EP1380634A1 - Lubricity additives stabilised against oxidation for highly desulphurised fuel oils. - Google Patents
Lubricity additives stabilised against oxidation for highly desulphurised fuel oils. Download PDFInfo
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- EP1380634A1 EP1380634A1 EP03013093A EP03013093A EP1380634A1 EP 1380634 A1 EP1380634 A1 EP 1380634A1 EP 03013093 A EP03013093 A EP 03013093A EP 03013093 A EP03013093 A EP 03013093A EP 1380634 A1 EP1380634 A1 EP 1380634A1
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L10/00—Use of additives to fuels or fires for particular purposes
- C10L10/08—Use of additives to fuels or fires for particular purposes for improving lubricity; for reducing wear
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- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/143—Organic compounds mixtures of organic macromolecular compounds with organic non-macromolecular compounds
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- 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
- C10M169/00—Lubricating compositions characterised by containing as components a mixture of at least two types of ingredient selected from base-materials, thickeners or additives, covered by the preceding groups, each of these compounds being essential
- C10M169/04—Mixtures of base-materials and additives
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- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M169/00—Lubricating compositions characterised by containing as components a mixture of at least two types of ingredient selected from base-materials, thickeners or additives, covered by the preceding groups, each of these compounds being essential
- C10M169/04—Mixtures of base-materials and additives
- C10M169/044—Mixtures of base-materials and additives the additives being a mixture of non-macromolecular and macromolecular compounds
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- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/18—Organic compounds containing oxygen
- C10L1/182—Organic compounds containing oxygen containing hydroxy groups; Salts thereof
- C10L1/183—Organic compounds containing oxygen containing hydroxy groups; Salts thereof at least one hydroxy group bound to an aromatic carbon atom
- C10L1/1835—Organic compounds containing oxygen containing hydroxy groups; Salts thereof at least one hydroxy group bound to an aromatic carbon atom having at least two hydroxy substituted non condensed benzene rings
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- C10L1/00—Liquid carbonaceous fuels
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- C10L1/19—Esters ester radical containing compounds; ester ethers; carbonic acid esters
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- C10L1/1905—Esters ester radical containing compounds; ester ethers; carbonic acid esters of di- or polycarboxylic acids
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- C10L1/19—Esters ester radical containing compounds; ester ethers; carbonic acid esters
- C10L1/191—Esters ester radical containing compounds; ester ethers; carbonic acid esters of di- or polyhydroxyalcohols
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- C10L1/195—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds
- C10L1/196—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derived from monomers containing a carbon-to-carbon unsaturated bond and a carboxyl group or salts, anhydrides or esters thereof homo- or copolymers of compounds having one or more unsaturated aliphatic radicals each having one carbon bond to carbon double bond, and at least one being terminated by a carboxyl radical or of salts, anhydrides or esters thereof
- C10L1/1966—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derived from monomers containing a carbon-to-carbon unsaturated bond and a carboxyl group or salts, anhydrides or esters thereof homo- or copolymers of compounds having one or more unsaturated aliphatic radicals each having one carbon bond to carbon double bond, and at least one being terminated by a carboxyl radical or of salts, anhydrides or esters thereof poly-carboxylic
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- C10L1/197—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derived from monomers containing a carbon-to-carbon unsaturated bond and an acyloxy group of a saturated carboxylic or carbonic acid
- C10L1/1973—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derived from monomers containing a carbon-to-carbon unsaturated bond and an acyloxy group of a saturated carboxylic or carbonic acid mono-carboxylic
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- C10L1/00—Liquid carbonaceous fuels
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- C10L1/192—Macromolecular compounds
- C10L1/198—Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid
- C10L1/1981—Condensation polymers of aldehydes or ketones
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- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
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- C10L1/22—Organic compounds containing nitrogen
- C10L1/221—Organic compounds containing nitrogen compounds of uncertain formula; reaction products where mixtures of compounds are obtained
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- C10L1/222—Organic compounds containing nitrogen containing at least one carbon-to-nitrogen single bond
- C10L1/224—Amides; Imides carboxylic acid amides, imides
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- C10L1/234—Macromolecular compounds
- C10L1/236—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derivatives thereof
- C10L1/2364—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derivatives thereof homo- or copolymers derived from unsaturated compounds containing amide and/or imide groups
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- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2205/00—Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions
- C10M2205/02—Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions containing acyclic monomers
- C10M2205/022—Ethene
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- C10M2207/00—Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
- C10M2207/28—Esters
- C10M2207/282—Esters of (cyclo)aliphatic oolycarboxylic acids
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- C10M2209/00—Organic macromolecular compounds containing oxygen as ingredients in lubricant compositions
- C10M2209/10—Macromolecular compoundss obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- C10M2209/101—Condensation polymers of aldehydes or ketones and phenols, e.g. Also polyoxyalkylene ether derivatives thereof
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- C10N2020/00—Specified physical or chemical properties or characteristics, i.e. function, of component of lubricating compositions
- C10N2020/01—Physico-chemical properties
- C10N2020/013—Iodine value
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- C10N2020/00—Specified physical or chemical properties or characteristics, i.e. function, of component of lubricating compositions
- C10N2020/01—Physico-chemical properties
- C10N2020/067—Unsaturated Compounds
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- C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
- C10N2030/06—Oiliness; Film-strength; Anti-wear; Resistance to extreme pressure
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- C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
- C10N2030/10—Inhibition of oxidation, e.g. anti-oxidants
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- 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
Definitions
- the present invention relates to additives from esters between polyols and Fatty acid mixtures and alkylphenol resins with improved oxidation stability, and their use to improve the lubricating effect of highly desulfurized fuel oils.
- Mineral oils and mineral oil distillates used as fuel oils generally contain 0.5 wt .-% and more sulfur, when burning causes the formation of sulfur dioxide. To the resulting To reduce environmental pollution, the sulfur content of fuel oils lowered further and further.
- the diesel fuel standard EN 590 writes in Europe since November 1999 a maximum sulfur content of 350 ppm. Further reductions in the sulfur content are in preparation. In Scandinavia come with fuel oils with less than 50 ppm and in exceptional cases less than 10 ppm sulfur to use. These fuel oils are used in the Usually made by making those from the petroleum by distillation obtained fractions hydrogenated refined. During the desulfurization also removes other substances that give the fuel oils a natural Give lubrication. These substances include, among others polyaromatic and polar compounds.
- EP-A-0 680 506 discloses that esters of fatty acids are desulfurized Give fuel oils an improved lubricating effect. It will be particularly Called glycerol monooleate and diisodecyl adipate.
- EP-A-0 739 970 discloses the suitability of glycerol ester mixtures for Improving the lubricity of low-sulfur fuel oils. It will Compositions of various degrees of esterification of the polyol and different degrees of saturation of the fatty acids disclosed.
- EP-A-0 839 174 discloses in their lubricating effect improved fuel oils which are low in sulfur and a mixture of polyol esters with unsaturated fatty acids include.
- EP 0743972 discloses fuel oils with improved lubricity, some Lubricity improvers and a nitrogen compound include.
- EP 0935645 discloses the use of C 1 -C 30 -alkylphenol resins as lubricity additives for low-sulfur diesel.
- the examples show C 18 and C 24 alkylphenol resins.
- WO-99/61562 discloses mixtures of alkylphenol resins, nitrogenous ones Compounds and ethylene copolymers as refrigeration and lubricity additives for low sulfur diesel.
- WO 01/19941 discloses partial esters of polyhydric alcohols with unsaturated ones Fatty acids (pentaerythritol esterified with tall oil fatty acid) as lubricity additives improved cold stability.
- Lubricity additives based on unsaturated fatty acids and their derivatives can with prolonged storage of the additive as well as the additive oils especially under elevated temperature to only partially oil-soluble products gum up. This can lead to the formation of viscous deposits and deposits in the additive storage container, in the fuel oil and in the engine. Stand like this z. B. the combustion and condensation products of glycerol suspected for Highly charged coke residues and deposits on the injection nozzles Diesel engines to be responsible.
- the fatty acid esters based on commercial fatty acid mixtures State of the art also show in the fuel oils additized with them pronounced tendency to emulsify. That means that when such a contact Fuel oil with water an emulsification of the water in the fuel oil takes place. These emulsions, particularly found at the oil / water phase boundary cannot be separated or only with great effort. As these emulsions as such can not be used as fuel oils, they reduce the value of Products. This problem is particularly pronounced when it comes to natural Fatty acid-based esters can be used.
- the object of the present invention was therefore to provide lubrication-improving additives for to find desulfurized fuel oils, one compared to the prior art improved oxidation stability and at the same time an improved effectiveness than Have lubricity additive.
- Another object of the invention are fuel oils with maximum 0.035 wt .-% sulfur content, which contain the additives according to the invention.
- Another object of the invention is the use of the invention Additives to improve the lubricating effect of fuel oils with at most 0.035% by weight sulfur content.
- Another object of the invention is a method for improving the Lubricating effect of fuel oils with a maximum sulfur content 0.035% by weight by adding the additive according to the invention to the fuel oils added.
- Preferred fatty acids which are part of the ester A) are those with 10 to 26 C atoms, in particular 12 to 22 C atoms.
- the alkyl residues or alkenyl residues of Fatty acids consist essentially of carbon and hydrogen. You can however other substituents such as e.g. Hydroxy, halogen, amino or nitro groups if they do not have the predominant hydrocarbon character affect.
- the fatty acids preferably contain at least one Double bond. You can have several double bonds, for example 2 or 3 Double bonds, contained and be of natural or synthetic origin. at polyunsaturated carboxylic acids can isolate their double bonds or also be conjugated. Mixtures of two or more unsaturated are preferred Fatty acids with 10 to 26 carbon atoms.
- fatty acid mixtures contain at least 50% by weight, in particular at least 75% by weight, specifically at least 90% by weight of the fatty acids contain one or more double bonds.
- the Iodine numbers of the fatty acids on which the esters according to the invention are based or Fatty acid mixtures are preferably above 100 g J / 100 g, particularly preferably between 105 and 190 g J / 100 g, in particular between 110 and 180 g J / 100 g and especially between 120 and 180 g l / 100 g fatty acid or fatty acid mixture.
- Suitable unsaturated fatty acids are, for example, oleic, eruca, palmitoleic, Myristoleic, linoleic, linolenic, elaeosteric, arachidonic and / or ricinoleic acid.
- those obtained from natural fats and oils are preferred Fatty acid mixtures or fractions, e.g. Peanut oil, fish, linseed oil, palm oil, Rapeseed oil, ricin oil, castor oil, rapeseed oil, soybean oil, sunflower oil, safflower and Tall oil fatty acid used, which have corresponding iodine numbers.
- fatty acids are dicarboxylic acids, such as dimer fatty acids and alkyl and alkenylsuccinic acids with C 8 -C 50 alk (en) yl radicals, preferably with C 8 -C 40 , in particular with C 12 -C 22 alkyl radicals.
- the alkyl radicals can be linear or branched (oligomerized alkenes, polyisobutylene) and saturated or unsaturated.
- the dicarboxylic acids can be used as such or in mixtures with monocarboxylic acids, with mixtures of dicarboxylic acids of up to 10% by weight, in particular less than 5% by weight, being preferred in mixtures.
- the fatty acid mixtures can have minor amounts, i.e. up to 20% by weight, preferably less than 10%, in particular less than 5% and especially less than 2% saturated fatty acids such as lauric, tridecane, Myristin, pentadecane, palmitin, margarine, stearin, isostearin, arachine and Contain beenic acid.
- minor amounts i.e. up to 20% by weight, preferably less than 10%, in particular less than 5% and especially less than 2% saturated fatty acids such as lauric, tridecane, Myristin, pentadecane, palmitin, margarine, stearin, isostearin, arachine and Contain beenic acid.
- the fatty acids can further 1-40, especially 1-25 wt .-%, in particular Contain 1-5 wt .-% resin acids.
- Suitable alcohols preferably contain 2 to 6, in particular 3 to 4 Carbon atoms, and 2 to 5, especially 3 to 4 hydroxyl groups, however a maximum of one hydroxyl group per carbon atom.
- Particularly suitable alcohols are ethylene glycol, diethylene glycol, propylene glycol, glycerin, trimethylolpropane, Neopentylglycol and pentaerythritol as well as the condensation accessible oligomers with 2 to 10 monomer units, such as Polyglycerol.
- the partial esters are made from alcohols and fatty acids in a known manner Esterification can be produced. Alternatively, partial saponification is natural occurring fats and oils possible.
- Esters according to the invention are those which consist of a di- or polyhydric alcohol and a fatty acid or a mixture can be produced from fatty acids. Both mixtures are made of, for example Mono-, di- and / or triesters, or possibly higher esters, of an alcohol various fatty acids, from mono-, di- and / or triesters, or possibly higher Esters, different alcohols with different fatty acids, as well Mixtures of mono-, di- and / or triesters, or possibly higher esters, one or several alcohols with different fatty acids. Those are preferred Esters that can be produced from a fatty acid mixture.
- the esters according to the invention preferably have iodine numbers of more than 50 g l / 100 g ester, particularly preferably between 90 and 200 g l / 100 g ester, in particular between 100 and 180 g l / 100 g ester and especially between 110 and 150 g l / 100 g ester.
- the iodine numbers result from the iodine number of the underlying fatty acid mixture and that used for the esterification Alcohol in a stoichiometric manner.
- partial esters whose OH numbers between 10 and 200 mg KOH / g ester are, particularly preferably between 100 and 200, in particular between 110 and 195, especially between 130 and 190 mg KOH / g ester.
