel; und
    von 0,02 Gew.-% bis 0,08 Gew.-% Phosphor.
  4. Schmiermittelzusammensetzung für emissionsarme Dieselmotoren gemäß Anspruch 3, wobei die Zusammensetzung enthält
    von 0,4 Gew.-% bis 1,0 Gew.-% Asche;
    von 0,05 Gew.-% bis 0,15 Gew.-% Schwefel; und
    von 0,02 Gew.-% bis 0,08 Gew.-% Phosphor.
  5. Schmiermittelzusammensetzung für emissionsarme Dieselmotoren gemäß irgendeinem der Ansprüche 1 bis 4, wobei die Zusammensetzung zudem umfasst einen Korrosionshemmer, ausgewählt aus dem Bernsteinsäureimidsalz von einer oder mehreren aromatischen Dicarboxylsäuren und dispergierten aromatischen Dicarboxylsäure-Korrosionshemmern.
  6. Schmiermittelzusammensetzung für emissionsarme Dieselmotoren gemäß Anspruch 5, wobei
    das Dispergiermittel ein boriertes Dispergiermittel ist; und
    der Verschleißhemmer ein Metalldithiophosphat ist.
  7. Schmiermittelzusammensetzung für emissionsarme Dieselmotoren gemäß Anspruch 6, wobei die Zusammensetzung enthält
    von 1,0 Gew.-% bis 4,0 Gew.-% des borierten Dispergiermittels;
    von 0,2 Gew.-% bis 1,1 Gew.-% des Verschleißhemmers; und
    von 0 Gew.-% bis 0,5 Gew.-% des Korrosionshemmers.
  8. Schmiermittelzusammensetzung für emissionsarme Dieselmotoren gemäß Anspruch 7, wobei
    das Dispergiermittel ein Bernsteinsäureimid ist;
    der Verschleißhemmer Zinkdithiophosphat ist; und
    der Korrosionshemmer eine neutralisierte Terephthalsäure ist.
  9. Schmiermittelzusammensetzung für emissionsarme Dieselmotoren gemäß Anspruch 8, zudem umfassend
    von 3,0 Gew.-% bis 8,0 Gew.-% nicht boriertes Dispergiermittel;
    von 0,6 Gew.-% bis 1,4 Gew.-% Calciumsulfonat;
    von 0,1 Gew.-% bis 0,5 Gew.-% Molybdän-Antioxidans;
    von 0 Gew.-% bis 1,0 Gew.-% phenolisches Antioxidans;
    von 0,1 Gew.-% bis 1,0 Gew.-% aminisches Antioxidans;
    von 0 Gew.-% bis 6,0 Gew.-% dispergierendes Olefin-Copolymer; und
    von 0 bis 25 ppm Schaumverhütungsmittel.
  10. Schmiermittelzusammensetzung für emissionsarme Dieselmotoren gemäß Anspruch 1 , wobei das nicht sulfurierte carboxylathaltige Zusatzmittel hergestellt wird durch ein Verfahren, umfassend
    (a) Neutralisation von Hydrocarbylphenolen mit einer Alkalierdbase in Anwesenheit eines Beschleunigers, welcher umfasst mindestens eine Carboxylsäure mit einem bis vier Kohlenstoffatomen, zur Herstellung eines Hydrocarbylphenats;
    (b) Carboxylierung des in Schritt (a) erhaltenen Hydrocarbylphenats mit Kohlendioxyd unter Carboxylierungsbedingungen, ausreichend zur Umsetzung von mindestens 20Mol% des anfänglichen Hydrocarbylphenols zu Hydrocarbylsalicylat; und
    (c) Abtrennung von mindestens 10 Gew.-% des anfänglichen Hydrocarbylphenols vom in Schritt (b) hergestellten Produkt zur Herstellung des Zusatzmittels,
    wobei die Zusammensetzung enthält:
    von 0 Gew.-% bis 1,2 Gew.-% Asche;
    von 0,1 Gew.-% bis 0,5 Gew.-% Schwefel; und
    von 0,02 Gew.-% bis 0,1 Gew.-% Phosphor.
  11. Schmiermittelzusammensetzung für emissionsarme Dieselmotoren gemäß Anspruch 10, wobei die Zusammensetzung enthält:
    weniger als 1,0 Gew.-% Asche;
    weniger als 0,3 Gew.-% Schwefel; und
    weniger als 0,08 Gew.-% Phosphor.
