EP2162513B1 - Huiles minérales contenant des additifs détergents dotées d'une fluidité à froid améliorée - Google Patents

Huiles minérales contenant des additifs détergents dotées d'une fluidité à froid améliorée Download PDF

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EP2162513B1
EP2162513B1 EP08759257.2A EP08759257A EP2162513B1 EP 2162513 B1 EP2162513 B1 EP 2162513B1 EP 08759257 A EP08759257 A EP 08759257A EP 2162513 B1 EP2162513 B1 EP 2162513B1
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alkyl
oil
carbon atoms
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use according
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EP2162513A1 (fr
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Matthias Krull
Robert Janssen
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Clariant International Ltd
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Clariant International Ltd
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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
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/146—Macromolecular compounds according to different macromolecular groups, mixtures thereof
    • 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
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/18—Organic compounds containing oxygen
    • C10L1/192—Macromolecular compounds
    • 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
    • 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
    • C10L10/14—Use of additives to fuels or fires for particular purposes for improving low temperature properties
    • 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
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/16—Hydrocarbons
    • C10L1/1625—Hydrocarbons macromolecular compounds
    • C10L1/1633—Hydrocarbons macromolecular compounds homo- or copolymers obtained by reactions only involving carbon-to carbon unsaturated bonds
    • C10L1/1641—Hydrocarbons macromolecular compounds homo- or copolymers obtained by reactions only involving carbon-to carbon unsaturated bonds from compounds containing aliphatic monomers
    • 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
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/18—Organic compounds containing oxygen
    • 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
    • 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
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/22—Organic compounds containing nitrogen
    • C10L1/222—Organic compounds containing nitrogen containing at least one carbon-to-nitrogen single bond
    • C10L1/2222—(cyclo)aliphatic amines; polyamines (no macromolecular substituent 30C); quaternair ammonium compounds; carbamates
    • 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
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/22—Organic compounds containing nitrogen
    • C10L1/222—Organic compounds containing nitrogen containing at least one carbon-to-nitrogen single bond
    • C10L1/224—Amides; Imides carboxylic acid amides, imides
    • 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
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/22—Organic compounds containing nitrogen
    • C10L1/234—Macromolecular compounds
    • C10L1/238—Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds
    • C10L1/2383—Polyamines or polyimines, or derivatives thereof (poly)amines and imines; derivatives thereof (substituted by a macromolecular group containing 30C)

Definitions

  • the present invention relates to the use of nucleating agents to improve the cold flowability of mineral oil distillates containing detergent additives, as well as the mineral oil distillates additive.
  • paraffin-rich crude oils are extracted and processed, which consequently also lead to paraffin-rich fuel oils.
  • the paraffins contained in particular in middle distillates can crystallize on lowering the temperature of the oil and partially agglomerate with the inclusion of oil. This crystallization and agglomeration can cause blockages of the filters in engines and firing systems, especially in winter, which prevents safe metering of the fuels and may possibly lead to a complete interruption of the fuel supply.
  • the paraffin problem is also exacerbated by the environmental reasons to reduce the sulfur content increasing hydrodesulfurization of fuel oils, which leads to an increased proportion of cold-critical paraffins in the fuel oil.
  • middle distillates are often added chemical additives, so-called cold flow improvers or flow improvers, modify the crystal structure and Agglomerationsne noticed the precipitated paraffins, so that the so-additive oils still pump or use at temperatures, often more than 20 ° C. lower than non-additized oils.
  • cold flow improver oil-soluble copolymers of ethylene and unsaturated esters, oil-soluble polar nitrogen compounds and / or comb polymers are usually used. In addition, however, other additions have been proposed.
  • detergent additives are being developed with ever increasing effectiveness. In addition, they are often used in very high dosage rates. It is reported that this reduces, for example, in diesel fuels, the specific consumption and the performance of the engines is increased.
  • these additives often have negative effects on the cold flowability of middle distillates and in particular on the efficacy of known cold flow improvers. Especially with middle distillates with low boiling point and simultaneously low aromatic content, it is often difficult or even impossible to adjust in the presence of modern detergent additives using conventional flow improvers a satisfactory cold flow behavior. For example, the addition of detergent additives often results in an antagonistic effect on the effectiveness of the added cold flow improvers.
  • the paraffin dispersion of the middle distillate, set by paraffin dispersants is impaired, without being able to be reconstituted by increased metering of paraffin dispersant.
  • the CFPP measured filterability with cold flow improvers additive oils is significantly reduced in the cold and can be compensated only by greatly increased dosage of the flow improver.
  • detergent additives which are derived from higher polyamines and those which are, for example, conditional have very high molecular weights by multiple alkylation and / or acylation of these polyamines.
  • those detergent additives whose hydrophobic residue is derived from sterically hindered olefins and / or higher molecular weight and / or polyfunctionalized poly (olefins).
  • WO-03/042337 teaches middle distillates with a maximum of 0.05% by weight of sulfur containing fatty acid esters of alkoxylated polyols having at least 3 OH groups (A) and at least one cold flow improver (B), said cold flow improver comprising at least one copolymer of ethylene and one or more ethylenically unsaturated carboxylic acid esters having an ethylene content of 60 to 90 mol%.
  • the invention thus relates to the use of at least one oil-soluble, acting as Nucleator for paraffin crystallization compound B) selected from comb polymers carrying alkyl side chains with a length of at least 20 carbon atoms, to improve the response to the lowering of Pour Point and CFPP Value as well as the improvement of the paraffin dispersion of mineral oil flow improvers C) other than B) in middle distillates containing at least one ashless nitrogen-containing detergent additive A) which is an oil-soluble, amphiphilic compound comprising at least one alkyl or alkenyl radical, which is bonded to a polar group, wherein the alkyl or alkenyl radical 10 to 500 carbon atoms and the polar group comprises 2 or more nitrogen atoms, wherein the ashless nitrogen-containing detergent additive A) comprises a polar moiety derived from polyamines of the formula (R 9 ) 2 N- [AN (R 9 )] q - (R 9 ) wherein each R 9 independently of one another represents hydrogen, an al
  • the improvement in the response of cold flow improvers C) according to the invention is understood to improve at least one cold property of middle distillates adjusted or adjustable by cold flow improver C) and adversely affected by the addition of a detergent additive A) by addition of a compound B) acting as a nucleating agent for the paraffin crystallization , Specifically, by adding the nucleating agent B), the cold property set or adjustable without the presence of the detergent additive A) by the cold flow improver C) is achieved.