- esters e.g. B. mixtures from mono-, di- and triglycerides, mixtures such as those used in the esterification of Polyols are created.
- alkylphenol-aldehyde resins (B) contained in the additive according to the invention are known in principle and are described, for example, in the Römpp Chemie Lexikon, 9th edition, Thieme Verlag 1988-92, Volume 4, pp. 3351ff. described.
- the alkyl or alkenyl radicals of the alkylphenol have 6-24, preferably 8-22, in particular 9-18, carbon atoms. They can be linear or preferably branched, the branching being able to contain secondary as well as tertiary structures.
- n- and iso-hexyl n- and iso-octyl, n- and iso-nonyl, n- and iso-decyl, n- and iso-dodecyl, tetradecyl, hexadecyl, octadecyl, eicosyl and tripropenyl, Tetrapropenyl, pentapropenyl and polyisobutenyl to C 24 .
- the prefix iso here means that the alkyl chain contains one or more secondary branches.
- the alkylphenol-aldehyde resin can also contain up to 20 mol% phenol units and / or alkylphenols with short alkyl chains such as e.g. B. contain butylphenol.
- alkylphenols can be used for the alkylphenol-aldehyde resin.
- the aldehyde in the alkylphenol-aldehyde resin has 1 to 10, preferably 1 to 4 Carbon atoms and can carry other functional groups. It is preferably a aliphatic aldehyde, particularly preferably it is formaldehyde.
- the molecular weight of the alkylphenol-aldehyde resins is preferably 350- 10,000, in particular 400 - 5000 g / mol. This preferably corresponds to one Degree of condensation n from 3 to 40, in particular from 4 to 20. Prerequisite here that the resins are oil-soluble.
- these alkylphenol-formaldehyde resins are those which contain oligomers or polymers with a repetitive structural unit of the formula are where R A is C 6 -C 24 alkyl or alkenyl and n is a number from 2 to 50.
- the alkylphenol-aldehyde resins are prepared in a known manner by basic catalysis, whereby condensation products of the resol type arise, or by acidic catalysis, producing condensation products of the novolak type.
- an alkylphenol with 6 - 24, preferably 8-22, in particular 9-18, carbon atoms per alkyl group, or mixtures thereof and at least one aldehyde reacted with one another, with per mol Alkylphenol compound about 0.5-2 moles, preferably 0.7-1.3 mol and in particular equimolar amounts of aldehyde can be used.
- Suitable alkylphenols are, in particular, n- and iso-hexylphenol, n- and iso-octylphenol, n- and iso-nonylphenol, n- and iso-decylphenol, n- and iso-dodecylphenol, tetradecylphenol, hexadecylphenol, octadecylphenol, eicosylphenol, tripropetraphenylphenol, tripropenylphenol (isobutenyl) phenol to C 24 .
- the alkylphenols are preferably para-substituted.
- the alkylphenols can be one or carry several alkyl radicals. They are preferably at most 5 mol%, especially at most 20 mol% and especially at most 40 mol% with more than an alkyl group. Preferably carry at most 40 mol%, in particular at most 20 mol% of the alkylphenols used in the ortho position an alkyl radical.
- the alkylphenols ortho to the hydroxyl group are not tertiary Alkyl groups substituted.
- the aldehyde can be a mono- or dialdehyde and other functional groups wear like -COOH.
- Particularly suitable aldehydes are formaldehyde, acetaldehyde, Butyraldehyde, glutardialdehyde and glyoxalic acid, formaldehyde is preferred.
- the Formaldehyde can be in the form of paraformaldehyde or in the form of a preferred 20 - 40 wt .-% aqueous formalin solution can be used. It can too appropriate amounts of trioxane can be used.
- alkylphenol and aldehyde usually takes place in the presence of alkaline catalysts, for example alkali hydroxides or alkylamines, or of acidic catalysts, for example inorganic or organic acids, such as hydrochloric acid, sulfuric acid, phosphoric acid, sulfonic acid, sulfamido acids or Haloacetic acids.
- alkaline catalysts for example alkali hydroxides or alkylamines
- acidic catalysts for example inorganic or organic acids, such as hydrochloric acid, sulfuric acid, phosphoric acid, sulfonic acid, sulfamido acids or Haloacetic acids.
- the condensation is preferably solvent-free at 90 to 200 ° C, preferably carried out at 100 to 160 ° C.
- a water Azeotropic organic solvent for example toluene, xylene, higher aromatics or mixtures thereof.
- the reaction mixture is on a Temperature of 90 to 200 ° C, preferably 100-160 ° C heated, the resulting Water of reaction is removed during the reaction by azeotropic distillation. Solvent that does not have protons under the conditions of condensation split off, can remain in the products after the condensation reaction.
- the Resins can be used directly or after neutralization of the catalyst, optionally after further dilution of the solution with aliphatic and / or aromatic hydrocarbons or hydrocarbon mixtures, e.g.
- the proportions by weight of components A) and B) in the additives according to the invention can vary widely depending on the application. They lay preferably between 10 and 99.999% by weight A) to 90 to 0.001% by weight B), in particular between 20 and 99.995% by weight A) to 80 to 0.005% by weight B). there to stabilize the fatty acids, smaller portions of the Components B from 0.001 to 10% by weight, preferably 0.005 to 5% by weight B) used, whereas to optimize the lubricity larger portions B of for example 5 to 90 wt .-%, preferably 10 to 80 wt .-% and in particular 25 to 75 wt .-% are used.
- Paraffin dispersants are additives that increase the size when the oil cools reduce the precipitated paraffin crystals and also cause the Paraffin particles do not settle, but colloidally with significantly reduced Sedimentation efforts, remain dispersed.
- the nitrogen-containing paraffin dispersants are preferably low molecular weight or polymeric, oil-soluble nitrogen compounds, e.g. Amine salts, Imides and / or amides obtained by reaction of aliphatic or aromatic amines, preferably long-chain aliphatic amines, with aliphatic or aromatic Obtain mono-, di-, tri-, tetra- and / or polycarboxylic acids or their anhydrides become.
- Contain particularly preferred paraffin dispersants Reaction products of secondary fatty amines with 8 to 36 carbon atoms, in particular Dicocos fatty amine, ditallow fatty amine and distearyl amine.
- paraffin dispersants are copolymers of maleic anhydride and ⁇ , ⁇ -unsaturated compounds, optionally with primary monoalkylamines and / or aliphatic alcohols can be implemented with the reaction products of alkenylspirobislactones Amines and reaction products of terpolymers based on ⁇ , ⁇ -unsaturated Dicarboxylic anhydrides, ⁇ , ⁇ -unsaturated compounds and polyoxyalkylene ethers lower unsaturated alcohols with amines and / or alcohols.
- suitable paraffin dispersants are listed.
- the polar nitrogen-containing paraffin dispersants can be the inventive Additives are added or added separately to the middle distillate to be added become.
- the quantitative ratio between paraffin dispersants and Additives according to the invention are between 5: 1 and 1: 5 and preferably between 3: 1 and 1: 3.
- additives according to the invention also together with one or more oil-soluble Co-additives are used, which alone have the lubricating effect and / or Improve the cold flow properties of crude oils, lubricating oils or fuel oils.
- oil-soluble Co-additives are copolymers containing vinyl acetate or Terpolymers of ethylene, comb polymers and oil-soluble amphiphiles.
- the additives according to the invention in a mixture with ethylene / vinyl acetate / vinyl 2-ethylhexanoate terpolymers, Ethylene / vinyl acetate / neononanoic acid vinyl ester terpolymers and / or ethylene vinyl acetate / vinyl neodecanoate terpolymers to improve the flowability and lubrication of Mineral oils or mineral oil distillates.
- neodecanoic acid vinyl esters contain 10 to 35% by weight of vinyl acetate and 1 to 25 wt .-% of the respective long-chain vinyl ester. More preferred In addition to ethylene and 10 to 35% by weight of vinyl esters, copolymers also contain 0.5 to 20 wt .-% olefin with 3 to 10 carbon atoms such.
- the additives according to the invention are used together with comb polymers.
- comb polymers This is understood to mean polymers in which hydrocarbon radicals having at least 8, in particular at least 10, carbon atoms are bonded to a polymer backbone. They are preferably homopolymers whose alkyl side chains contain at least 8 and in particular at least 10 carbon atoms. In the case of copolymers, at least 20%, preferably at least 30%, of the monomers have side chains (cf. Comb-like Polymers-Structure and Properties; NA Platé and VP Shibaev, J. Polym. Sci. Macromolecular Revs. 1974, 8, 117 ff).
- Suitable comb polymers are, for example, fumarate / vinyl acetate copolymers (cf. EP 0 153 176 A1), copolymers of a C 6 -C 24 ⁇ -olefin and an NC 6 -C 22 alkylmaleimide (cf. EP 0 320 766) , further esterified olefin / maleic anhydride copolymers, polymers and copolymers of ⁇ -olefins and esterified copolymers of styrene and maleic anhydride.
- fumarate / vinyl acetate copolymers cf. EP 0 153 176 A1
- copolymers of a C 6 -C 24 ⁇ -olefin and an NC 6 -C 22 alkylmaleimide cf. EP 0 320 766
- further esterified olefin / maleic anhydride copolymers polymers and copolymers of ⁇ -
- the mixing ratio (in parts by weight) of the additives according to the invention Ethylene copolymers or comb polymers are each 1:10 to 20: 1, preferably 1: 1 to 10: 1.
- the additives of the invention are oiled in amounts from 0.0001 to 1% by weight, preferably 0.001 to 0.1% by weight and especially 0.002 to 0.05% by weight added. They can be used as such or dissolved in solvents such as e.g. aliphatic and / or aromatic hydrocarbons or Hydrocarbon mixtures such as Toluene, xylene, ethylbenzene, decane, Pentadecane, gasoline fractions, diesel, kerosene or commercial Solvent mixtures such as Solvent Naphtha, ® Shellsol AB, ® Solvesso 150, ® Solvesso 200, ® Exxsol, ® Isopar and ® Shellsol D types, as well as polar solvents such as Alcohols, glycols and esters such as fatty acid alkyl esters and in particular rapeseed oleic acid methyl ester (RME).
- the additives according to the invention can be used at elevated temperature for a long time stored without aging effects, without causing signs of aging such as resinification and the formation of insoluble structures or deposits in Storage containers and / or engine parts comes. They also improve the Oxidation stability of the additive oils with reduced at the same time Emulsify. This is especially true with oils that are made up of larger proportions of oils Crack processes included, beneficial.
- Lubricity of middle distillates This can be used for setting the specification required dosage rate can be reduced.
- Another advantage of the additives according to the invention is that of the additives according to state of the art fatty acid esters used as lubricity additives reduced crystallization temperature. So you can even at low Temperatures of, for example, 0 ° C to -20 ° C and sometimes also lower can be used without any problems.
- the additives of the invention are for use in middle distillates particularly suitable.
- Middle distillates are especially those Mineral oils obtained from crude oil distillation and in the range of Boil 120 to 450 ° C, for example kerosene, jet fuel, diesel and heating oil.
- the oils may also contain or from alcohols such as methanol and / or ethanol consist.
- the additives according to the invention are preferably used in such Middle distillates used that contain less than 350 ppm sulfur, in particular less than 200 ppm sulfur and in special cases less than 50 ppm or contain less than 10 ppm sulfur. It is generally about those middle distillates which have been subjected to hydrogenating refining, and which therefore only contains small amounts of polyaromatic and polar compounds contain, which give them a natural lubricating effect.
- the Additives according to the invention are also preferably used in such Middle distillates used, the 95% distillation points below 370 ° C, in particular 350 ° C and in special cases below 330 ° C. They are the same additives according to the invention for use in synthetic fuels also low lubricity, as z. B. in Fischer-Tropsch erosion can be produced, suitable.
- the oils with improved lubricity have a wear scar diameter of preferred measured in the HFRR test less than 460 ⁇ m, especially less than 450 ⁇ m.
- the additives according to the invention can also be used as components in lubricating oils.
- the mixtures can be used alone or together with other additives be used, e.g. with pour point depressants, corrosion inhibitors, Antioxidants, sludge inhibitors, dehazers, conductivity improvers, lubricity additives, and additives to lower the cloud point.
- additive packages that include known ashless dispersion additives, detergents, defoamers, antioxidants, dehazers, Demulsifiers and corrosion inhibitors included.
- Test oil 1 Test oil 2
- Test oil 3 distillation IBP [° C] 202 182 164 20% [° C] 237 221 214 90% [° C] 321 280 342
- FBP [° C] 348 304 367 Cloud Point [° C] -5.9 -29.7 -7.7 CFPP [° C] -8th -33 -13
- the additives used are characterized below.
- the OH numbers were in accordance with DIN 53240 by implementation with a defined amount excess acetic anhydride and subsequent titration of the formed Acetic acid determined.
- Iodine numbers are determined according to Kaufmann. For this purpose, a defined amount of a methanolic bromine solution is added to the sample, an amount of bromine which is equivalent to the content of double bonds being deposited. The excess bromine is back-titrated with sodium thiosulfate.
- a mixture of 9 g A 7, 1 g B1 and 2 g C2 gave after three days of storage 90 ° C and then diluted with 500 ml test oil 3 a clear solution and a filtration time of 65 s.
- the lubricating effect of the additives was tested using an HFRR device from PCS Instruments on additive oils at 60 ° C.
- the high frequency Reciprocating Rig Test (HFRR) is described in D. Wei, H. Spikes, Wear, Vol. 111, No. 2, p. 217, 1986.
- the results are given as the coefficient of friction and wear scar (WS 1.4).