  12. Schmiermittelzusammensetzung für emissionsarme Dieselmotoren gemäß Anspruch 10, wobei die Zusammensetzung enthält
    von 0,4 Gew.-% bis 1,0 Gew.-% Asche;
    von 0,05 Gew.-% bis 0,3 Gew.-% Schwefel; und
    von 0,02 Gew.-% bis 0,08 Gew.-% Phosphor.
  13. Schmiermittelzusammensetzung für emissionsarme Dieselmotoren gemäß Anspruch 12, wobei die Zusammensetzung enthält
    von 0,4 Gew.-% bis 1,0 Gew.-% Asche;
    von 0,05 Gew.-% bis 0,15 Gew.-% Schwefel; und
    von 0,02 Gew.-% bis 0,08 Gew.-% Phosphor.
  14. Schmiermittelzusammensetzung für emissionsarme Dieselmotoren gemäß irgendeinem der Ansprüche 10 bis 13, wobei im Abtrennungsschritt mindestens 30 Gew. % der anfänglichen Hydrocarbylphenole vom in Schritt (b) hergestellten Produkt abgetrennt werden zur Herstellung des Zusatzmittels.
  15. Schmiermittelzusammensetzung für emissionsarme Dieselmotoren gemäß irgendeinem der Ansprüche 10 bis 13, wobei im Abtrennungsschritt bis zu 55 Gew. % der anfänglichen Hydrocarbylphenole vom in Schritt (b) hergestellten Produkt abgetrennt werden zur Herstellung des Zusatzmittels.
  16. Schmiermittelzusammensetzung für emissionsarme Dieselmotoren gemäß irgendeinem der Ansprüche 10 bis 13, wobei im Abtrennungsschritt 45 Gew. % bis 50 Gew.-% der anfänglichen Hydrocarbylphenole vom in Schritt (b) hergestellten Produkt abgetrennt werden zur Herstellung des Zusatzmittels.
  17. Schmiermittelzusammensetzung für emissionsarme Dieselmotoren gemäß irgendeinem der Ansprüche 10 bis 13, wobei im Abtrennungsschritt die anfänglichen Hydrocarbylphenole durch Destillation entfernt werden.
  18. Schmiermittelzusammensetzung für emissionsarme Dieselmotoren gemäß Anspruch 17, wobei im Abtrennungsschritt mindestens 30 Gew. % der anfänglichen Hydrocarbylphenole vom in Schritt (b) hergestellten Produkt abgetrennt werden zur Herstellung des Zusatzmittels.
  19. Schmiermittelzusammensetzung für emissionsarme Dieselmotoren gemäß Anspruch 17, wobei im Abtrennungsschritt bis zu 55 Gew. % der anfänglichen Hydrocarbylphenole vom in Schritt (b) hergestellten Produkt abgetrennt werden zur Herstellung des Zusatzmittels.
  20. Schmiermittelzusammensetzung für emissionsarme Dieselmotoren gemäß Anspruch 17, wobei im Abtrennungsschritt 45 Gew. % bis 50 Gew.-% der anfänglichen Hydrocarbylphenole vom in Schritt (b) hergestellten Produkt abgetrennt werden zur Herstellung des Zusatzmittels.
  21. Schmiermittelzusammensetzung für emissionsarme Dieselmotoren gemäß Anspruch 17, wobei die Destillation durchgeführt wird über eine Fallfilmdestillation, Abstreiffilm-Verdampferdestillation oder Kurzwegdestillation.
  22. Schmiermittelzusammensetzung für emissionsarme Dieselmotoren gemäß Anspruch 21, wobei die Destillation durchgeführt wird bei Temperaturen im Bereich von 150°C bis 250°C und einem Druck von 0,1 bis 4 mbar.
  23. Schmiermittelzusammensetzung für emissionsarme Dieselmotoren gemäß Anspruch 21, wobei die Destillation durchgeführt wird bei Temperaturen im Bereich von 190°C bis 230°C und einem Druck von 0,5 bis 3 mbar.
  24. Schmiermittelzusammensetzung für emissionsarme Dieselmotoren gemäß Anspruch 21, wobei die Destillation durchgeführt wird bei Temperaturen im Bereich von 195°C bis 225°C und einem Druck von 1 bis 2 mbar.