  • Cold properties are understood here individually or in combination as the pour point, the cold filter plugging point, the low-temperature flow, and the paraffin dispersion of middle distillates.
  • Particularly affected is the response of flow improvers in middle distillates containing more than 10 ppm of a nitrogen-containing detergent additive A), especially more than 20 ppm and especially more than 40 ppm such as 50 to 2000 ppm of nitrogen-containing detergent additive A).
  • the additives contain, based on one part by weight of the nitrogen-containing detergent additive A) from 0.01 to 10 parts by weight, and in particular from 0.05 to 5 parts by weight, for example from 0.1 to 3 parts by weight of the oil-soluble compound B) acting as nucleator for the paraffin crystallization.
  • Ashless means that the additives in question essentially consist only of elements which form gaseous reaction products during combustion.
  • the additives consist essentially only of the elements carbon, hydrogen, oxygen and nitrogen.
  • ashless additives are substantially free of metals and metal salts.
  • Nucleators are understood to be compounds which initiate the crystallization of paraffins on cooling a paraffin-containing oil. They thus shift the beginning of the paraffin crystallization of the oil additized with them, which can be determined, for example, by measuring the cloud point or the Wax Appearance Temperature (WAT), to higher temperatures. These are compounds that are soluble in the oil above the cloud point and begin to crystallize just above the temperature of the paraffin saturation and then serve as seed for the crystallization of the paraffins. Thus, they prevent over-saturation of the oil with paraffins and lead to crystallization near the saturation concentration. This leads to the formation of a multiplicity of equally small paraffin crystals.
  • WAT Wax Appearance Temperature
  • paraffin crystallization thus begins at a higher temperature than in non-additized oil. This can be determined, for example, by measuring the WAT by means of differential scanning calorimetry (DSC) with a slow cooling of the oil at, for example, -2 K / min.
  • DSC differential scanning calorimetry
  • the alkyl or alkenyl group imparts oil-solubility to the detergent additives.
  • alkyl radical has 15 to 500 carbon atoms and in particular 20 to 350 carbon atoms, for example 50 to 200 carbon atoms.
  • This alkyl radical can be linear or branched, in particular it is branched.
  • the alkyl radical is derived from oligomers of lower olefins having 3 to 6 C atoms such as propene, butene, pentene or hexene and mixtures thereof.
  • Preferred isomers of these olefins are isobutene, 2-butene, 1-butene, 2-methyl-2-butene, 2,3-dimethyl-2-butene, 1-pentene, 2-pentene and iso-pentene and mixtures thereof.
  • Particular preference is given to propene, isobutene, 2-butene, 2-methyl-2-butene, 2,3-dimethyl-2-butene and mixtures thereof.
  • olefin mixtures which are more than 70 mol%, especially more than 80 mol%, for example more than 90 mol% or contain more than 95 mol% of 2-methyl-2-butene, 2,3-dimethyl-2-butene and / or isobutene.
  • Particularly suitable for the preparation of such detergent additives are highly reactive low molecular weight polyolefins having a proportion of terminal double bonds of at least 75%, especially at least 85% and in particular at least 90% such as at least 95%.
  • Particularly preferred low molecular weight polyolefins are poly (isobutylene), poly (2-butene), poly (2-methyl-2-butene), poly (2,3-dimethyl-2-butene), poly (ethylene-co-isobutylene) and atactic poly (propylene).
  • the molecular weight of particularly preferred polyolefins is between 500 and 3000 g / mol.
  • Such oligomers of lower olefins are accessible for example by polymerization by means of Lewis acids such as BF 3 and AlCl 3 , by means of Ziegler catalysts and in particular by means of metallocene catalysts.
  • the polar component of the detergent additives which are particularly problematic for the response of known cold additives is derived from polyamines having 2 to 20 N atoms.
  • polyamines correspond to the formula (R 9 ) 2 N- [AN (R 9 )] q - (R 9 ) wherein each R 9 is independently hydrogen, an alkyl or hydroxyalkyl radical of up to 24 carbon atoms, a polyoxyalkylene radical - (AO) r - or polyiminoalkylene radical - [AN (R 9 )] s - (R 9 ) but wherein at least one R 9 is hydrogen, q is an integer from 1 to 19, A is an alkylene radical having 1 to 6 C atoms, r and s independently of one another are from 1 to 50.
  • polyamines usually these are mixtures of polyamines and in particular mixtures of poly (ethylene amines) and / or poly (propyleneamines).
  • DETA dimethylaminopropylamine
  • TETA triethylenetetramine
  • TEPA tetraethylenepentamine
  • PEHA pentaethylenehexamine
  • PEHA pentapropylenehexamine
  • heavy polyamines ethylenediamine, 1,2-propylenediamine, dimethylaminopropylamine, diethylenetriamine (DETA), dipropy
  • Heavy polyamines are generally understood as meaning mixtures of polyalkylenepolyamines which, in addition to small amounts of TEPA and PEHA, are mainly oligomers having 7 or more nitrogen atoms, of which two or more in the form of primary amino groups. These polyamines often also contain branched structural elements via tertiary amino groups.
  • Suitable amines include those which comprise cyclic structural units derived from piperazine.
  • the piperazine units may preferably carry hydrogen at one or both nitrogen atoms, an alkyl or hydroxyalkyl radical having up to 24 carbon atoms or a polyiminoalkylene radical - [AN (R 9 )] s - (R 9 ), where A, R 9 and s have the meanings given above.