- a low wear scar and a low coefficient of friction (friction) show a good lubricating effect.
- Wear scar values of less than 460 ⁇ m are regarded as an indication of a sufficient lubricating effect, although in practice values of less than 400 ⁇ m are aimed for.
- the dosing rates in Table 6 relate to the amount of active ingredient dosed.
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Abstract
Description
Die vorliegende Erfindung betrifft Additive aus Estern zwischen Polyolen und Fettsäuregemischen und Alkylphenolharzen mit verbesserter Oxidationsstabilität, sowie deren Verwendung zur Verbesserung der Schmierwirkung von hochentschwefelten Brennstoffölen.The present invention relates to additives from esters between polyols and Fatty acid mixtures and alkylphenol resins with improved oxidation stability, and their use to improve the lubricating effect of highly desulfurized fuel oils.
Mineralöle und Mineralöldestillate, die als Brennstofföle verwendet werden, enthalten im allgemeinen 0,5 Gew.-% und mehr Schwefel, der bei der Verbrennung die Bildung von Schwefeldioxid verursacht. Um die daraus resultierenden Umweltbelastungen zu vermindern, wird der Schwefelgehalt von Brennstoffölen immer weiter abgesenkt. Die Dieseltreibstoffe betreffende Norm EN 590 schreibt in Europa seit November 1999 einen maximalen Schwefelgehalt von 350 ppm vor. Weitere Absenkungen des Schwefelgehalts sind in Vorbereitung. In Skandinavien kommen bereits Brennstofföle mit weniger als 50 ppm und in Ausnahmefällen mit weniger als 10 ppm Schwefel zur Anwendung. Diese Brennstofföle werden in der Regel dadurch hergestellt, dass man die aus dem Erdöl durch Destillation erhaltenen Fraktionen hydrierend raffiniert. Bei der Entschwefelung werden aber auch andere Substanzen entfernt, die den Brennstoffölen eine natürliche Schmierwirkung verleihen. Zu diesen Substanzen zählen unter anderem polyaromatische und polare Verbindungen.Mineral oils and mineral oil distillates used as fuel oils generally contain 0.5 wt .-% and more sulfur, when burning causes the formation of sulfur dioxide. To the resulting To reduce environmental pollution, the sulfur content of fuel oils lowered further and further. The diesel fuel standard EN 590 writes in Europe since November 1999 a maximum sulfur content of 350 ppm. Further reductions in the sulfur content are in preparation. In Scandinavia come with fuel oils with less than 50 ppm and in exceptional cases less than 10 ppm sulfur to use. These fuel oils are used in the Usually made by making those from the petroleum by distillation obtained fractions hydrogenated refined. During the desulfurization also removes other substances that give the fuel oils a natural Give lubrication. These substances include, among others polyaromatic and polar compounds.
Es hat sich nun aber gezeigt, dass die reibungs- und verschleißmindernden
Eigenschaften von Brennstoffölen mit zunehmendem Entschwefelungsgrad
schlechter werden. Oftmals sind diese Eigenschaften so mangelhaft, dass an den
vom Kraftstoff geschmierten Materialien, wie z.B. den Verteiler-Einspritzpumpen von
Dieselmotoren schon nach kurzer Zeit mit Fraßerscheinungen gerechnet werden
muss. Der gemäß EN 590 seit dem Jahr 2000 festgesetzte Maximalwert für den
95%-Destillationspunkt von maximal 360°C und die mittlerweile in Skandinavien
vorgenommene weitere Absenkung des 95%-Destillationspunkts auf unter 350°C
und teilweise unter 330°C verschärft diese Problematik weiter.
Im Stand der Technik sind daher Ansätze beschrieben, die eine Lösung dieses
Problems darstellen sollen (sogenannte Lubricity-Additive).However, it has now been shown that the friction and wear-reducing properties of fuel oils deteriorate as the level of desulfurization increases. Often these properties are so inadequate that the materials lubricated by the fuel, such as the distributor injection pumps of diesel engines, are likely to start seizing after a short time. The maximum value for the 95% distillation point of maximum 360 ° C, which has been set in accordance with EN 590 since 2000, and the further reduction of the 95% distillation point to below 350 ° C and sometimes below 330 ° C in Scandinavia further exacerbates this problem.
Approaches are therefore described in the prior art which are intended to represent a solution to this problem (so-called lubricity additives).
EP-A-0 680 506 offenbart, dass Ester von Fettsäuren hochentschwefelten Brennstoffölen eine verbesserte Schmierwirkung verleihen. Es werden insbesondere Glycerinmonooleat und Diisodecyladipat genannt.EP-A-0 680 506 discloses that esters of fatty acids are desulfurized Give fuel oils an improved lubricating effect. It will be particularly Called glycerol monooleate and diisodecyl adipate.
EP-A-0 739 970 offenbart die Eignung von Glycerinestergemischen zur Verbesserung der Schmierfähigkeit von schwefelarmen Brennstoffölen. Es werden Zusammensetzungen verschiedener Veresterungsgrade des Polyols und verschiedener Sättigungsgrade der Fettsäuren offenbart.EP-A-0 739 970 discloses the suitability of glycerol ester mixtures for Improving the lubricity of low-sulfur fuel oils. It will Compositions of various degrees of esterification of the polyol and different degrees of saturation of the fatty acids disclosed.
EP-A-0 839 174 offenbart in ihrer Schmierwirkung verbesserte Brennstofföle, die schwefelarm sind und eine Mischung von Polyolestern mit ungesättigten Fettsäuren umfassen.EP-A-0 839 174 discloses in their lubricating effect improved fuel oils which are low in sulfur and a mixture of polyol esters with unsaturated fatty acids include.
DE 19614722 offenbart Mischungen von Partialestern hoch ungesättigter Fettsäuren mit verschiedenen Polyolen mit verbesserter Kältestabilität. Diese können unter anderem auch schwefelarmen Dieselölen als Schmieradditive zugesetzt werden.DE 19614722 discloses mixtures of partial esters of highly unsaturated fatty acids with various polyols with improved cold stability. These can be found at low-sulfur diesel oils can also be added as lubricating additives.
EP 0743972 offenbart Brennstofföle mit verbesserter Lubricity, die einen Schmierfähigkeitsverbesserer und eine Stickstoffverbindung umfassen.EP 0743972 discloses fuel oils with improved lubricity, some Lubricity improvers and a nitrogen compound include.
EP 0935645 offenbart die Verwendung von C1-C30-Alkylphenolharzen als Lubricity-Additive für schwefelarmen Diesel. In den Beispielen belegt sind C18- und C24-Alkylphenolharze.EP 0935645 discloses the use of C 1 -C 30 -alkylphenol resins as lubricity additives for low-sulfur diesel. The examples show C 18 and C 24 alkylphenol resins.
WO-99/61562 offenbart Mischungen aus Alkylphenolharzen, stickstoffhaltigen Verbindungen und Ethylen-Copolymeren als Kälte- und Lubricity-Additive für schwefelarmen Diesel.WO-99/61562 discloses mixtures of alkylphenol resins, nitrogenous ones Compounds and ethylene copolymers as refrigeration and lubricity additives for low sulfur diesel.
WO 01/19941 offenbart Partialester mehrwertiger Alkohole mit ungesättigten Fettsäuren (Pentaerythritol verestert mit Tallölfettsäure) als Lubricity-Additive mit verbesserter Kältestabilität.WO 01/19941 discloses partial esters of polyhydric alcohols with unsaturated ones Fatty acids (pentaerythritol esterified with tall oil fatty acid) as lubricity additives improved cold stability.
Die auf ungesättigten Fettsäuren und deren Derivaten basierenden Lubricity-Additive können bei längerer Lagerung des Additivs wie auch der additivierten Öle insbesondere unter erhöhter Temperatur zu nur noch bedingt öllöslichen Produkten verharzen. Dies kann zur Bildung von viskosen Ausscheidungen und Ablagerungen im Lagerbehälter des Additivs, im Brennstofföl wie auch im Motor führen. So stehen z. B. die Verbrennungs- und Kondensationsprodukte des Glycerins im Verdacht, für Koksrückstände und Ablagerungen an den Einspritzdüsen hochaufgeladener Dieselmotoren verantwortlich zu sein.Lubricity additives based on unsaturated fatty acids and their derivatives can with prolonged storage of the additive as well as the additive oils especially under elevated temperature to only partially oil-soluble products gum up. This can lead to the formation of viscous deposits and deposits in the additive storage container, in the fuel oil and in the engine. Stand like this z. B. the combustion and condensation products of glycerol suspected for Highly charged coke residues and deposits on the injection nozzles Diesel engines to be responsible.
Die Wirksamkeit der derzeit eingesetzten Lubricity-Additive ist oftmals unbefriedigend, so daß entweder sehr hohe Dosierraten oder Synergisten eingesetzt werden müssen.The effectiveness of the lubricity additives currently used is often unsatisfactory, so that either very high dosing rates or synergists are used Need to become.
Die auf kommerziellen Fettsäuremischungen basierenden Fettsäureester des Standes der Technik zeigen zudem in den mit ihnen additivierten Brennstoffölen eine ausgeprägte Emulgierneigung. Das bedeutet, dass bei Kontakt eines solchen Brennstofföls mit Wasser eine Emulgierung des Wassers im Brennstofföl stattfindet. Diese insbesondere an der Phasengrenze Öl/Wasser anzutreffenden Emulsionen lassen sich nicht oder nur unter großem Aufwand trennen. Da diese Emulsionen als solche nicht als Brennstofföle eingesetzt werden können, mindern sie den Wert der Produkte. Besonders stark tritt dieses Problem dann hervor, wenn auf natürlichen Fettsäuregemischen basierende Ester verwendet werden.The fatty acid esters based on commercial fatty acid mixtures State of the art also show in the fuel oils additized with them pronounced tendency to emulsify. That means that when such a contact Fuel oil with water an emulsification of the water in the fuel oil takes place. These emulsions, particularly found at the oil / water phase boundary cannot be separated or only with great effort. As these emulsions as such can not be used as fuel oils, they reduce the value of Products. This problem is particularly pronounced when it comes to natural Fatty acid-based esters can be used.
Aufgabe vorliegender Erfindung war daher, schmierverbessernde Zusätze für entschwefelte Brennstofföle zu finden, die eine gegenüber dem Stand der Technik verbesserte Oxidationsstabilität und gleichzeitig eine verbesserte Wirksamkeit als Lubricity-Additiv aufweisen.The object of the present invention was therefore to provide lubrication-improving additives for to find desulfurized fuel oils, one compared to the prior art improved oxidation stability and at the same time an improved effectiveness than Have lubricity additive.
Überraschenderweise wurde gefunden, dass Kombinationen von Partialestern aus ungesättigten Fettsäuren und Polyolen mit Alkylphenol-Aldehydharzen eine deutlich verbesserte Oxidationsstabilität aufweisen und bei ausgewählten Kombinationen aus Hydroxylzahl und Jodzahl eine besonders geringe Emulgierfähigkeit aufweisen. Des weiteren zeigen sie in schwefelarmen Brennstoffölen eine den Einzelbestandteilen überlegene Schmierwirkung.Surprisingly, it was found that combinations of partial esters unsaturated fatty acids and polyols with alkylphenol-aldehyde resins a clearly have improved oxidation stability and selected combinations Hydroxyl number and iodine number have a particularly low emulsifiability. Of they also show the individual components in low-sulfur fuel oils superior lubrication.
Gegenstand der Erfindung ist daher ein Additiv zur Verbesserung der
Schmierfähigkeit von Brennstoffölen mit einem Schwefelgehalt von maximal
0,035 Gew.-%, enthaltend
Ein weiterer Gegenstand der Erfindung sind Brennstofföle mit maximal 0,035 Gew.-% Schwefelgehalt, die die erfindungsgemäßen Additive enthalten.Another object of the invention are fuel oils with maximum 0.035 wt .-% sulfur content, which contain the additives according to the invention.
Ein weiterer Gegenstand der Erfindung ist die Verwendung der erfindungsgemäßen Additive zur Verbesserung der Schmierwirkung von Brennstoffölen mit höchstens 0,035 Gew.-% Schwefelgehalt.Another object of the invention is the use of the invention Additives to improve the lubricating effect of fuel oils with at most 0.035% by weight sulfur content.
Ein weiterer Gegenstand der Erfindung ist ein Verfahren zur Verbesserung der Schmierwirkung von Brennstoffölen mit einem Schwefelgehalt von maximal 0,035 Gew.-%, indem man den Brennstoffölen das erfindungsgemäße Additiv zusetzt.Another object of the invention is a method for improving the Lubricating effect of fuel oils with a maximum sulfur content 0.035% by weight by adding the additive according to the invention to the fuel oils added.