  25. Schmiermittelzusammensetzung für emissionsarme Dieselmotoren gemäß irgendeinem der Ansprüche 10 bis 13, wobei das nicht sulfurierte, carboxylathaltige Detergensdispergierungs-Zusatzmittel auf Basis eines hydroxy-aromatischen Tensids von 10 bis 50 Gew.-% organisches Verdünnungsmittel umfasst.
  26. Schmiermittelzusammensetzung für emissionsarme Dieselmotoren gemäß Anspruch 25, wobei das nicht sulfurierte, carboxylathaltige Detergensdispergierungs-Zusatzmittel auf Basis eines hydroxy-aromatischen Tensids von 20 bis 50 Gew.-% organisches Verdünnungsmittel umfasst.
  27. Schmiermittelzusammensetzung für emissionsarme Dieselmotoren gemäß irgendeinem der Ansprüche 10 bis 13, wobei im Neutralisationsschritt
    (a) die Neutralisation durchgeführt wird in Anwesenheit von mindestens einer Carboxylsäure mit einem bis vier Kohlenstoffatomen, und ein Abwesenheit von Alkalibase, Dialkohol und Monoalkohol;
    (b) die Neutralisation bei einer Temperatur von mindestens 200°C durchgeführt wird;
    (c) der Druck fortschreitend unter atmosphärischen Druck verringert wird, um Wasser aus der Reaktion zu entfernen, in Abwesenheit von Lösungsmitteln, die mit Wasser ein Azeotrop bilden können;
    (d) die Hydrocarbylphenole bis zu 85 Gew.-% lineare Hydrocarbylphenole, vermischt mit mindestens 15 Gew.-% des verzweigten Hydrocarbylphenols, in welchem das verzweigte Hydrocarbylradikal mindestens neun Kohlenstoffatome enthält; und
    (e) die Mengen der verwendeten Reagenzien den folgenden Molverhältnissen entsprechen:
    (1) Alkalierdbase/Hydrocarbylphenol von 0,2:1 bis 0,7:1; und
    (2) Carboxylsäure/Hydrocarbylphenol von 0,01:1 bis 0,5:1.
  28. Schmiermittelzusammensetzung für emissionsarme Dieselmotoren gemäß irgendeinem der Ansprüche 10 bis 13, wobei die Zusammensetzung zudem umfasst einen Korrosionshemmer, ausgewählt aus einem Bernsteinsäureimidsalz von einer oder mehreren aromatischen Dicarboxylsäuren und dispergierten aromatischen Dicarboxylsäure-Korrosionshemmern.
  29. Verwendung eines sulfurierten, carboxylathaltigen Detergensdispergierungs-Zusatzmittels auf Basis eines hydroxy-aromatischen Tensids wie in Anspruch 1 definiert, in einer Schmiermittelzusammensetzung für emissionsarme Dieselmotoren zur Verringerung von Korrosion, wobei die Schmiermittelzusammensetzung für emissionsarme Dieselmotoren umfasst:
    eine größere Menge Basisöl mit Schmierviskosität;
    ein Dispergiermittel; und
    einen Verschleißhemmer; und
    wobei die Schmiermittelzusammensetzung enthält:
    von 0 Gew.-% bis 1,2 Gew.-% Asche;
    von 0,1 Gew.-% bis 0,5 Gew.-% Schwefel; und
    von 0,02 Gew.-% bis 0,1 Gew.-% Phosphor.