  • Suitable amines include alicyclic diamines such as 1,4-di (aminomethyl) cyclohexane and heterocyclic nitrogen compounds such as imidazolines and N-aminoalkylpiperazines such as N- (2-aminoethyl) piperazine.
  • detergent additives whose polar portion is derived from hydroxyl-bearing polyamines, heterocycle-substituted polyamines, and aromatic polyamines are problematic. Examples which may be mentioned are: N- (2-hydroxyethyl) ethylenediamine, N, N 1 -bis- (2-hydroxyethyl) ethylene diamine, N- (3-hydroxybutyl) tetra (methylene) diamine, N-2-aminoethylpiperazine, N-2- and N-3-aminopropylmorpholine, N-3- (dimethylamino) propylpiperazine, 2-heptyl-3- (2-aminopropyl) imidazoline, 1,4-bis (2-aminoethyl) piperazine, 1- (2-hydroxyethyl) piperazine, various isomers of phenylenediamine and naphthalenediamine and mixtures of these amines.
  • Detergent additives based on heavy polyamines in which R 9 is hydrogen in the above formula and q has values of at least 3, in particular at least 4, such as 5, 6 or 7, are particularly critical for the cold additization of middle distillates.
  • R 9 is hydrogen in the above formula and q has values of at least 3, in particular at least 4, such as 5, 6 or 7, are particularly critical for the cold additization of middle distillates.
  • a proportion of more than 10 wt .-%, in particular more than 20 wt .-% and especially of more than 50 wt .-% of amines having q-values of 4 or higher and especially with q Values of 5 or higher and especially with q values of 6 or higher on the total amount of amines used proved to be particularly critical.
  • oil-soluble alkyl moiety and the polar head group of the detergent additives may be linked together either directly via a C-N or through an ester, amide or imide bond.
  • preferred detergent additives are alkylpolyamines, Mannich reaction products, hydrocarbyl-substituted succinic acid amides and imides, and mixtures of these classes of substances.
  • the detergent additives linked via C-N bonds are preferably alkylpoly (amines) which are obtainable, for example, by reacting polyisobutylenes with polyamines, for example by hydroformylation and subsequent reductive amination with the abovementioned polyamines.
  • alkylpoly amines
  • one or more alkyl radicals may be bound to the polyamine.
  • Detergent additives based on higher polyamines having more than 4 N atoms, for example those having 5, 6 or 7 N atoms, are particularly critical for the cold addition.
  • Detergent additives containing amide or imide bonds are obtainable, for example, by reaction of alkenylsuccinic anhydrides with polyamines.
  • Alkenylsuccinic anhydride and polyamine are preferably reacted in a molar ratio of about 1: 0.5 to about 1: 1.
  • the preparation of the underlying Alkenylbernsteinklaanhydride is usually carried out by addition of ethylenically unsaturated polyolefins or chlorinated polyolefins to ethylenically unsaturated dicarboxylic acids.
  • alkenyl succinic anhydrides can be prepared by reaction of chlorinated polyolefins with maleic anhydride.
  • the preparation also succeeds by thermal addition of polyolefins to maleic anhydride in an "ene reaction".
  • highly reactive olefins with a high content of, for example, more than 75% and especially more than 85 mol%, based on the total number of polyolefin molecules, of isomers having a terminal double bond are particularly suitable.
  • the molar ratio of the two reactants in the reaction between maleic anhydride and polyolefin can vary within wide limits. Preferably, it may be between 10: 1 and 1: 5, with molar ratios of 6: 1 to 1: 1 being particularly preferred.
  • Maleic anhydride is preferably used in stoichiometric excess, for example 1.1 to 3 moles of maleic anhydride per mole of polyolefin. Excess maleic anhydride can be removed from the reaction by, for example, distillation.
  • the accessible reaction products have, based on the reacted with unsaturated carboxylic acids fractions of the poly (olefins) on average a Malein istsgrad of more than 1, preferably about 1.01 to 2.0 and in particular 1.1 to 1.8 dicarboxylic acid per alkyl radical. Reaction with the abovementioned amines results in products with markedly increased effectiveness as detergent additives. On the other hand, as the degree of maleation increases, so does the impairment of the efficacy of cold flow improvers.
  • alkenyl succinic anhydrides with polyamines leads to products which can carry one or more amide and / or imide bonds per polyamine and depending on the Maleinleitersgrad one or two polyamines per alkyl radical.
  • Alkenylsuccinic anhydride per mole of polyamine is preferably used for the reaction of 1.0 to 1.7 and in particular 1.1 to 1.5, so that free primary amino groups remain in the product.
  • alkenyl succinic anhydride and polyamine are reacted equimolarly.
  • polyamines with Alkenylsuccinic anhydrides with a high degree of acylation of 1.1 or more anhydride groups per alkyl radical such as, for example, 1.3 or more anhydride groups per alkyl radical, also give rise to polymers which are particularly problematic for the response of cold additives.
  • Typical and particularly preferred acylated nitrogen compounds are obtained by reacting poly (isobutylene), poly (2-butenyl), poly (2-methyl-2-butenyl) -, poly (2,3-dimethyl-2-butenyl) - or Poly (propenyl) succinic anhydrides having an average of about 1.2 to 1.5 anhydride groups per alkyl radical whose alkylene radicals carry between 50 and 400 carbon atoms, with a mixture of poly (ethylene amines) having about 3 to 7 nitrogen atoms and about 1 to 6 ethylene units available.
  • Oil-soluble Mannich reaction products based on polyolefin-substituted phenols and polyamines also impair the effectiveness of conventional cold flow improvers.
  • Mannich bases of this kind are prepared by known processes, for example by alkylating phenol and / or salicylic acid with the polyolefins described above, such as, for example, poly (isobutylene), poly (2-butene), poly (2-methyl-2-butene), poly ( 2,3-dimethyl-2-butene) or atactic poly (propylene) and subsequent condensation of the alkylphenol with aldehydes having 1 to 6 carbon atoms such as formaldehyde or its reactive equivalents such as formalin or paraformaldehyde and the above-described polyamines such as TEPA, PEHA or heavy polyamines produced.