Bevorzugte Fettsäuren, die Bestandteil der Ester A) sind, sind solche mit 10 bis 26 C-Atomen, insbesondere 12 bis 22 C-Atomen. Die Alkylreste bzw. Alkenylreste der Fettsäuren bestehen im wesentlichen aus Kohlenstoff und Wasserstoff. Sie können jedoch weitere Substituenten wie z.B. Hydroxy-, Halogen-, Amino- oder Nitrogruppen tragen, sofern diese den vorwiegenden Kohlenwasserstoffcharakter nicht beeinträchtigen. Die Fettsäuren enthalten vorzugsweise mindestens eine Doppelbindung. Sie können mehrere Doppelbindungen, beispielsweise 2 oder 3 Doppelbindungen, enthalten und natürlicher oder synthetischer Herkunft sein. Bei mehrfach ungesättigten Carbonsäuren können deren Doppelbindungen isoliert oder auch konjugiert sein. Bevorzugt sind Mischungen aus zwei oder mehr ungesättigten Fettsäuren mit 10 bis 26 C-Atomen. In besonders bevorzugten Fettsäuremischungen enthalten mindestens 50 Gew.-%, insbesondere mindestens 75 Gew.-%, speziell mindestens 90 Gew.-% der Fettsäuren eine oder mehrere Doppelbindungen. Die Jodzahlen der den erfindungsgemäßen Estern zugrunde liegenden Fettsäuren bzw. Fettsäuregemische liegen bevorzugt oberhalb 100 g J/100 g, besonders bevorzugt zwischen 105 und 190 g J/100 g, insbesondere zwischen 110 und 180 g J/100 g und speziell zwischen 120 und 180 g l/100 g Fettsäure bzw. Fettsäuregemisch.Preferred fatty acids which are part of the ester A) are those with 10 to 26 C atoms, in particular 12 to 22 C atoms. The alkyl residues or alkenyl residues of Fatty acids consist essentially of carbon and hydrogen. You can however other substituents such as e.g. Hydroxy, halogen, amino or nitro groups if they do not have the predominant hydrocarbon character affect. The fatty acids preferably contain at least one Double bond. You can have several double bonds, for example 2 or 3 Double bonds, contained and be of natural or synthetic origin. at polyunsaturated carboxylic acids can isolate their double bonds or also be conjugated. Mixtures of two or more unsaturated are preferred Fatty acids with 10 to 26 carbon atoms. In particularly preferred fatty acid mixtures contain at least 50% by weight, in particular at least 75% by weight, specifically at least 90% by weight of the fatty acids contain one or more double bonds. The Iodine numbers of the fatty acids on which the esters according to the invention are based or Fatty acid mixtures are preferably above 100 g J / 100 g, particularly preferably between 105 and 190 g J / 100 g, in particular between 110 and 180 g J / 100 g and especially between 120 and 180 g l / 100 g fatty acid or fatty acid mixture.
Geeignete ungesättigte Fettsäuren sind beispielsweise Öl-, Eruca-, Palmitolein-, Myristolein-, Linol-, Linolen-, Elaeosterin-, Arachidon- und/oder Ricinolsäure. Bevorzugt werden erfindungsgemäß aus natürlichen Fetten und Ölen gewonnene Fettsäuremischungen bzw. -fraktionen, wie z.B. Erdnussöl-, Fisch-, Leinöl-, Palmöl-, Rapsöl-, Ricinen-, Ricinusöl-, Rüböl-, Sojaöl-, Sonnenblumenöl-, Färberdistel- und Tallölfettsäure eingesetzt, die entsprechende Jodzahlen aufweisen.Suitable unsaturated fatty acids are, for example, oleic, eruca, palmitoleic, Myristoleic, linoleic, linolenic, elaeosteric, arachidonic and / or ricinoleic acid. According to the invention, those obtained from natural fats and oils are preferred Fatty acid mixtures or fractions, e.g. Peanut oil, fish, linseed oil, palm oil, Rapeseed oil, ricin oil, castor oil, rapeseed oil, soybean oil, sunflower oil, safflower and Tall oil fatty acid used, which have corresponding iodine numbers.
Als Fettsäuren ebenfalls geeignet sind Dicarbonsäuren, wie Dimerfettsäuren und Alkyl- sowie Alkenylbernsteinsäuren mit C8-C50-Alk(en)ylresten, bevorzugt mit C8-C40-, insbesondere mit C12-C22-Alkylresten. Die Alkylreste können linear wie auch verzweigt (oligomerisierte Alkene, Polyisobutylen) und gesättigt oder ungesättigt sein. Die Dicarbonsäuren können als solche oder in Mischungen mit Monocarbonsäuren eingesetzt werden, wobei in Mischungen Anteile der Dicarbonsäuren von bis zu 10 Gew.-%, insbesondere weniger als 5 Gew.-% bevorzugt sind.Also suitable as fatty acids are dicarboxylic acids, such as dimer fatty acids and alkyl and alkenylsuccinic acids with C 8 -C 50 alk (en) yl radicals, preferably with C 8 -C 40 , in particular with C 12 -C 22 alkyl radicals. The alkyl radicals can be linear or branched (oligomerized alkenes, polyisobutylene) and saturated or unsaturated. The dicarboxylic acids can be used as such or in mixtures with monocarboxylic acids, with mixtures of dicarboxylic acids of up to 10% by weight, in particular less than 5% by weight, being preferred in mixtures.
Daneben können die Fettsäuremischungen untergeordnete Mengen, d.h. bis zu 20 Gew.-%, bevorzugt weniger als 10%, insbesondere weniger als 5 % und speziell weniger als 2 % gesättigter Fettsäuren wie beispielsweise Laurin-, Tridecan-, Myristin-, Pentadecan-, Palmitin-, Margarin-, Stearin-, Isostearin-, Arachin- und Behensäure enthalten.In addition, the fatty acid mixtures can have minor amounts, i.e. up to 20% by weight, preferably less than 10%, in particular less than 5% and especially less than 2% saturated fatty acids such as lauric, tridecane, Myristin, pentadecane, palmitin, margarine, stearin, isostearin, arachine and Contain beenic acid.
Die Fettsäuren können weiterhin 1-40, speziell 1-25 Gew.-%, insbesondere 1-5 Gew.-% Harzsäuren enthalten.The fatty acids can further 1-40, especially 1-25 wt .-%, in particular Contain 1-5 wt .-% resin acids.
Geeignete Alkohole enthalten vorzugsweise 2 bis 6, insbesondere 3 bis 4 Kohlenstorfatome, und 2 bis 5, insbesondere 3 bis 4 Hydroxylgruppen, jedoch maximal eine Hydroxylgruppe pro Kohlenstoffatom. Besonders geeignete Alkohole sind Ethylenglykol, Diethylenglykol, Propylenglykol, Glycerin, Trimethylolpropan, Neopentylglykol und Pentaerythritol sowie die daraus durch Kondensation zugänglichen Oligomere mit 2 bis 10 Monomereinheiten, wie beispielsweise Polyglycerin.Suitable alcohols preferably contain 2 to 6, in particular 3 to 4 Carbon atoms, and 2 to 5, especially 3 to 4 hydroxyl groups, however a maximum of one hydroxyl group per carbon atom. Particularly suitable alcohols are ethylene glycol, diethylene glycol, propylene glycol, glycerin, trimethylolpropane, Neopentylglycol and pentaerythritol as well as the condensation accessible oligomers with 2 to 10 monomer units, such as Polyglycerol.
Die Partialester sind aus Alkoholen und Fettsäuren in bekannter Weise durch Veresterung herstellbar. Alternativ ist auch die partielle Verseifung natürlich vorkommender Fette und Öle möglich. Erfindungsgemäße Ester sind solche, die aus einem zwei- oder mehrwertigen Alkohol und einer Fettsäure oder einem Gemisch von Fettsäuren herstellbar sind. Hierbei sind sowohl Mischungen beispielsweise aus Mono-, Di- und/oder Triestern, oder ggf. höheren Estern, eines Alkohols mit verschiedenen Fettsäuren, aus Mono-, Di- und/oder Triestern, oder ggf. höheren Estern, verschiedener Alkohole mit verschiedenen Fettsäuren, als auch aus Mischungen von Mono-, Di- und/oder Triestern, oder ggf. höheren Estern, eines oder mehrerer Alkohole mit verschiedenen Fettsäuren umfasst. Bevorzugt sind solche Ester, die aus einem Fettsäuregemisch herstellbar sind.The partial esters are made from alcohols and fatty acids in a known manner Esterification can be produced. Alternatively, partial saponification is natural occurring fats and oils possible. Esters according to the invention are those which consist of a di- or polyhydric alcohol and a fatty acid or a mixture can be produced from fatty acids. Both mixtures are made of, for example Mono-, di- and / or triesters, or possibly higher esters, of an alcohol various fatty acids, from mono-, di- and / or triesters, or possibly higher Esters, different alcohols with different fatty acids, as well Mixtures of mono-, di- and / or triesters, or possibly higher esters, one or several alcohols with different fatty acids. Those are preferred Esters that can be produced from a fatty acid mixture.
Bevorzugt weisen die erfindungsgemäßen Ester Jodzahlen von mehr als 50 g l/100 g Ester auf, besonders bevorzugt liegen sie zwischen 90 und 200 g l/100 g Ester, insbesondere zwischen 100 und 180 g l/100 g Ester und speziell zwischen 110 und 150 g l/100 g Ester. Die Jodzahlen ergeben sich aus der Jodzahl des zugrundeliegenden Fettsäuregemischs und dem zur Veresterung verwendeten Alkohol in stöchiometrischer Weise. The esters according to the invention preferably have iodine numbers of more than 50 g l / 100 g ester, particularly preferably between 90 and 200 g l / 100 g ester, in particular between 100 and 180 g l / 100 g ester and especially between 110 and 150 g l / 100 g ester. The iodine numbers result from the iodine number of the underlying fatty acid mixture and that used for the esterification Alcohol in a stoichiometric manner.
Bevorzugt sind ebenfalls Partialester, deren OH-Zahlen zwischen 10 und 200 mg KOH/g Ester liegen, besonders bevorzugt zwischen 100 und 200, insbesondere zwischen 110 und 195, speziell zwischen 130 und 190 mg KOH/g Ester. In der Regel handelt es sich dabei um Mischungen verschiedener Ester, z. B. um Mischungen aus Mono- Di- und Triglyceriden, Mischungen, wie sie bei der Veresterung von Polyolen entstehen.Also preferred are partial esters whose OH numbers between 10 and 200 mg KOH / g ester are, particularly preferably between 100 and 200, in particular between 110 and 195, especially between 130 and 190 mg KOH / g ester. Usually these are mixtures of different esters, e.g. B. mixtures from mono-, di- and triglycerides, mixtures such as those used in the esterification of Polyols are created.
Die Partialester mit OH-Zahlen zwischen 110 und 200 mg KOH/g Ester zeichnen sich insbesondere in Kombination mit den Alkylphenolharzen B) durch eine sehr geringe Emulgierneigung aus. Vermutlich bewirkt dabei der durch die OH-Zahl begrenzte HLB-Bereich der Additive eine reduzierte Affinität der amphiphilen Wirkstoffe zu Wasser; gleichzeitig wird die Ausbildung oberflächenaktiver und micellarer Strukturen durch die mittels Jodzahl charakterisierte Anzahl an Doppelbindungen in den Alkylresten gestört.Draw the partial esters with OH numbers between 110 and 200 mg KOH / g ester especially in combination with the alkylphenol resins B) through a very low tendency to emulsify. This is probably caused by the OH number limited HLB range of additives a reduced affinity of the amphiphilic Active substances to water; at the same time, the training becomes more surface active and micellar structures by the number characterized by iodine number Double bonds in the alkyl residues disturbed.
Die im erfindungsgemäßen Additiv enthaltenen Alkylphenol-Aldehyd-Harze (B) sind prinzipiell bekannt und beispielsweise im Römpp Chemie Lexikon, 9. Auflage, Thieme Verlag 1988-92, Band 4, S. 3351ff. beschrieben. Die Alkyl- oder Alkenylreste des Alkylphenols besitzen 6 - 24, bevorzugt 8 - 22, insbesondere 9-18 Kohlenstoffatome. Sie können linear oder bevorzugt verzweigt sein, wobei die Verzweigung sekundäre wie auch tertiäre Strukturen enthalten kann. Bevorzugt handelt es sich um n- und iso-Hexyl, n- und iso-Octyl, n- und iso-Nonyl, n- und iso-Decyl, n- und iso-Dodecyl, Tetradecyl, Hexadecyl, Octadecyl, Eicosyl sowie Tripropenyl, Tetrapropenyl, Pentapropenyl und Polyisobutenyl bis C24. Der Präfix iso bedeutet hier, daß die Alkylkette eine oder mehrere sekundäre Verzweigungen enthält. Das Alkylphenol-Aldehyd-Harz kann auch bis zu 20 mol-% Phenoleinheiten und/oder Alkylphenole mit kurzen Alkyketten wie z. B. Butylphenol enthalten. Für das Alkylphenol-Aldehydharz können gleiche oder verschiedene Alkylphenole verwendet werden.The alkylphenol-aldehyde resins (B) contained in the additive according to the invention are known in principle and are described, for example, in the Römpp Chemie Lexikon, 9th edition, Thieme Verlag 1988-92, Volume 4, pp. 3351ff. described. The alkyl or alkenyl radicals of the alkylphenol have 6-24, preferably 8-22, in particular 9-18, carbon atoms. They can be linear or preferably branched, the branching being able to contain secondary as well as tertiary structures. It is preferably n- and iso-hexyl, n- and iso-octyl, n- and iso-nonyl, n- and iso-decyl, n- and iso-dodecyl, tetradecyl, hexadecyl, octadecyl, eicosyl and tripropenyl, Tetrapropenyl, pentapropenyl and polyisobutenyl to C 24 . The prefix iso here means that the alkyl chain contains one or more secondary branches. The alkylphenol-aldehyde resin can also contain up to 20 mol% phenol units and / or alkylphenols with short alkyl chains such as e.g. B. contain butylphenol. The same or different alkylphenols can be used for the alkylphenol-aldehyde resin.