EP04252592A 2003-05-22 2004-05-04 Emissionsarmes Schmiermittel mit verbessertem Korrosionsschutz Expired - Lifetime EP1479752B1 (de)

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Families Citing this family (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4578115B2 (ja) * 2004-02-04 2010-11-10 Ｊｘ日鉱日石エネルギー株式会社 潤滑油組成物
JP4515797B2 (ja) * 2004-03-19 2010-08-04 新日本石油株式会社 ディーゼルエンジン用潤滑油組成物
US20060223724A1 (en) * 2005-03-29 2006-10-05 Gatto Vincent J Lubricating oil composition with reduced phosphorus levels
US7956022B2 (en) * 2005-07-29 2011-06-07 Chevron Oronite Company Llc Low sulfur metal detergent-dispersants
US7951760B2 (en) * 2005-07-29 2011-05-31 Chevron Oronite S.A. Overbased alkali metal alkylhydroxybenzoates having low crude sediment
US8030258B2 (en) * 2005-07-29 2011-10-04 Chevron Oronite Company Llc Overbased alkaline earth metal alkylhydroxybenzoates having low crude sediment
JP5438251B2 (ja) * 2005-08-29 2014-03-12 シェブロン・オロナイト・カンパニー・エルエルシー 内燃機関用潤滑油組成物
ES2380949T3 (es) * 2005-11-03 2012-05-21 Infineum International Limited Copolímeros de dibloques lineales como aditivos anti-desgaste para lubricantes de cárter de motores de combustión interna
US20070105731A1 (en) * 2005-11-04 2007-05-10 Chin Chu Lubricating oil compositions
US7981846B2 (en) * 2005-11-30 2011-07-19 Chevron Oronite Company Llc Lubricating oil composition with improved emission compatibility
US20080146473A1 (en) * 2006-12-19 2008-06-19 Chevron Oronite Company Llc Lubricating oil with enhanced piston cleanliness control
US8747650B2 (en) * 2006-12-21 2014-06-10 Chevron Oronite Technology B.V. Engine lubricant with enhanced thermal stability
US7838474B2 (en) * 2007-10-31 2010-11-23 Chevron Oronite Company Llc Lubricating oil compositions comprising a biodiesel fuel and a detergent
CN102575185B (zh) * 2009-08-06 2014-03-05 卢布里佐尔公司 含沥青质分散剂的润滑组合物
US9976103B2 (en) * 2009-12-14 2018-05-22 The Lubrizol Corporation Lubricating composition containing an antiwear agent
ES2673725T3 (es) * 2012-03-01 2018-06-25 Infineum International Limited Método de lubricación de un motor marino
US9359573B2 (en) * 2012-08-06 2016-06-07 Exxonmobil Research And Engineering Company Migration of air release in lubricant base stocks
JP5831440B2 (ja) 2012-12-17 2015-12-09 株式会社ダイヤメット 粉末冶金用原料粉末
US10370320B2 (en) * 2017-12-30 2019-08-06 Rohm And Haas Electronic Materials Llc Purification methods

Family Cites Families (45)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3100673A (en) * 1963-08-13 Dyeings and prints possessing fastness
US2992708A (en) * 1954-01-14 1961-07-18 Lyon George Albert Air circulating wheel structure
US3036971A (en) * 1958-12-24 1962-05-29 Socony Mobil Oil Co Inc Lubricating oils containing carbonated basic sulfurized calcium phenates
DE1248643B (de) * 1959-03-30 1967-08-31 The Lubrizol Corporation, Cleveland, Ohio (V. St. A.) Verfahren zur Herstellung von öllöslichen aeylierten Aminen
NL124842C (de) * 1959-08-24
NL255193A (de) * 1959-08-24
NL255194A (de) * 1959-08-24
US3381022A (en) * 1963-04-23 1968-04-30 Lubrizol Corp Polymerized olefin substituted succinic acid esters
US3287271A (en) * 1965-01-21 1966-11-22 Chevron Res Combined detergent-corrosion inhibitors
US3272746A (en) * 1965-11-22 1966-09-13 Lubrizol Corp Lubricating composition containing an acylated nitrogen compound
US3374174A (en) * 1966-04-12 1968-03-19 Lubrizol Corp Composition
US3692681A (en) * 1968-08-02 1972-09-19 Chevron Res Dispersion of terephthalic acid in detergent containing hydrocarbon oil medium
US3912764A (en) * 1972-09-29 1975-10-14 Cooper Edwin Inc Preparation of alkenyl succinic anhydrides
US4234435A (en) * 1979-02-23 1980-11-18 The Lubrizol Corporation Novel carboxylic acid acylating agents, derivatives thereof, concentrate and lubricant compositions containing the same, and processes for their preparation
FR2529226B1 (fr) * 1982-06-24 1987-01-16 Orogil Procede de preparation d'alkylphenates sulfurises de metaux alcalino-terreux utilisables comme additifs pour huiles lubrifiantes