  • the polyolefins described above such as, for example, poly (isobutylene), poly (2-butene), poly (2-methyl-2-butene), poly ( 2,3-dimethyl-2-butene) or atactic poly (propylene) and subsequent condensation of the alkylphenol with aldehydes having 1 to 6 carbon atoms such as
  • the average molecular weight determined by means of vapor pressure osmometry is particularly efficient, but at the same time also for the cold additization of middle distillates of particularly critical detergent additives is above 800 g / mol and in particular above 2,000 g / mol such as above 3,000 g / mol.
  • the average molecular weight of the above-described detergent additives can also be increased via crosslinking reagents and adapted to the intended use.
  • Suitable crosslinking reagents are, for example, dialdehydes, such as glutaric dialdehyde, bisepoxides derived, for example, from bisphenol A, Dicarboxylic acids and their reactive derivatives such as maleic anhydride and alkenylsuccinic anhydrides and higher polybasic carboxylic acids and their derivatives such as trimellitic acid, trimellitic anhydride and pyromellitic dianhydride.
  • Preferred comb polymers B) acting as nucleator for the paraffin crystallization are polymers which carry alkyl side chains bonded to the polymer backbone and have a length of at least 20 carbon atoms. Particularly preferred are those polymers which carry side chains having 22 to 60, such as 24 to 45 carbon atoms.
  • the proportion of these alkyl side chains in the total amount of the alkyl side chains of the polymer is at least 10 mol%, preferably at least 25 mol% and in particular at least 50 mol%, for example at least 80 mol%.
  • the side chains are linear or have at least correspondingly long linear segments.
  • the polymer backbone may for example be composed of ethylenically unsaturated mono- and / or polycarboxylic acids such as, for example, acrylic acid, methacrylic acid, fumaric acid, maleic acid, itaconic acid.
  • it may contain other monomers such as olefins, vinyl esters and / or vinyl ethers. Particular preference is given to copolymers based on fumaric acid and vinyl acetate and those based on maleic acid and ⁇ -olefins.
  • the polymer backbone carries long-chain alkyl radicals with a molar average of at least 18, preferably at least 20, such as at least 24 C atoms.
  • the alkyl radicals can be bonded directly to the backbone via a C-C bond or can be bound to the polymer backbone via an ester, amide, imide or ammonium group.
  • the alkyl radicals can be bonded to the polymer backbone via spacers such as, for example, polyoxyalkylene or polyalkyleneamine groups having in each case 1 to 200 and in particular 2 to 50 oxyalkyl or alkylenamine units.
  • nucleator suitable for the paraffin crystallization comb polymers B are, for example, polymers of the formula (1)
  • Preferred comb polymers are, for example, copolymers of ethylenically unsaturated dicarboxylic acids such as maleic or fumaric acid with other ethylenically unsaturated monomers such as olefins or vinyl esters.
  • Particularly preferred olefins are ⁇ -olefins having at least 22 and especially 24 to 60 carbon atoms such as C 20 - ⁇ -olefin, C 24 - ⁇ -olefin, C 26 - ⁇ -olefin and mixtures thereof such as C 20-24 - ⁇ -olefin, C 26-28 - ⁇ -olefin or C24-28- ⁇ -olefin and technical chain cuts in the range C 30+ .
  • ⁇ -olefins linear alkenes with terminal double bond.
  • a particularly preferred comonomer vinyl ester is vinyl acetate.
  • the copolymers of unsaturated carboxylic acids are essentially alternating copolymers.
  • these copolymers of ethylenically unsaturated carboxylic acids are esterified with alcohols to at least 50%, preferably to 60-100% and in particular to 70-98%, for example to 80-95%.
  • Alcohols having at least 20 and preferably having at least 22 carbon atoms are preferably used for this purpose.
  • shorter-chain alcohols having, for example, 10 to 18 and especially 12 to 16 C atoms for the esterification, provided that the polymer already carries a sufficient amount of long side chains with at least 20 C atoms.
  • comb polymers are homopolymers and copolymers of alkyl acrylates, alkyl methacrylates and alkyl vinyl ethers derived from alcohols having at least 20 and especially 22 to 60 carbon atoms, such as 24 to 40 carbon atoms, as well as homo- and copolymers of alkyl vinyl esters derived from Derive fatty acids with at least 20 and especially 22 to 40 carbon atoms.
  • copolymers of dicarboxylic acids such as maleic or fumaric acid and vinyl acetate, which have been esterified with long-chain fatty alcohols having at least 20 carbon atoms, are used as comb polymers.
  • alkylphenol-aldehyde resins which are derived from alkylphenols having one or two alkyl radicals in ortho and / or para position to the OH group.
  • Particularly preferred as starting materials are alkylphenols which carry at least two hydrogen atoms capable of condensation with aldehydes on the aromatic and in particular monoalkylated phenols.
  • the alkyl radical is in the para position to the phenolic OH group.
  • the alkyl radicals can be used in the alkylphenol-aldehyde resins which can be used in the process according to the invention may be the same or different, they may be saturated or preferably unsaturated
  • At least 10 mol%, preferably at least 25 mol% and in particular at least 50 mol%, for example at least 80 mol% of the alkyl radicals of the alkylphenol resins suitable according to the invention as nucleator B) have alkyl chains with at least 20 carbon atoms and preferably between 22 and 60 such as 24 to 45 carbon atoms. On a molar average, the alkyl radicals have at least 18, preferably 20 to 60, such as 24 to 45 carbon atoms. In a preferred embodiment, mixtures of alkylphenols having different alkyl radicals are used for the preparation of the alkylphenol resins. Thus, for example, resins based on mixtures of C 20/22/24 -alkylphenols, C 24/26/28 -alkylphenols and of alkylphenols with chain lengths of C 30 and higher have proven particularly suitable.
  • Suitable alkylphenol resins may also contain or consist of structural units of other phenol analogs such as salicylic acid, hydroxybenzoic acid and derivatives thereof such as esters, amides and salts. That is, the alkyl radicals may be bonded to the phenol directly via a C-C bond or via an ester or ether group.