Der Aldehyd im Alkylphenol-Aldehyd-Harz besitzt 1 bis 10, bevorzugt 1 bis 4 Kohlenstoffatome und kann weitere funktionelle Gruppen tragen. Bevorzugt ist er ein aliphatischer Aldehyd, besonders bevorzugt ist er Formaldehyd. The aldehyde in the alkylphenol-aldehyde resin has 1 to 10, preferably 1 to 4 Carbon atoms and can carry other functional groups. It is preferably a aliphatic aldehyde, particularly preferably it is formaldehyde.
Das Molekulargewicht der Alkylphenol-Aldehyd-Harze beträgt vorzugsweise 350 - 10.000, insbesondere 400 - 5000 g/mol. Bevorzugt entspricht dies einem Kondensationsgrad n von 3 bis 40, insbesondere von 4 bis 20. Voraussetzung ist hierbei, dass die Harze öllöslich sind.The molecular weight of the alkylphenol-aldehyde resins is preferably 350- 10,000, in particular 400 - 5000 g / mol. This preferably corresponds to one Degree of condensation n from 3 to 40, in particular from 4 to 20. Prerequisite here that the resins are oil-soluble.
In einer bevorzugten Ausführungsform der Erfindung handelt es sich bei diesen Alkylphenol-Formaldehydharzen um solche, die Oligo- oder Polymere mit einer repetitiven Struktureinheit der Formel sind, worin RA für C6-C24-Alkyl oder -Alkenyl und n für eine Zahl von 2 bis 50 steht.In a preferred embodiment of the invention, these alkylphenol-formaldehyde resins are those which contain oligomers or polymers with a repetitive structural unit of the formula are where R A is C 6 -C 24 alkyl or alkenyl and n is a number from 2 to 50.
Die Herstellung der Alkylphenol-Aldehyd-Harze erfolgt in bekannter Weise durch basische Katalyse, wobei Kondensationsprodukte vom Resoltyp entstehen, oder durch saure Katalyse, wobei Kondensationsprodukte vom Novolaktyp entstehen.The alkylphenol-aldehyde resins are prepared in a known manner by basic catalysis, whereby condensation products of the resol type arise, or by acidic catalysis, producing condensation products of the novolak type.
Die nach beiden Arten gewonnenen Kondensate sind für die erfindungsgemäßen Zusammensetzungen geeignet. Bevorzugt ist die Kondensation in Gegenwart von sauren Katalysatoren.The condensates obtained in both ways are for the inventive ones Suitable compositions. The condensation in the presence of acidic catalysts.
Zur Herstellung der Alkylphenol-Aldehyd-Harze werden ein Alkylphenol mit 6 - 24, bevorzugt 8 - 22, insbesondere 9 - 18 C-Atomen je Alkylgruppe, oder Gemische hiervon und mindestens ein Aldehyd miteinander umgesetzt, wobei pro mol Alkylphenolverbindung etwa 0,5 - 2 mol, vorzugsweise 0,7- 1,3 mol und insbesondere äquimolare Mengen Aldehyd eingesetzt werden.To prepare the alkylphenol-aldehyde resins, an alkylphenol with 6 - 24, preferably 8-22, in particular 9-18, carbon atoms per alkyl group, or mixtures thereof and at least one aldehyde reacted with one another, with per mol Alkylphenol compound about 0.5-2 moles, preferably 0.7-1.3 mol and in particular equimolar amounts of aldehyde can be used.
Geeignete Alkylphenole sind insbesondere n- und iso-Hexylphenol, n- und isoOctylphenol, n- und iso- Nonylphenol, n- und iso-Decylphenol, n- und iso-Dodecylphenol, Tetradecylphenol, Hexadecylphenol, Octadecylphenol, Eicosylphenol, Tripropenylphenol, Tetrapropenylphenol und Polyi(isobutenyl)phenol bis C24.Suitable alkylphenols are, in particular, n- and iso-hexylphenol, n- and iso-octylphenol, n- and iso-nonylphenol, n- and iso-decylphenol, n- and iso-dodecylphenol, tetradecylphenol, hexadecylphenol, octadecylphenol, eicosylphenol, tripropetraphenylphenol, tripropenylphenol (isobutenyl) phenol to C 24 .
Die Alkylphenole sind vorzugsweise para-substituiert. Die Alkylphenole können einen oder mehrere Alkylreste tragen. Vorzugsweise sind sie zu höchstens 5 mol-%, insbesondere zu höchstens 20 mol-% und speziell höchstens 40 mol-% mit mehr als einer Alkylgruppe substituiert. Bevorzugt tragen höchstens 40 mol-%, insbesondere höchstens 20 mol-% der eingesetzten Alkylphenole in ortho-Position einen Alkylrest. Speziell sind die Alkylphenole in ortho-Position zur Hydroxylgruppe nicht mit tertiären Alkylgruppen substituiert.The alkylphenols are preferably para-substituted. The alkylphenols can be one or carry several alkyl radicals. They are preferably at most 5 mol%, especially at most 20 mol% and especially at most 40 mol% with more than an alkyl group. Preferably carry at most 40 mol%, in particular at most 20 mol% of the alkylphenols used in the ortho position an alkyl radical. Specifically, the alkylphenols ortho to the hydroxyl group are not tertiary Alkyl groups substituted.
Der Aldehyd kann ein Mono- oder Dialdehyd sein und weitere funktionelle Gruppen wie -COOH tragen. Besonders geeignete Aldehyde sind Formaldehyd, Acetaldehyd, Butyraldehyd, Glutardialdehyd und Glyoxalsäure, bevorzugt ist Formaldehyd. Der Formaldehyd kann in Form von Paraformaldehyd oder in Form einer vorzugsweise 20 - 40 gew.-%igen wässrigen Formalinlösung eingesetzt werden. Es können auch entsprechende Mengen an Trioxan verwendet werden.The aldehyde can be a mono- or dialdehyde and other functional groups wear like -COOH. Particularly suitable aldehydes are formaldehyde, acetaldehyde, Butyraldehyde, glutardialdehyde and glyoxalic acid, formaldehyde is preferred. The Formaldehyde can be in the form of paraformaldehyde or in the form of a preferred 20 - 40 wt .-% aqueous formalin solution can be used. It can too appropriate amounts of trioxane can be used.
Die Umsetzung von Alkylphenol und Aldehyd erfolgt üblicherweise in Gegenwart von alkalischen Katalysatoren, beispielsweise Alkalihydroxiden oder Alkylaminen, oder von sauren Katalysatoren, beispielsweise anorganischen oder organischen Säuren, wie Salzsäure, Schwefelsäure, Phosphorsäure, Sulfonsäure, Sulfamidosäuren oder Halogenessigsäuren. Die Kondensation wird bevorzugt lösemittelfrei bei 90 bis 200°C, bevorzugt bei 100 bis 160°C durchgeführt. In einer weiteren bevorzugten Ausführungsform erfolgt die Umsetzung in Gegenwart eines mit Wasser ein Azeotrop bildenden organischen Lösungsmittels, beispielsweise Toluol, Xylol, höheren Aromaten oder Gemischen hiervon. Das Reaktionsgemisch wird auf eine Temperatur von 90 bis 200°C, bevorzugt 100 - 160°C erhitzt, wobei das entstehende Reaktionswasser während der Umsetzung durch azeotrope Destillation entfernt wird. Lösungsmittel, die unter den Bedingungen der Kondensation keine Protonen abspalten, können nach der Kondensationsreaktion in den Produkten bleiben. Die Harze können direkt oder nach Neutralisation des Katalysators eingesetzt werden, gegebenenfalls nach weiterer Verdünnung der Lösung mit aliphatischen und/oder aromatischen Kohlenwasserstoffen oder Kohlenwasserstoffgemischen, z.B. Benzinfraktionen, Kerosin, Decan, Pentadecan, Toluol, Xylol, Ethylbenzol oder Lösungsmitteln wie ® Solvent Naphtha, ® Shellsol AB, ® Solvesso 150, ® Solvesso 200, ® Exxsol, ® ISOPAR- und ® Shellsol D-Typen.The reaction of alkylphenol and aldehyde usually takes place in the presence of alkaline catalysts, for example alkali hydroxides or alkylamines, or of acidic catalysts, for example inorganic or organic acids, such as hydrochloric acid, sulfuric acid, phosphoric acid, sulfonic acid, sulfamido acids or Haloacetic acids. The condensation is preferably solvent-free at 90 to 200 ° C, preferably carried out at 100 to 160 ° C. In another preferred The embodiment is carried out in the presence of a water Azeotropic organic solvent, for example toluene, xylene, higher aromatics or mixtures thereof. The reaction mixture is on a Temperature of 90 to 200 ° C, preferably 100-160 ° C heated, the resulting Water of reaction is removed during the reaction by azeotropic distillation. Solvent that does not have protons under the conditions of condensation split off, can remain in the products after the condensation reaction. The Resins can be used directly or after neutralization of the catalyst, optionally after further dilution of the solution with aliphatic and / or aromatic hydrocarbons or hydrocarbon mixtures, e.g. Gasoline fractions, kerosene, decane, pentadecane, toluene, xylene, ethylbenzene or Solvents such as ® Solvent Naphtha, ® Shellsol AB, ® Solvesso 150, ® Solvesso 200, ® Exxsol, ® ISOPAR and ® Shellsol D types.
Die Gewichtsanteile der Bestandteile A) und B) in den erfindungsgemäßen Additiven können je nach Anwendungsfall in weiten Grenzen variieren. Sie liegen vorzugsweise zwischen 10 und 99,999 Gew.-% A) zu 90 bis 0,001 Gew.-% B), insbesondere zwischen 20 und 99,995 Gew.-% A) zu 80 bis 0,005 Gew.-% B). Dabei werden zur Stabilisierung der Fettsäuren bevorzugt kleinere Anteile der Komponenten B von 0,001 bis 10 Gew.-%, bevorzugt 0,005 bis 5 Gew.-% B) eingesetzt, wogegen zur Optimierung der Schmierfähigkeit größere Anteile B von beispielsweise 5 bis 90 Gew.-%, bevorzugt 10 bis 80 Gew.-% und insbesondere 25 bis 75 Gew.-% eingesetzt werden.The proportions by weight of components A) and B) in the additives according to the invention can vary widely depending on the application. they lay preferably between 10 and 99.999% by weight A) to 90 to 0.001% by weight B), in particular between 20 and 99.995% by weight A) to 80 to 0.005% by weight B). there to stabilize the fatty acids, smaller portions of the Components B from 0.001 to 10% by weight, preferably 0.005 to 5% by weight B) used, whereas to optimize the lubricity larger portions B of for example 5 to 90 wt .-%, preferably 10 to 80 wt .-% and in particular 25 to 75 wt .-% are used.
Überraschenderweise wurde ebenfalls gefunden, dass eine weitere Steigerung der Wirksamkeit als Lubricity-Additiv erzielt wird, wenn die erfindungsgemäßen Mischungen zusammen mit stickstoffhaltigen Paraffindispergatoren eingesetzt werden. Paraffindispergatoren sind Additive, die bei Abkühlung des Öls die Größe der ausfallenden Paraffinkristalle reduzieren und darüber hinaus bewirken, dass die Paraffinpartikel sich nicht absetzen, sondern kolloidal mit deutlich reduziertem Sedimentationsbestreben, dispergiert bleiben.Surprisingly, it was also found that a further increase in Effectiveness as a lubricity additive is achieved if the inventive Mixtures used together with nitrogen-containing paraffin dispersants become. Paraffin dispersants are additives that increase the size when the oil cools reduce the precipitated paraffin crystals and also cause the Paraffin particles do not settle, but colloidally with significantly reduced Sedimentation efforts, remain dispersed.
Bei den stickstoffhaltigen Paraffindispergatoren handelt es sich vorzugsweise um niedermolekulare oder polymere, öllösliche Stickstoffverbindungen, z.B. Aminsalze, Imide und/oder Amide, die durch Reaktion aliphatischer oder aromatischer Amine, vorzugsweise langkettiger aliphatischer Amine, mit aliphatischen oder aromatischen Mono-, Di-, Tri-, Tetra- und/oder Polycarbonsäuren oder deren Anhydriden erhalten werden. Besonders bevorzugte Paraffindispergatoren enthalten Umsetzungsprodukte sekundärer Fettamine mit 8 bis 36 C-Atomen, insbesondere Dicocosfettamin, Ditalgfettamin und Distearylamin. Andere Paraffindispergatoren sind Copolymere des Maleinsäureanhydrids und α,β-ungesättigten Verbindungen, die gegebenenfalls mit primären Monoalkylaminen und/oder aliphatischen Alkoholen umgesetzt werden können, die Umsetzungsprodukte von Alkenylspirobislactonen mit Aminen und Umsetzungsprodukte von Terpolymerisaten auf Basis α,β-ungesättigter Dicarbonsäureanhydride, α,β-ungesättigter Verbindungen und Polyoxyalkylenether niederer ungesättigter Alkohole mit Aminen und/oder Alkoholen. Im folgenden werden einige geeignete Paraffindispergatoren aufgeführt.The nitrogen-containing paraffin dispersants are preferably low molecular weight or polymeric, oil-soluble nitrogen compounds, e.g. Amine salts, Imides and / or amides obtained by reaction of aliphatic or aromatic amines, preferably long-chain aliphatic amines, with aliphatic or aromatic Obtain mono-, di-, tri-, tetra- and / or polycarboxylic acids or their anhydrides become. Contain particularly preferred paraffin dispersants Reaction products of secondary fatty amines with 8 to 36 carbon atoms, in particular Dicocos fatty amine, ditallow fatty amine and distearyl amine. Other paraffin dispersants are copolymers of maleic anhydride and α, β-unsaturated compounds, optionally with primary monoalkylamines and / or aliphatic alcohols can be implemented with the reaction products of alkenylspirobislactones Amines and reaction products of terpolymers based on α, β-unsaturated Dicarboxylic anhydrides, α, β-unsaturated compounds and polyoxyalkylene ethers lower unsaturated alcohols with amines and / or alcohols. Hereinafter some suitable paraffin dispersants are listed.