US4747965A (en) * 1985-04-12 1988-05-31 Chevron Research Company Modified succinimides
US4612132A (en) * 1984-07-20 1986-09-16 Chevron Research Company Modified succinimides
GB8703549D0 (en) * 1987-02-16 1987-03-25 Shell Int Research Preparation of basic salt
US5112507A (en) * 1988-09-29 1992-05-12 Chevron Research And Technology Company Polymeric dispersants having alternating polyalkylene and succinic groups
GB8827306D0 (en) * 1988-11-23 1988-12-29 Shell Int Research Process for separation of phenol
US5266186A (en) * 1989-10-12 1993-11-30 Nalco Chemical Company Inhibiting fouling employing a dispersant
US5241003A (en) * 1990-05-17 1993-08-31 Ethyl Petroleum Additives, Inc. Ashless dispersants formed from substituted acylating agents and their production and use
JP3086727B2 (ja) * 1991-08-09 2000-09-11 オロナイトジャパン株式会社 低リンエンジン油製造用の添加剤組成物
US5319030A (en) * 1992-07-23 1994-06-07 Chevron Research And Technology Company One-step process for the preparation of alkenyl succinic anhydride
US5286799A (en) * 1992-07-23 1994-02-15 Chevron Research And Technology Company Two-step free radical catalyzed process for the preparation of alkenyl succinic anhydride
US5356552A (en) * 1993-03-09 1994-10-18 Chevron Research And Technology Company, A Division Of Chevron U.S.A. Inc. Chlorine-free lubricating oils having modified high molecular weight succinimides
US5334321A (en) * 1993-03-09 1994-08-02 Chevron Research And Technology Company, A Division Of Chevron U.S.A. Inc. Modified high molecular weight succinimides
US5525247A (en) * 1993-08-11 1996-06-11 Idemitsu Kosan Co., Ltd. Low ash lubricating oil composition for diesel engine and method for lubrication of diesel engine using same
FR2717491B1 (fr) * 1994-03-17 1996-06-07 Chevron Chem Sa Additifs détergents-dispersants pour huiles lubrifiantes du type alkylsalicylates-alkylphénates, alcalino-terreux, sulfurisés et suralcalinisés.
JPH07268374A (ja) * 1994-03-30 1995-10-17 Cosmo Sogo Kenkyusho:Kk 石油添加剤ならびに芳香族ヒドロキシカルボン酸アルカリ土類金属塩の製造法
DE69617761T2 (de) * 1995-02-01 2002-08-08 The Lubrizol Corp., Wickliffe Schmiermittelzusammensetzung mit geringem Aschegehalt
US5716912A (en) * 1996-04-09 1998-02-10 Chevron Chemical Company Polyalkylene succinimides and post-treated derivatives thereof
IT1282788B1 (it) * 1996-06-04 1998-03-31 Euron Spa Composizioni lubrificanti a basse emissioni di particolato per motori a combustione interna
JPH1135962A (ja) * 1997-07-16 1999-02-09 Idemitsu Kosan Co Ltd 潤滑油組成物
DE69812873T2 (de) * 1998-01-30 2004-01-22 Chevron Chemical S.A. Schwefel- und alkalimetalfreie Schmieröladditive
US5942476A (en) * 1998-06-03 1999-08-24 Chevron Chemical Company Low-viscosity highly overbased phenate-carboxylate
US6348438B1 (en) * 1999-06-03 2002-02-19 Chevron Oronite S.A. Production of high BN alkaline earth metal single-aromatic ring hydrocarbyl salicylate-carboxylate
US6423670B2 (en) * 2000-03-20 2002-07-23 Infineum International Ltd. Lubricating oil compositions
US6569818B2 (en) * 2000-06-02 2003-05-27 Chevron Oronite Company, Llc Lubricating oil composition
JP3722472B2 (ja) * 2000-06-02 2005-11-30 シェブロンテキサコジャパン株式会社 潤滑油組成物
US6784143B2 (en) * 2001-05-11 2004-08-31 Infineum International Ltd. Lubricating oil composition
JP4931299B2 (ja) * 2001-07-31 2012-05-16 Ｊｘ日鉱日石エネルギー株式会社 潤滑油組成物
US7026273B2 (en) * 2001-11-09 2006-04-11 Infineum International Limited Lubricating oil compositions
US6784142B2 (en) * 2002-02-14 2004-08-31 Chevron Oronite Company Llc Lubricating oil composition comprising borated and EC-treated succinimides and phenolic antioxidants
US7018958B2 (en) * 2002-10-22 2006-03-28 Infineum International Limited Lubricating oil compositions

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US20040235682A1 (en) 2004-11-25
EP1479752A2 (de) 2004-11-24
CA2467843A1 (en) 2004-11-22
CA2467843C (en) 2013-08-06
JP4921697B2 (ja) 2012-04-25
SG116548A1 (en) 2005-11-28
JP2004346326A (ja) 2004-12-09
EP1479752A3 (de) 2009-10-28

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