  • Preferred polycondensates are accessible by reacting alkylphenols with aldehydes and / or ketones.
  • Suitable aldehydes for the alkylphenol-aldehyde resins are those having 1 to 12 carbon atoms and preferably those having 1 to 4 carbon atoms such as formaldehyde, acetaldehyde, propionaldehyde, butyraldehyde, 2-ethylhexanal, benzaldehyde, glyoxalic acid and their reactive equivalents such as paraformaldehyde and trioxane.
  • Particularly preferred is formaldehyde in the form of paraformaldehyde and especially formalin.
  • the polycondensation can also be carried out in the presence of aldehydes and amines in the form of a Mannich reaction.
  • the compounds suitable as nucleator B) are alkylphenol-formaldehyde resins which contain oligomers or polymers having a repeating structural unit of the formula (2) wherein R 11 is C 20 -C 200 -alkyl or -alkenyl, OR 10 or OC (O) -R 10 , R 10 is C 20 -C 200 -alkyl or -alkenyl and n is a number from 5 to 200, contain.
  • R 10 preferably represents C 22 -C 100 -alkyl or -alkenyl and in particular C 24 -C 50 -alkyl or -alkenyl.
  • R 11 particularly preferably represents C 22 -C 100 -alkyl or -alkenyl and in particular C 24 -C 50 -alkyl or -alkenyl.
  • n is a number from 7 to 100 and especially for a number from 10 to 50.
  • alkylphenol-aldehyde resins are accessible by known methods, for. B. by condensation of the corresponding alkylphenols with formaldehyde, ie with 0.5 to 1.5 moles, preferably 0.8 to 1.2 moles of formaldehyde per mole of alkylphenol.
  • the condensation can be carried out solvent-free, but preferably it is carried out in the presence of an inert or only partially water-miscible inert organic solvent such as mineral oils, alcohols, ethers and the like. Particularly preferred are solvents which can form azeotropes with water.
  • solvents in particular aromatics such as toluene, xylene diethylbenzene and higher-boiling commercial solvent mixtures such as Shellsol® AB, and solvent naphtha are used.
  • fatty acids and their derivatives such as esters with lower alcohols having 1 to 5 carbon atoms such as ethanol and especially methanol are suitable as solvents.
  • the condensation is preferably carried out between 70 and 200 ° C such as between 90 and 160 ° C. It is usually catalysed by 0.05 to 5 wt .-% bases or preferably by 0.05 to 5 wt .-% acids.
  • acidic catalysts in addition to carboxylic acids such as acetic acid and oxalic acid in particular strong mineral acids such as hydrochloric acid, phosphoric acid and sulfuric acid and sulfonic acids common catalysts.
  • Particularly suitable catalysts are sulfonic acids which contain at least one sulfonic acid group and at least one saturated or unsaturated, linear, branched and / or cyclic hydrocarbon radical having 1 to 40 C atoms and preferably having 3 to 24 C atoms.
  • aromatic sulfonic acids especially alkylaromatic mono-sulfonic acids having one or more C 1 -C 28 -alkyl radicals and in particular those having C 3 -C 22 -alkyl radicals.
  • Suitable examples are methanesulfonic acid, butanesulfonic acid, benzenesulfonic acid, p-toluenesulfonic acid, xylenesulfonic acid, 2-mesitylenesulfonic acid, 4-ethylbenzenesulfonic acid, isopropylbenzenesulfonic acid, 4-butylbenzenesulfonic acid, 4-octylbenzenesulfonic acid; Dodecylbenzenesulfonic acid, didodecylbenzenesulfonic acid, naphthalenesulfonic acid. Mixtures of these sulfonic acids are suitable.
  • the molecular weight of the comb polymers B) preferred as nucleators for paraffin crystallization by gel permeation chromatography against poly (styrene) standards in THF is preferably 1,000-100,000 g / mol, particularly preferably 2,000-50,000 g / mol and especially 2,500-25,000 g / mol for example 3,000-20,000 g / mol.
  • the prerequisite here is that the comb polymers, at least in application-relevant concentrations of 0.001 to 1 wt .-% are oil-soluble.
  • the quantitative ratio between detergent additive A) and nucleators B) in the additized oil can vary within wide limits. It has proven particularly useful to use from 0.01 to 10 parts by weight, in particular from 0.05 to 5 parts by weight, for example from 0.1 to 3 parts by weight of nucleator per part by weight of detergent additive, in each case based on the active ingredient.
  • Preferred cold flow improvers as constituent III are copolymers of ethylene and olefinically unsaturated compounds.
  • Suitable ethylene copolymers are, in particular, those which contain, in addition to ethylene, from 8 to 21 mol%, in particular from 10 to 18 mol%, of olefinically unsaturated comonomer compounds.
  • the olefinically unsaturated compounds are preferably vinyl esters, acrylic esters, methacrylic esters, alkyl vinyl ethers and / or alkenes, it being possible for the abovementioned compounds to be substituted by hydroxyl groups.
  • One or more comonomers may be included in the polymer.
  • said alkyl groups may be substituted with one or more hydroxyl groups.
  • R 1 is a branched alkyl radical or a neoalkyl radical having 7 to 11 carbon atoms, in particular having 8, 9 or 10 carbon atoms.
  • Particularly preferred vinyl esters are derived from secondary and especially tertiary carboxylic acids whose branching is in the alpha position to the carbonyl group.
  • Suitable vinyl esters include vinyl acetate, vinyl propionate, vinyl butyrate, vinyl isobutyrate, vinyl hexanoate, vinyl heptanoate, vinyl octanoate, vinyl pivalate, Vinyl 2-ethylhexanoate, vinyl laurate, vinyl stearate and versatic acid esters, such as vinyl neononanoate, vinyl neodecanoate, vinyl neoundecanoate.
  • these ethylene copolymers contain vinyl acetate and at least one further vinyl ester of the formula 1 in which R 1 is C 4 to C 30 -alkyl, preferably C 4 to C 16 -alkyl, especially C 6 - to C 12 -alkyl ,
  • Suitable acrylic esters include, for.