Die nachfolgend genannten Paraffindispergatoren werden zum Teil durch Reaktion
von Verbindungen, die eine Acylgruppe enthalten, mit einem Amin hergestellt. Bei
diesem Amin handelt es sich um eine Verbindung der Formel NR6R7R8, worin R6, R7
und R8 gleich oder verschieden sein können, und wenigstens eine dieser Gruppen
für C8-C36-Alkyl, C6-C36-Cycloalkyl, C8-C36-Alkenyl, insbesondere C12-C24-Alkyl,
C12-C24-Alkenyl oder Cyclohexyl steht, und die übrigen Gruppen entweder
Wasserstoff, C1-C36-Alkyl, C2-C36-Alkenyl, Cyclohexyl, oder eine Gruppe der Formeln
- (A-O)x-E oder -(CH2)n-NYZ bedeuten, worin A für eine Ethylen- oder
Propylengruppe steht, x eine Zahl von 1 bis 50, E = H, C1-C30-Alkyl, C5-C12-Cycloalkyl
oder C6-C30-Aryl, und n 2, 3 oder 4 bedeuten, und Y und Z unabhängig
voneinander H, C1-C30-Alkyl oder -(A-O)x bedeuten. Unter Acylgruppe wird hier eine
funktionelle Gruppe folgender Formel verstanden:
R10 einen geradkettigen oder verzweigten Alkylenrest mit 2 bis 6 Kohlenstoffatomen oder den Rest der Formel in der R6 und R7 insbesondere Alkylreste mit 10 bis 30, bevorzugt 14 bis 24 C-Atomen bedeuten, wobei die Amidstrukturen auch zum Teil oder vollständig in Form der Ammoniumsalzstruktur der Formel vorliegen können. Die Amide bzw. Amid-Ammoniumsalze bzw. Ammoniumsalze z.B. der Nitrilotriessigsäure, der Ethylendiamintetraessigsäure oder der Propylen-1,2-diamintetraessigsäure werden durch Umsetzung der Säuren mit 0,5 bis 1,5 Mol Amin, bevorzugt 0,8 bis 1,2 Mol Amin pro Carboxylgruppe erhalten. Die Umsetzungstemperaturen betragen etwa 80 bis 200°C, wobei zur Herstellung der Amide eine kontinuierliche Entfernung des entstandenen Reaktionswasser erfolgt. Die Umsetzung muss jedoch nicht vollständig zum Amid geführt werden, vielmehr können 0 bis 100 Mol-% des eingesetzten Amins in Form des Ammoniumsalzes vorliegen. Unter analogen Bedingungen können auch die unter B1) genannten Verbindungen hergestellt werden.Als Amine der Formel kommen insbesondere Dialkylamine in Betracht, in denen R6, R7 einen geradkettigen Alkylrest mit 10 bis 30 Kohlenstoffatomen, vorzugsweise 14 bis 24 Kohlenstoffatomen, bedeutet. Im einzelnen seien Dioleylamin, Dipalmitylamin, Dikokosfettamin und Dibehenylamin und vorzugsweise Ditalgfettamin genannt.
R22 und R23 unabhängig voneinander Wasserstoff oder Methyl,
a, b gleich Null oder Eins und a + b gleich Eins,
R24 und R25 gleich oder verschieden sind und für die Gruppen -NHR6, N(R6)2 und/oder -OR27 stehen, und R27 für ein Kation der Formel H2N(R6)2 oder
H3NR6 steht, 19 - 80 Mol-%, bevorzugt 39-60 Mol-% an bivalenten
Struktureinheiten der Formel 4 worin
R28 Wasserstoff oder C1-C4-Alkyl und
R29 C6-C60-Alkyl oder C6-C18-Aryl bedeuten und
1 - 30 Mol-%, bevorzugt 1 - 20 Mol-% an bivalenten Struktureinheiten der Formel 5 worin
R30 Wasserstoff oder Methyl,
R31 Wasserstoff oder C1-C4-Alkyl,
R33 C1-C4-Alkylen,
m eine Zahl von 1 bis 100,
R32 C1-C24-Alkyl, C5-C20-Cycloalkyl, C6-C18-Aryl oder -C(O)-R34, wobei
R34 C1-C40-Alkyl, C5-C10-Cycloalkyl oder C6-C18-Aryl, enthalten. Die vorgenannten Alkyl-, Cycloalkyl- und Arylreste können gegebenenfalls substituiert sein. Geeignete Substituenten der Alkyl- und Arylreste sind beispielsweise (C1-C6)-Alkyl, Halogene, wie Fluor, Chlor, Brom und Jod, bevorzugt Chlor und (C1-C6)-Alkoxy. Alkyl steht hier für einen geradkettigen oder verzweigten Kohlenwasserstoffrest. Im einzelnen seien genannt: n-Butyl, tert.-Butyl, n-Hexyl, n-Octyl, Decyl, Dodecyl, Tetradecyl, Hexadecyl, Octadecyl, Dodecenyl, Tetrapropenyl, Tetradecenyl, Pentapropenyl, Hexadecenyl, Octadecenyl und Eicosanyl oder Mischungen, wie Cocosalkyl, Talgfettalkyl und Behenyl.Cycloalkyl steht hier für einen cyclischen aliphatischen Rest mit 5 - 20 Kohlenstoffatomen. Bevorzugte Cycloalkylreste sind Cyclopentyl und Cyclohexyl.Aryl steht hier für einen gegebenenfalls substituiertes aromatisches Ringsystem mit 6 bis 18 Kohlenstoffatomen.Die Terpolymere bestehen aus den bivalenten Struktureinheiten der Formeln 1 und 3 sowie 4 und 5 und ggf. 2. Sie enthalten lediglich noch in an sich bekannter Weise die bei der Polymerisation durch Initiierung, Inhibierung und Kettenabbruch entstandenen Endgruppen.Im einzelnen leiten sich Struktureinheiten der Formeln 1 bis 3 von α,β-ungesättigten Dicarbonsäureanhydriden der Formeln 6 und 7 wie Maleinsäureanhydrid, Itaconsäureanhydrid, Citraconsäureanhydrid, bevorzugt Maleinsäureanhydrid, ab.Die Struktureinheiten der Formel 4 leiten sich von den α,β-ungesättigten Verbindungen der Formel 8 ab. Beispielhaft seien die folgenden α,β-ungesättigten Olefine genannt: Styrol, α-Methylstyrol, Dimethylstyrol, α-Ethylstyrol, Diethylstyrol, i-Propylstyrol, tert.-Butylstyrol, Diisobutylen und α-Olefine, wie Decen, Dodecen, Tetradecen, Pentadecen, Hexadecen, Octadecen, C20-α-Olefin, C24-α-Olefin, C30-α-Olefin, Tripropenyl, Tetrapropenyl, Pentapropenyl sowie deren Mischungen. Bevorzugt sind α-Olefine mit 10 bis 24 C-Atomen und Styrol, besonders bevorzugt sind α-Olefine mit 12 bis 20 C-Atomen.Die Struktureinheiten der Formel 5 leiten sich von Polyoxyalkylenethern niederer, ungesättigter Alkohole der Formel 9 ab. Bei den Monomeren der Formel 9 handelt es sich um Veretherungsprodukte (R32 = -C(O)R34) oder Veresterungsprodukte (R32 = -C(O)R34) von Polyoxyalkylenethern (R32 = H).Die Polyoxyalkylenether (R32 = H) lassen sich nach bekannten Verfahren z.B. durch Anlagerung von α-Olefinoxiden, wie Ethylenoxid, Propylenoxid und/oder Butylenoxid an polymerisierbare niedere, ungesättigte Alkohole der Formel 10 und anschließende Veresterung oder Veretherung herstellen. Solche polymerisierbaren niederen ungesättigten Alkohole sind z.B. Allylalkohol, Methallylalkohol, Butenole, wie 3-Buten-1-ol und 1-Buten-3-ol oder Methylbutenole, wie 2-Methyl-3-buten-1-ol, 2-Methyl-3-buten-2-ol und 3-Methyl-3-buten-1-ol. Bevorzugt sind Anlagerungsprodukte von Ethylenoxid und/oder Propylenoxid an Allylalkohol.Als zur Herstellung der Terpolymere geeignete primäre Amine seien beispielsweise die folgenden genannt:
R22 und R23 unabhängig voneinander Wasserstoff oder Methyl,
a, b gleich Null oder 1 und a + b gleich 1,
R37 = -OH, -O-[C1-C30-Alkyl], -NR6R7, OsNrR6R7H2
R38 = R37oderNR6R39
R39 = -(A-O)x-E
mit
A = Ethylen- oder Propylengruppe
x = 1 bis 50
E = H, C1-C30-Alkyl, C5-C12-Cycloalkyl oder C6-C30-Aryl bedeuten, und 80 - 20 Mol-%, bevorzugt 60 - 40 Mol-% an bivalenten Struktureinheiten der Formel 4 enthalten. Im einzelnen leiten sich die Struktureinheiten der Formeln 13, 14 und 15 von α,β-ungesättigten Dicarbonsäureanhydriden der Formeln 6 und/oder 7 ab.Die Struktureinheiten der Formel 4 leiten sich von den α,β-ungesättigten Olefinen der Formel 8 ab. Die vorgenannte Alkyl-, Cycloalkyl- und Arylreste haben die gleichen Bedeutungen wie unter 8.Die Reste R37 und R38 in Formel 13 bzw. R39 in Formel 15 leiten sich von Polyetheraminen oder Alkanolaminen der Formeln 16 a) und b), Aminen der Formel NR6R7R8 sowie gegebenenfalls von Alkoholen mit 1 bis 30 Kohlenstoffatomen ab. Darin bedeuten
- R53
- Wasserstoff, C6-C40-Alkyl oder
- R54
- Wasserstoff, C1-C4-Alkyl
- R55
- Wasserstoff, C1- bis C4-Alkyl, C5- bis C12-Cycloalkyl oder C6- bis C30-Aryl
- R56, R57
- unabhängig voneinander Wasserstoff, C1- bis C22-Alkyl, C2- bis C22-Alkenyl oder Z - OH
- Z
- C2- bis C4-Alkylen
- n
- eine Zahl zwischen 1 und 1000.
R 10 is a straight-chain or branched alkylene radical having 2 to 6 carbon atoms or the radical of the formula in which R 6 and R 7 are in particular alkyl radicals having 10 to 30, preferably 14 to 24, carbon atoms, the amide structures also partially or completely in the form of the ammonium salt structure of the formula can be present. The amides or amide ammonium salts or ammonium salts, for example of nitrilotriacetic acid, ethylenediaminetetraacetic acid or propylene-1,2-diamine tetraacetic acid, are reacted with 0.5 to 1.5 mol of amine, preferably 0.8 to 1.2 mol, by reacting the acids Amine obtained per carboxyl group. The reaction temperatures are about 80 to 200 ° C, with the amides being continuously removed from the water of reaction formed. However, the reaction does not have to be carried out completely to give the amide; on the contrary, 0 to 100 mol% of the amine used can be in the form of the ammonium salt. The compounds mentioned under B1) can also be prepared under analogous conditions. As amines of the formula Dialkylamines are particularly suitable in which R 6 , R 7 is a straight-chain alkyl radical having 10 to 30 carbon atoms, preferably 14 to 24 carbon atoms. Dioleylamine, dipalmitylamine, dicoconut fatty amine and dibehenylamine and preferably ditallow fatty amine may be mentioned in particular.
R 22 and R 23 independently of one another are hydrogen or methyl,
a, b is zero or one and a + b is one,
R 24 and R 25 are the same or different and stand for the groups -NHR 6 , N (R 6 ) 2 and / or -OR 27 , and R 27 for a cation of the formula H 2 N (R 6 ) 2 or
H 3 NR 6 is 19-80 mol%, preferably 39-60 mol% of bivalent
Structural units of formula 4 wherein
R 28 is hydrogen or C 1 -C 4 alkyl and
R 29 is C 6 -C 60 alkyl or C 6 -C 18 aryl and
1 to 30 mol%, preferably 1 to 20 mol% of bivalent structural units of the formula 5 wherein
R 30 is hydrogen or methyl,
R 31 is hydrogen or C 1 -C 4 alkyl,
R 33 C 1 -C 4 alkylene,
m is a number from 1 to 100,
R 32 is C 1 -C 24 alkyl, C 5 -C 20 cycloalkyl, C 6 -C 18 aryl or -C (O) -R 34 , where
R 34 contains C 1 -C 40 alkyl, C 5 -C 10 cycloalkyl or C 6 -C 18 aryl. The aforementioned alkyl, cycloalkyl and aryl radicals can optionally be substituted. Suitable substituents of the alkyl and aryl radicals are, for example, (C 1 -C 6 ) alkyl, halogens such as fluorine, chlorine, bromine and iodine, preferably chlorine and (C 1 -C 6 ) alkoxy. Alkyl here stands for a straight-chain or branched hydrocarbon residue. The following may be mentioned in detail: n-butyl, tert.-butyl, n-hexyl, n-octyl, decyl, dodecyl, tetradecyl, hexadecyl, octadecyl, dodecenyl, tetrapropenyl, tetradecenyl, pentapropenyl, hexadecenyl, octadecenyl and eicosanyl or mixtures, such as coconut alkyll , Tallow fatty alkyl and behenyl. Cycloalkyl here stands for a cyclic aliphatic radical with 5-20 carbon atoms. Preferred cycloalkyl radicals are cyclopentyl and cyclohexyl. Aryl here stands for an optionally substituted aromatic ring system with 6 to 18 carbon atoms. The terpolymers consist of the bivalent structural units of the formulas 1 and 3 as well as 4 and 5 and optionally 2. They only contain in themselves The end groups formed during the polymerization by initiation, inhibition and chain termination are known. In particular, structural units of the formulas 1 to 3 are derived from α, β-unsaturated dicarboxylic acid anhydrides of the formulas 6 and 7 such as maleic anhydride, itaconic anhydride, citraconic anhydride, preferably maleic anhydride. The structural units of the formula 4 are derived from the α, β-unsaturated compounds of the formula 8. The following α, β-unsaturated olefins may be mentioned by way of example: styrene, α-methylstyrene, dimethylstyrene, α-ethylstyrene, diethylstyrene, i-propylstyrene, tert-butylstyrene, diisobutylene and α-olefins, such as decene, dodecene, tetradecene, pentadecene, Hexadecene, octadecene, C 20 -α-olefin, C 24 -α-olefin, C 30 -α-olefin, tripropenyl, tetrapropenyl, pentapropenyl and mixtures thereof. Preferred are α-olefins with 10 to 24 C atoms and styrene, particularly preferred are α-olefins with 12 to 20 C atoms. The structural units of the formula 5 are derived from polyoxyalkylene ethers of lower, unsaturated alcohols of the formula 9. The monomers of the formula 9 are etherification products (R 32 = -C (O) R 34 ) or esterification products (R 32 = -C (O) R 34 ) of polyoxyalkylene ethers (R 32 = H). The polyoxyalkylene ethers (R 32 = H) can be prepared using known processes, for example by adding α-olefin oxides, such as ethylene oxide, propylene oxide and / or butylene oxide, to polymerizable lower, unsaturated alcohols of the formula 10 and subsequent esterification or etherification. Such polymerizable lower unsaturated alcohols are, for example, allyl alcohol, methallyl alcohol, butenols, such as 3-buten-1-ol and 1-buten-3-ol, or methylbutenols, such as 2-methyl-3-buten-1-ol, 2-methyl-3 -buten-2-ol and 3-methyl-3-buten-1-ol. Addition products of ethylene oxide and / or propylene oxide onto allyl alcohol are preferred. Examples of primary amines suitable for the preparation of the terpolymers are:
R 22 and R 23 independently of one another are hydrogen or methyl,
a, b is zero or 1 and a + b is 1,
R 37 = -OH, -O- [C 1 -C 30 alkyl], -NR 6 R 7 , O s N r R 6 R 7 H 2
R 38 = R 37 or NR 6 R 39
R 39 = - (AO) x -E
With
A = ethylene or propylene group
x = 1 to 50
E = H, C 1 -C 30 alkyl, C 5 -C 12 cycloalkyl or C 6 -C 30 aryl, and 80-20 mol%, preferably 60-40 mol%, of bivalent structural units of the formula 4 contain. In particular, the structural units of the formulas 13, 14 and 15 are derived from α, β-unsaturated dicarboxylic anhydrides of the formulas 6 and / or 7. The structural units of the formula 4 are derived from the α, β-unsaturated olefins of the formula 8. The abovementioned alkyl, cycloalkyl and aryl radicals have the same meanings as under 8. The radicals R 37 and R 38 in formula 13 and R 39 in formula 15 are derived from polyether amines or alkanolamines of the formulas 16 a) and b), amines of the formula NR 6 R 7 R 8 and optionally from alcohols having 1 to 30 carbon atoms. Mean in it
- R 53
- Hydrogen, C 6 -C 40 alkyl or
- R 54
- Hydrogen, C 1 -C 4 alkyl
- R 55
- Hydrogen, C 1 to C 4 alkyl, C 5 to C 12 cycloalkyl or C 6 to C 30 aryl
- R 56 , R 57
- independently of one another hydrogen, C 1 - to C 22 -alkyl, C 2 - to C 22 -alkenyl or Z - OH
- Z
- C 2 to C 4 alkylene
- n
- a number between 1 and 1000.
Die polaren stickstoffhaltigen Paraffindispergatoren können den erfindungsgemäßen Additiven beigemischt oder separat dem zu additivierenden Mitteldestillat zugesetzt werden. Das Mengenverhältnis zwischen Paraffindispergatoren und den erfindungsgemäßen Additiven liegt zwischen 5:1 und 1:5 und bevorzugt zwischen 3:1 und 1:3.The polar nitrogen-containing paraffin dispersants can be the inventive Additives are added or added separately to the middle distillate to be added become. The quantitative ratio between paraffin dispersants and Additives according to the invention are between 5: 1 and 1: 5 and preferably between 3: 1 and 1: 3.
Zur Herstellung von Additivpaketen für spezielle Problemlösungen können die erfindungsgemäßen Additive auch zusammen mit einem oder mehreren öllöslichen Co-Additiven eingesetzt werden, die für sich allein die Schmierwirkung und/oder die Kaltfließeigenschaften von Rohölen, Schmierölen oder Brennstoffölen verbessern. Beispiele solcher Co-Additive sind Vinylacetat enthaltende Copolymerisate oder Terpolymerisate des Ethylens, Kammpolymere sowie öllösliche Amphiphile.For the production of additive packages for special problem solutions the additives according to the invention also together with one or more oil-soluble Co-additives are used, which alone have the lubricating effect and / or Improve the cold flow properties of crude oils, lubricating oils or fuel oils. Examples of such co-additives are copolymers containing vinyl acetate or Terpolymers of ethylene, comb polymers and oil-soluble amphiphiles.
So haben sich Mischungen der erfindungsgemäßen Additive mit Copolymerisaten hervorragend bewährt, die 10 bis 40 Gew.-% Vinylacetat und 60 bis 90 Gew.-% Ethylen enthalten. Nach einer weiteren Ausgestaltung der Erfindung setzt man die erfindungsgemäßen Additive in Mischung mit Ethylen/Vinylacetat/Vinyl-2-ethylhexanoat-Terpolymeren, Ethylen/Vinylacetat/ Neononansäurevinylester-Terpolymeren und/oder Ethylen-Vinylacetat/ Neodecansäurevinylester-Terpolymeren zur gleichzeitigen Verbesserung der Fließfähigkeit und Schmierwirkung von Mineralölen oder Mineralöldestillaten ein. Die Terpolymerisate der 2-Ethylhexansäurevinylester, Neononansäurevinylester bzw. der Neodecansäurevinylester enthalten außer Ethylen 10 bis 35 Gew.-% Vinylacetat und 1 bis 25 Gew.-% des jeweiligen langkettigen Vinylesters. Weitere bevorzugte Copolymere enthalten neben Ethylen und 10 bis 35 Gew.-% Vinylestern noch 0,5 bis 20 Gew.-% Olefin mit 3 bis 10 C-Atomen wie z. B. Isobutylen, Diisobutylen, 4-Methylpenten oder Norbornen.So have mixtures of the additives according to the invention with copolymers excellent proven, the 10 to 40 wt .-% vinyl acetate and 60 to 90 wt .-% Contain ethylene. According to a further embodiment of the invention, the additives according to the invention in a mixture with ethylene / vinyl acetate / vinyl 2-ethylhexanoate terpolymers, Ethylene / vinyl acetate / neononanoic acid vinyl ester terpolymers and / or ethylene vinyl acetate / vinyl neodecanoate terpolymers to improve the flowability and lubrication of Mineral oils or mineral oil distillates. The terpolymers of vinyl 2-ethylhexanoate, Vinyl neononanoate or In addition to ethylene, neodecanoic acid vinyl esters contain 10 to 35% by weight of vinyl acetate and 1 to 25 wt .-% of the respective long-chain vinyl ester. More preferred In addition to ethylene and 10 to 35% by weight of vinyl esters, copolymers also contain 0.5 to 20 wt .-% olefin with 3 to 10 carbon atoms such. B. isobutylene, diisobutylene, 4-methylpentene or norbornene.
Schließlich werden in einer weiteren Ausführungsform der Erfindung die erfindungsgemäßen Additive zusammen mit Kammpolymeren verwendet. Hierunter versteht man Polymere, bei denen Kohlenwasserstoffreste mit mindestens 8, insbesondere mindestens 10 Kohlenstoffatomen an einem Polymerrückgrat gebunden sind. Vorzugsweise handelt es sich um Homopolymere, deren Alkylseitenketten mindestens 8 und insbesondere mindestens 10 Kohlenstoffatome enthalten. Bei Copolymeren weisen mindestens 20 %, bevorzugt mindestens 30 % der Monomeren Seitenketten auf (vgl. Comb-like Polymers-Structure and Properties; N.A. Platé and V.P. Shibaev, J. Polym. Sci. Macromolecular Revs. 1974, 8, 117 ff). Beispiele für geeignete Kammpolymere sind z.B. Fumarat/Vinylacetat-Copolymere (vgl. EP 0 153 176 A1), Copolymere aus einem C6-C24-α-Olefin und einem N-C6-C22-Alkylmaleinsäureimid (vgl. EP 0 320 766), ferner veresterte Olefin/Maleinsäureanhydrid-Copolymere, Polymere und Copolymere von α-Olefinen und veresterte Copolymere von Styrol und Maleinsäureanhydrid.Finally, in a further embodiment of the invention, the additives according to the invention are used together with comb polymers. This is understood to mean polymers in which hydrocarbon radicals having at least 8, in particular at least 10, carbon atoms are bonded to a polymer backbone. They are preferably homopolymers whose alkyl side chains contain at least 8 and in particular at least 10 carbon atoms. In the case of copolymers, at least 20%, preferably at least 30%, of the monomers have side chains (cf. Comb-like Polymers-Structure and Properties; NA Platé and VP Shibaev, J. Polym. Sci. Macromolecular Revs. 1974, 8, 117 ff). Examples of suitable comb polymers are, for example, fumarate / vinyl acetate copolymers (cf. EP 0 153 176 A1), copolymers of a C 6 -C 24 α-olefin and an NC 6 -C 22 alkylmaleimide (cf. EP 0 320 766) , further esterified olefin / maleic anhydride copolymers, polymers and copolymers of α-olefins and esterified copolymers of styrene and maleic anhydride.
Kammpolymere können beispielsweise durch die Formel beschrieben werden. Darin bedeuten
- A
- R', COOR', OCOR', R"-COOR' oder OR';
- D
- H, CH3, A oder R;
- E
- H oder A;
- G
- H, R", R"-COOR', einen Arylrest oder einen heterocyclischen Rest;
- M
- H, COOR", OCOR", OR" oder COOH;
- N
- H, R", COOR", OCOR, COOH oder einen Arylrest;
- R'
- eine Kohlenwasserstoffkette mit 8-150 Kohlenstoffatomen;
- R"
- eine Kohlenwasserstoffkette mit 1 bis 10 Kohlenstoffatomen;
- m
- eine Zahl zwischen 0,4 und 1,0; und
- n
- eine Zahl zwischen 0 und 0,6.
- A
- R ', COOR', OCOR ', R "-COOR' or OR ';
- D
- H, CH 3 , A or R;
- e
- H or A;
- G
- H, R ", R" -COOR ', an aryl radical or a heterocyclic radical;
- M
- H, COOR ", OCOR", OR "or COOH;
- N
- H, R ", COOR", OCOR, COOH or an aryl radical;
- R '
- a hydrocarbon chain with 8-150 carbon atoms;
- R "
- a hydrocarbon chain of 1 to 10 carbon atoms;
- m
- a number between 0.4 and 1.0; and
- n
- a number between 0 and 0.6.
Das Mischungsverhältnis (in Gewichtsteilen) der erfindungsgemäßen Additive mit Ethylencopolymeren bzw. Kammpolymeren beträgt jeweils 1:10 bis 20:1, vorzugsweise 1:1 bis 10:1.The mixing ratio (in parts by weight) of the additives according to the invention Ethylene copolymers or comb polymers are each 1:10 to 20: 1, preferably 1: 1 to 10: 1.
Die erfindungsgemäßen Additive werden ölen in Mengen von 0,0001 bis 1 Gew.-%, bevorzugt 0,001 bis 0,1 Gew.-% und speziell 0,002 bis 0,05 Gew.-% zugesetzt. Dabei können sie als solche oder auch gelöst in Lösemitteln, wie z.B. aliphatischen und/oder aromatischen Kohlenwasserstoffen oder Kohlenwasserstoffgemischen wie z.B. Toluol, Xylol, Ethylbenzol, Decan, Pentadecan, Benzinfraktionen, Diesel, Kerosin oder kommerziellen Lösemittelgemischen wie Solvent Naphtha, ® Shellsol AB, ® Solvesso 150, ® Solvesso 200, ® Exxsol-, ® Isopar- und ® Shellsol D-Typen, sowie polaren Lösungsmitteln wie Alkoholen, Glykolen und Estern wie beispielsweise Fettsäurealkylestern und insbesondere Rapsölsäuremethylester (RME), eingesetzt werden. Bevorzugt enthalten die erfindungsgemäßen Additive bis zu 70 %, speziell 5 - 60 %, insbesondere 10 - 40 Gew.-% Lösemittel.The additives of the invention are oiled in amounts from 0.0001 to 1% by weight, preferably 0.001 to 0.1% by weight and especially 0.002 to 0.05% by weight added. They can be used as such or dissolved in solvents such as e.g. aliphatic and / or aromatic hydrocarbons or Hydrocarbon mixtures such as Toluene, xylene, ethylbenzene, decane, Pentadecane, gasoline fractions, diesel, kerosene or commercial Solvent mixtures such as Solvent Naphtha, ® Shellsol AB, ® Solvesso 150, ® Solvesso 200, ® Exxsol, ® Isopar and ® Shellsol D types, as well as polar solvents such as Alcohols, glycols and esters such as fatty acid alkyl esters and in particular rapeseed oleic acid methyl ester (RME). Prefers contain the additives according to the invention up to 70%, especially 5-60%, in particular 10 - 40 wt .-% solvent.