  • said alkyl groups may be substituted with one or more hydroxyl groups.
  • An example of such an acrylic ester is hydroxyethyl methacrylate.
  • the alkenes are preferably simple unsaturated hydrocarbons having 3 to 30 carbon atoms, especially 4 to 16 carbon atoms and especially 5 to 12 carbon atoms.
  • Suitable alkenes include propene, butene, isobutylene, pentene, hexene, 4-methylpentene, octene, diisobutylene and norbornene and its derivatives such as methylnorbornene and vinylnorbornene.
  • said alkyl groups may be substituted with one or more hydroxyl groups.
  • terpolymers which, apart from ethylene, have from 3.5 to 20 mol%, in particular from 8 to 15 mol% of vinyl acetate and from 0.1 to 12 mol%, in particular from 0.2 to 5 mol%, of at least one longer-chain and preferably branched one Vinyl esters such as vinyl 2-ethylhexanoate, vinyl neononanoate or vinyl neodecanoate, wherein the total comonomer content of the terpolymers is preferably between 8 and 21 mol%, in particular between 12 and 18 mol%.
  • copolymers contain, in addition to ethylene and 8 to 18 mol% of vinyl esters of C 2 to C 12 carboxylic acids, from 0.5 to 10 mol% of olefins such as propene, butene, isobutylene, hexene, 4-methylpentene, octene, diisobutylene and / or norbornene.
  • olefins such as propene, butene, isobutylene, hexene, 4-methylpentene, octene, diisobutylene and / or norbornene.
  • these ethylene-co- and terpolymers have melt viscosities at 140 ° C of 20 to 10,000 m ⁇ Pas, in particular from 30 to 5,000 m ⁇ Pas, especially from 50 to 2,000 m ⁇ Pas.
  • the means of 1 H-NMR spectroscopy, certain degrees of branching are preferably between 1 and 9 CH 3/100 CH 2 groups, especially between 2 and 6 CH 3/100 CH 2 groups, which do not stem from the comonomers.
  • the polymers underlying the mixtures differ in at least one characteristic.
  • they may contain different comonomers, have different comonomer contents, molecular weights and / or degrees of branching.
  • the mixing ratio between the additives and ethylene copolymers as constituent III can vary within wide limits depending on the application, with the ethylene copolymers III often representing the greater proportion.
  • Such additive and oil mixtures preferably contain 0.1 to 25, preferably 0.5 to 10 parts by weight of ethylene copolymers per part by weight of the additive combination according to the invention.
  • cold flow improvers which are suitable are oil-soluble polar nitrogen compounds (constituent IV). These are preferably reaction products of fatty amines with compounds containing an acyl group.
  • the preferred amines are compounds of the formula NR 6 R 7 R 8 , in which R 6 , R 7 and R 8 may be identical or different, and at least one of these groups is C 8 -C 36 -alkyl, C 6 - C 36 -cycloalkyl, C 8 -C 36 -alkenyl, in particular C 12 -C 24 -alkyl, C 12 -C 24 -alkenyl or cyclohexyl, and the other groups are either hydrogen, C 1 -C 36 -alkyl, C 2 -C 36 alkenyl, cyclohexyl, or a group of the formulas - (AO) x -E or - (CH 2 ) n -NYZ, where A is an ethyl or propyl group,
  • polyamines of the formula - [N- (CH 2 ) n ] m -NR 6 R 7 , in which m is a number between 1 and 20 and n, R 6 and R 7 have the meanings given above, are suitable as fatty amines .
  • the alkyl and alkenyl radicals can be linear or branched and contain up to two double bonds. They are preferably linear and substantially saturated, ie they have iodine numbers of less than 75 gl 2 / g, preferably less than 60 gl 2 / g and in particular between 1 and 10 gl 2 / g.
  • secondary fatty amines in which two of the groups R 6 , R 7 and R 8 are C 8 -C 36 -alkyl, C 6 -C 36 -cycloalkyl, C 8 -C 36 -alkenyl, in particular C 12 -C 24 alkyl, C 12 -C 24 alkenyl or cyclohexyl.
  • Suitable fatty amines are, for example, octylamine, decylamine, dodecylamine, tetradecylamine, hexadecylamine, octadecylamine, eicosylamine, behenylamine, didecylamine, didodecylamine, ditetradecylamine, dihexadecylamine, dioctadecylamine, dieicosylamine, dibehenylamine and mixtures thereof.
  • the amines contain chain cuts based on natural raw materials such as eg coco fatty amine, tallow fatty amine, hydrogenated tallow fatty amine, dicocosfettamine, ditallow fatty amine and di (hydrogenated tallow fatty amine).
  • Particularly preferred amine derivatives are amine salts, imides and / or amides such as, for example, amide ammonium salts of secondary fatty amines, in particular dicocosfettamine, ditallow fatty amine and distearylamine.
  • Suitable carbonyl compounds for the reaction with amines are both monomeric and polymeric compounds having one or more carboxyl groups. In the case of the monomeric carbonyl compounds, preference is given to those having 2, 3 or 4 carbonyl groups. They can also contain heteroatoms such as oxygen, sulfur and nitrogen.
  • carboxylic acids examples include maleic, fumaric, crotonic, itaconic, succinic, C 1 -C 40 -alkenylsuccinic, adipic, glutaric, sebacic, and malonic acids and benzoic, phthalic, trimellitic and pyromellitic acid, nitrilotriacetic acid , Ethylenediaminetetraacetic acid and their reactive derivatives such as esters, anhydrides and acid halides.
  • Copolymers of ethylenically unsaturated acids such as, for example, acrylic acid, methacrylic acid, maleic acid, fumaric acid and itaconic acid, have proven particularly suitable as polymeric carbonyl compounds, particular preference is given to copolymers of maleic anhydride.
  • Suitable comonomers are those which impart oil solubility to the copolymer. Oil-soluble means here that the copolymer dissolves without residue in the middle distillate to be additive after reaction with the fatty amine in practice-relevant metering rates.