Die erfindungsgemäßen Additive können bei erhöhter Temperatur über längere Zeit ohne Alterungseffekte gelagert werden, ohne dass es zu Alterungserscheinungen wie Verharzung und der Bildung unlöslicher Strukturen oder Ablagerungen in Lagerbehältern und/oder Motorteilen kommt. Darüber hinaus verbessern sie die Oxidationsstabilität der additivierten Öle bei gleichzeitig verminderter Emulgierneigung. Dies ist insbesondere bei Ölen, die größere Anteile an Ölen aus Crack-Prozessen enthalten, von Vorteil.The additives according to the invention can be used at elevated temperature for a long time stored without aging effects, without causing signs of aging such as resinification and the formation of insoluble structures or deposits in Storage containers and / or engine parts comes. They also improve the Oxidation stability of the additive oils with reduced at the same time Emulsify. This is especially true with oils that are made up of larger proportions of oils Crack processes included, beneficial.
Des weiteren zeigen sie eine den Einzelkomponenten überlegene Verbesserung der Lubricity von Mitteldestillaten. Damit kann die für die Einstellung der Spezifikation erforderliche Dosierrate abgesenkt werden.Furthermore, they show an improvement in the superiority of the individual components Lubricity of middle distillates. This can be used for setting the specification required dosage rate can be reduced.
Ein weiterer Vorteil der erfindungsgemäßen Additive ist ihre gegenüber den gemäß dem Stand der Technik als Lubricity-Additive eingesetzten Fettsäureestern abgesenkte Kristallisationstemperatur. So können sie auch bei niedrigen Temperaturen von beispielsweise 0°C bis -20°C und teilweise auch niedriger problemlos eingesetzt werden.Another advantage of the additives according to the invention is that of the additives according to state of the art fatty acid esters used as lubricity additives reduced crystallization temperature. So you can even at low Temperatures of, for example, 0 ° C to -20 ° C and sometimes also lower can be used without any problems.
Die erfindungsgemäßen Additive sind für die Verwendung in Mitteldestillaten besonders gut geeignet. Als Mitteldestillate bezeichnet man insbesondere solche Mineralöle, die durch Destillation von Rohöl gewonnen werden und im Bereich von 120 bis 450°C sieden, beispielsweise Kerosin, Jet-Fuel, Diesel und Heizöl. Die Öle können auch Alkohole wie Methanol und/oder Ethanol enthalten oder aus diesen bestehen. Vorzugsweise werden die erfindungsgemäßen Additive in solchen Mitteldestillaten verwendet, die weniger als 350 ppm Schwefel, insbesondere weniger als 200 ppm Schwefel und in speziellen Fällen weniger als 50 ppm bzw. weniger als 10 ppm Schwefel enthalten. Es handelt sich dabei im allgemeinen um solche Mitteldestillate, die einer hydrierenden Raffination unterworfen wurden, und die daher nur geringe Anteile an polyaromatischen und polaren Verbindungen enthalten, die ihnen eine natürliche Schmierwirkung verleihen. Die erfindungsgemäßen Additive werden weiterhin vorzugsweise in solchen Mitteldestillaten verwendet, die 95 %-Destillationspunkte unter 370°C, insbesondere 350°C und in Spezialfällen unter 330°C aufweisen. Des gleichen sind die erfindungsgemäßen Additive für die Verwendung in synthetischen Kraftstoffen mit ebenfalls geringer Schmierfähigkeit, wie sie z. B. im Fischer-Tropsch-erozeß hergestellt werden können, geeignet. Die in ihrer Schmierfähigkeit verbesserten Öle besitzen einen im HFRR-Test gemessenen Wear Scar Diameter von bevorzugt weniger als 460 µm, speziell weniger als 450 µm. Die erfindungsgemäßen Additive können auch als Komponenten in Schmierölen eingesetzt werden.The additives of the invention are for use in middle distillates particularly suitable. Middle distillates are especially those Mineral oils obtained from crude oil distillation and in the range of Boil 120 to 450 ° C, for example kerosene, jet fuel, diesel and heating oil. The oils may also contain or from alcohols such as methanol and / or ethanol consist. The additives according to the invention are preferably used in such Middle distillates used that contain less than 350 ppm sulfur, in particular less than 200 ppm sulfur and in special cases less than 50 ppm or contain less than 10 ppm sulfur. It is generally about those middle distillates which have been subjected to hydrogenating refining, and which therefore only contains small amounts of polyaromatic and polar compounds contain, which give them a natural lubricating effect. The Additives according to the invention are also preferably used in such Middle distillates used, the 95% distillation points below 370 ° C, in particular 350 ° C and in special cases below 330 ° C. They are the same additives according to the invention for use in synthetic fuels also low lubricity, as z. B. in Fischer-Tropsch erosion can be produced, suitable. The oils with improved lubricity have a wear scar diameter of preferred measured in the HFRR test less than 460 µm, especially less than 450 µm. The additives according to the invention can also be used as components in lubricating oils.
Die Mischungen können allein oder auch zusammen mit anderen Additiven verwendet werden, z.B. mit Stockpunkterniedrigern, Korrosionsinhibitoren, Antioxidantien, Schlamminhibitoren, Dehazern, Leitfähigkeitsverbesserern, Lubricity-Additiven, und Zusätzen zur Erniedrigung des Cloud-Points. Des weiteren werden sie erfolgreich zusammen mit Additivpaketen eingesetzt, die u.a. bekannte aschefreie Dispergieradditive, Detergenzien, Entschäumer, Antioxidantien, Dehazer, Demulgatoren und Korrosionsinhibitoren enthalten.The mixtures can be used alone or together with other additives be used, e.g. with pour point depressants, corrosion inhibitors, Antioxidants, sludge inhibitors, dehazers, conductivity improvers, lubricity additives, and additives to lower the cloud point. Be further successfully used together with additive packages that include known ashless dispersion additives, detergents, defoamers, antioxidants, dehazers, Demulsifiers and corrosion inhibitors included.
Die Vorteile der erfindungsgemäßen Additive werden durch die nachfolgenden Beispiele näher erläutert.The advantages of the additives according to the invention are shown by the following Examples explained in more detail.
Im folgenden werden die eingesetzten Additive charakterisiert. Die OH-Zahlen wurden gemäß DIN 53240 durch Umsetzung mit einer definierten Menge überschüssigem Acetanhydrid und anschließende Titration der gebildeten Essigsäure bestimmt.The additives used are characterized below. The OH numbers were in accordance with DIN 53240 by implementation with a defined amount excess acetic anhydride and subsequent titration of the formed Acetic acid determined.
Jodzahlen werden nach Kaufmann bestimmt. Dazu wird die Probe mit einer
definierten Menge einer methanolischen Bromlösung versetzt, wobei sich eine dem
Gehalt an Doppelbindungen equivalente Menge Brom anlagert. Der Überschuss an
Brom wird mit Natriumthiosulfat zurücktitriert.
In einen 500 ml Erlenmeyerkolben werden 10 g des zu überprüfenden
Additiv(gemisch)s eingewogen. Der Kolben wird drei Tage bei einer Temperatur von
90 °C im Trockenschrank gelagert, wobei täglich die über dem Additiv stehende
Atmosphäre durch Überleiten eines Luftstroms ausgetauscht wird.
Nach der Konditionierung lässt man die Mischung eine Stunde bei Raumtemperatur
abkühlen. Anschließend wird mit 500 ml Dieselkraftstoff (Testöl 3) versetzt und gut
durchmischt. Nach zwei Stunden Standzeit wird die Mischung visuell auf eventuelle
Ausscheidungen, Trübungen, unlösliche Anteile u.s.w. beurteilt, die Hinweise auf
oxidative Veränderungen geben (visuelle Beurteilung). Sodann wird über ein
0,8 µm Filter bei einer Druckdifferenz von 800 mbar filtriert. Die Gesamtmenge muss
innerhalb von 2 Minuten filtrierbar sein, ansonsten wird das nach 2 Minuten filtrierte
Volumen notiert.
After conditioning, the mixture is allowed to cool for one hour at room temperature. Then 500 ml of diesel fuel (test oil 3) is added and mixed well. After standing for two hours, the mixture is visually assessed for possible excretions, cloudiness, insoluble components, etc., which give indications of oxidative changes (visual assessment). Then it is filtered through a 0.8 µm filter at a pressure difference of 800 mbar. The total amount must be filterable within 2 minutes, otherwise the volume filtered after 2 minutes is noted.
Eine Mischung aus 9 g A 7, 1 g B1 und 2 g C2 ergab nach dreitägiger Lagerung bei 90°C und anschließender Verdünnung mit 500 ml Testöl 3 eine klare Lösung und eine Filtrationszeit von 65 s.A mixture of 9 g A 7, 1 g B1 and 2 g C2 gave after three days of storage 90 ° C and then diluted with 500 ml test oil 3 a clear solution and a filtration time of 65 s.
Verschiedene Ester wurden jeweils 5 Tage bei 15°C, +5°C und -5°C gelagert und nach 3 bzw. 5 Tagen visuell auf Fließfähigkeit und evtl. Ausscheidungen bzw. Trübungen beurteilt. Die Bewertungen haben folgende Bedeutung:
- +
- fließfähig und klar
- O
- fließfähig aber trüb bzw. mit Ausscheidungen
- ―
- fest
- +
- flowable and clear
- O
- flowable but cloudy or with excretions
- -
- firmly
Die Schmierwirkung der Additive wurde mittels eines HFRR-Geräts der Firma PCS
Instruments an additivierten Ölen bei 60°C geprüft. Der High Frequency
Reciprocating Rig Test (HFRR) ist beschrieben in D. Wei, H. Spikes, Wear, Vol. 111,
No. 2, p. 217, 1986. Die Ergebnisse sind als Reibungskoeffizient und Wear Scar
(WS 1.4) angegeben. Ein niedriger Wear Scar und ein niedriger Reibungskoeffizient
(Friction) zeigen eine gute Schmierwirkung. Wear Scar-Werte von weniger als 460
µm werden als Indiz für eine ausreichende Schmierwirkung angesehen, wobei in der
Praxis jedoch Werte von weniger als 400 µm angestrebt werden. Die Dosierraten in
Tabelle 6 beziehen sich auf die Menge an dosiertem Wirkstoff.
Reciprocating Rig Test (HFRR) is described in D. Wei, H. Spikes, Wear, Vol. 111, No. 2, p. 217, 1986. The results are given as the coefficient of friction and wear scar (WS 1.4). A low wear scar and a low coefficient of friction (friction) show a good lubricating effect. Wear scar values of less than 460 µm are regarded as an indication of a sufficient lubricating effect, although in practice values of less than 400 µm are aimed for. The dosing rates in Table 6 relate to the amount of active ingredient dosed.
Claims (13)
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
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DE10230771 | 2002-07-09 | ||
DE10230771 | 2002-07-09 | ||
DE10252973 | 2002-11-14 | ||
DE2002152973 DE10252973A1 (en) | 2002-11-14 | 2002-11-14 | Lubricity additive for low-sulfur fuel oils, e.g. diesel fuel, comprises a polyol fatty acid partial ester and an alkylphenol resin |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1380634A1 true EP1380634A1 (en) | 2004-01-14 |
EP1380634B1 EP1380634B1 (en) | 2007-08-15 |
Family
ID=29737617
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP03013093A Revoked EP1380634B1 (en) | 2002-07-09 | 2003-06-11 | Lubricity additives stabilised against oxidation for highly desulphurised fuel oils. |
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Country | Link |
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US (2) | US20040010965A1 (en) |
EP (1) | EP1380634B1 (en) |
JP (1) | JP4484458B2 (en) |
AT (1) | ATE370214T1 (en) |
CA (1) | CA2431749C (en) |
DE (1) | DE50307929D1 (en) |
ES (1) | ES2291562T3 (en) |
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US20060046941A1 (en) * | 2004-08-26 | 2006-03-02 | Laurent Chambard | Lubricating oil compositions |
EP1997870A1 (en) | 2004-08-26 | 2008-12-03 | Infineum International Limited | Lubricating oil compositions |
DE102005035277B4 (en) * | 2005-07-28 | 2007-10-11 | Clariant Produkte (Deutschland) Gmbh | Mineral oils with improved conductivity and cold flowability |
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Also Published As
Publication number | Publication date |
---|---|
US7815696B2 (en) | 2010-10-19 |
JP4484458B2 (en) | 2010-06-16 |
DE50307929D1 (en) | 2007-09-27 |
ATE370214T1 (en) | 2007-09-15 |
CA2431749A1 (en) | 2004-01-09 |
JP2004043801A (en) | 2004-02-12 |
US20040010965A1 (en) | 2004-01-22 |
CA2431749C (en) | 2010-12-14 |
EP1380634B1 (en) | 2007-08-15 |
US20060162241A1 (en) | 2006-07-27 |
ES2291562T3 (en) | 2008-03-01 |
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