  • Suitable comonomers are, for example, olefins, alkyl esters of acrylic acid and methacrylic acid, alkyl vinyl esters and alkyl vinyl ethers having 2 to 75, preferably 4 to 40 and in particular 8 to 20 carbon atoms in the alkyl radical.
  • the carbon number refers to the alkyl radical attached to the double bond.
  • the molecular weights of the polymeric carbonyl compounds are preferred between 400 and 20,000, more preferably between 500 and 10,000, such as between 1,000 and 5,000.
  • Oil-soluble polar nitrogen compounds which have been obtained by reaction of aliphatic or aromatic amines, preferably long-chain aliphatic amines, with aliphatic or aromatic mono-, di-, tri- or tetracarboxylic acids or their anhydrides have proven particularly suitable (cf. US 4 211 534 ).
  • amides and ammonium salts of aminoalkylene polycarboxylic acids such as nitrilotriacetic acid or ethylenediaminetetraacetic acid with secondary amines are suitable as oil-soluble polar nitrogen compounds (cf. EP 0 398 101 ).
  • oil-soluble polar nitrogen compounds are copolymers of maleic anhydride with ⁇ , ⁇ -unsaturated compounds, which can optionally be reacted with primary monoalkylamines and / or aliphatic alcohols (cf. EP-A-0 154 177 . EP-0 777 712 ), the reaction products of Alkenylspirobislactonen with amines (see. EP-A-0 413 279 B1) and after EP-A-0 606 055 A2 Reaction products of terpolymers based on ⁇ , ⁇ -unsaturated dicarboxylic acid anhydrides, ⁇ , ⁇ -unsaturated compounds and polyoxyalkylene ethers of lower unsaturated alcohols.
  • the mixing ratio between the inventive ethylene copolymers III and oil-soluble polar nitrogen compounds as constituent IV may vary depending on the application.
  • Such additive mixtures preferably contain 0.1 to 10 parts by weight, preferably 0.2 to 5 parts by weight, based on the active compounds, of at least one oil-soluble polar nitrogen compound per part by weight of the additive combination according to the invention.
  • the mixing ratio between the additives and the further components V and VI is generally in each case between 1:10 and 10: 1, preferably between 1: 5 and 5: 1.
  • Additives contain 15-80% by weight, preferably 20-70% by weight of detergent additive A), 2-40% by weight, preferably 5-25% by weight of nucleator B) and 15-80% by weight, preferably 20-70% by weight of cold flow improver C).
  • the additives are preferably used as concentrates which contain from 10 to 95% by weight and preferably from 20 to 80% by weight, for example from 25 to 60% by weight, of solvent.
  • Preferred solvents are higher-boiling aliphatic, aromatic hydrocarbons, alcohols, esters, ethers and mixtures thereof.
  • Such concentrates preferably contain from 0.01 to 10 parts by weight, preferably from 0.05 to 5 parts by weight, for example from 0.1 to 3 parts by weight of the comb polymer B) per part by weight of detergent additive A).
  • the Nucleatoren B improve the response of detergent additive-containing middle distillates such as kerosene, jet fuel, diesel and fuel oil for conventional flow improvers with regard to the lowering of pour point and CFPP value and the improvement of paraffin dispersion.
  • Particularly preferred mineral oil distillates are middle distillates.
  • the middle distillate is in particular those mineral oils which are obtained by distillation of crude oil, boiling in the range of about 150 to 450 ° C and in particular in the range of about 170 to 390 ° C, for example kerosene, jet fuel, diesel and fuel oil.
  • middle distillates contain about 5 to 50 wt .-%, such as about 10 to 35 wt .-% n-paraffins, of which the longer-chain crystallize on cooling and can affect the flowability of the middle distillate.
  • Particularly advantageous are the compositions of the invention in middle aromatics with low aromatic content of less than 21 wt .-%, such as less than 19 wt .-%.
  • compositions according to the invention are furthermore particularly advantageous in low boiling end middle distillates, ie in middle distillates which have 90% distillation points below 360 ° C., in particular 350 ° C. and in special cases below 340 ° C. and furthermore in such middle distillates, the boiling ranges have between 20 and 90% distillation volume of less than 120 ° C and in particular of less than 110 ° C.
  • aromatic compounds is meant the sum of mono-, di- and polycyclic aromatic compounds as determinable by HPLC according to DIN EN 12916 (2001 edition).
  • the middle distillates can also minor amounts such as, for example, up to 40% by volume, preferably 1 to 20% by volume, especially 2 to 15 such as 3 to 10% by volume of the oils of animal and / or vegetable origin described in more detail below, such as, for example, fatty acid methyl esters ,
  • compositions according to the invention are also suitable for improving the cold properties of detergent additives containing fuels based on renewable raw materials (biofuels).
  • biofuels oils obtained from animal and preferably vegetable material or both, and derivatives thereof, which can be used as fuel and especially as diesel or fuel oil.
  • biofuels oils obtained from animal and preferably vegetable material or both, and derivatives thereof, which can be used as fuel and especially as diesel or fuel oil.
  • biofuels examples include rapeseed oil, coriander oil, soybean oil, cottonseed oil, sunflower oil, castor oil, olive oil, peanut oil, corn oil, almond oil, palm kernel oil, coconut oil, mustard seed oil, beef tallow, bone oil, fish oils and used edible oils.
  • Other examples include oils derived from wheat, jute, sesame, shea nut, arachis oil and linseed oil.
  • the fatty acid alkyl esters, also referred to as biodiesel can be derived from these oils by methods known in the art.
  • Rapeseed oil which is a mixture of glycerol esterified fatty acids, is preferred because it is available in large quantities and is readily available by squeezing rapeseed.
  • sunflower, palm and soybeans and their mixtures with rapeseed oil are preferred.
  • Particularly suitable as biofuels are lower alkyl esters of fatty acids.
  • commercially available mixtures of the ethyl, propyl, butyl and especially methyl esters of fatty acids having 14 to 22 carbon atoms for example of lauric acid, myristic acid, palmitic acid, palmitoleic acid, stearic acid, oleic acid, elaidic acid, petroselinic acid, ricinoleic acid, Elaeostearic, linoleic, linolenic, eicosanoic, gadoleic, docosanoic or erucic acid into consideration.
  • Preferred esters have an iodine value of from 50 to 150 and in particular from 90 to 125.
  • Mixtures with particularly advantageous properties are those which contain mainly, ie at least 50% by weight of methyl esters of fatty acids having 16 to 22 carbon atoms and 1, 2 or 3 double bonds contain.
  • the preferred lower alkyl esters of fatty acids are the methyl esters of oleic, linoleic, linolenic and erucic acids.
  • the additives can be used alone or together with other additives, for.
  • pour point depressants or dewaxing aids with other detergents, with antioxidants, cetane number improvers, dehazers, demulsifiers, dispersants, defoamers, dyes, corrosion inhibitors, lubricity additives, sludge inhibitors, odorants and / or cloud point depressants.
  • detergent additives (A) with different nucleators (B) and further flow improvers (C) with the characteristics given below were used.
  • paraffin dispersion in middle distillates is determined in the short sediment test as follows: 150 ml of the middle distillates mixed with the additive components indicated in the table were cooled to -13 ° C. in a cold cabinet at -2 ° C./hour in 200 ml graduated cylinders and stored at this temperature for 16 hours. Subsequently, the volume and appearance of both the sedimented paraffin phase and the oil phase above are visually determined and assessed. A small amount of sediment and a cloudy oil phase show a good paraffin dispersion.
  • test oil 1 The determination of the CFPP values in test oil 1 was carried out after adding the oil with 200 ppm C2 and 150 ppm C3.
  • detergent additive A1 the reaction product of poly (isobutenyl) -succinic anhydride and pentaethylene-hexamine according to Table 2
  • detergent additive A2 the reaction product of poly (isobutenyl) succinic anhydride and pentaethylenehexamine according to Table 2, Example 13 used.
  • Table 2 Effect of nucleators on detergent-induced antagonism in test oil 1 example Detergent additive (DA) Dosing rate DA / ppm CFPP in test oil 1 [° C] polyolefin Mw polyolefin polyamine mol of ASA / mol of polyamine without DA with DA with DA + Nucleator (B) 1 PIB 700 TEPA 1.0 150 -29 -25 50 ppm B1 -30 2 PIB 700 TEPA 1.4 150 -29 -26 50 ppm B1 -29 3 PIB 1000 PEHA 1.0 150 -29 -22 75 ppm B2 -28 4 PIB 1000 PEHA 1.5 150 -29 -21 75 ppm B2 -27 5 PIB 1000 PAM 1.0 150 -29 -18 60 ppm B1 -28 6 PIB 1000 PAM 1.3 150 -29 -15 60 ppm B1 -25 7 PIB 1000 PAM 1.3 150 -29 -15 75 ppm B1

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Claims (19)

  1. Utilisation d'au moins un composé B) soluble dans les huiles, agissant en tant qu'agent de nucléation pour la cristallisation de paraffines, choisi parmi les polymères en peigne, qui portent des chaînes latérales alkyle d'une longueur d'au moins 20 atomes C, pour améliorer la réponse au regard de la réduction du point d'écoulement et de la valeur CFPP, ainsi que pour améliorer la dispersion des paraffines d'agents d'amélioration de l'écoulement à froid d'huiles minérales C), qui sont différents de B), dans des distillats moyens, qui contiennent au moins un additif détergent azoté sans cendres A), qui est un composé amphiphile soluble dans les huiles, qui comprend au moins un radical alkyle ou alcényle, qui est relié à un groupe polaire, le radical alkyle ou alcényle comprenant 10 à 500 atomes C et le groupe polaire comprenant 2 atomes d'azote ou plus, l'additif détergent azoté sans cendres A) comprenant une fraction polaire, qui est dérivée de polyamines de formule

            (R9)2N-[A-N(R9)]q-(R9)

    dans laquelle les R9 représentent chacun indépendamment les uns des autres l'hydrogène, un radical alkyle ou hydroxyalkyle contenant jusqu'à 24 atomes C, un radical polyoxyalkylène -(A-O)r- ou un radical polyiminoalkylène -[A-N(R9)]s-(R9), au moins un R9 représentant toutefois l'hydrogène, q représente un nombre entier de 1 à 19, A représente un radical alkylène de 1 à 6 atomes C, et r et s représentent indépendamment l'un de l'autre des nombres entiers de 1 à 50, et des composés azotés polaires solubles dans les huiles étant utilisés en tant qu'agents d'amélioration de l'écoulement à froid C), qui sont des produits de réaction de composés de formule NR6R7R8, dans laquelle R6, R7 et R8 peuvent être identiques ou différents, et au moins un de ces groupes représente alkyle en C8-C36, cycloalkyle en C6-C36, alcényle en C8-C36, notamment alkyle en C12-C24, alcényle en C12-C24 ou cyclohexyle, et les autres groupes signifient soit hydrogène, alkyle en C1-C36, alcényle en C2-C36, cyclohexyle, soit un groupe de formule -(A-O)x-E ou-(CH2)n-NYZ, A représentant un groupe éthyle ou propyle, x signifiant un nombre de 1 à 50, E = H, alkyle en C1-C30, cycloalkyle en C5-C12 ou aryle en C6-C30, et n = 2, 3 ou 4, et Y et Z signifiant indépendamment l'un de l'autre H, alkyle en C1-C30 ou -(A-O)x, avec des composés qui contiennent au moins un groupe acyle.
  2. Utilisation selon la revendication 1, dans laquelle, par rapport à une partie en poids de l'additif détergent azoté A), 0,01 à 10 parties en poids du composé B) soluble dans les huiles, agissant en tant qu'agent de nucléation pour la cristallisation de paraffines, sont utilisées.
  3. Utilisation selon la revendication 1 et/ou 2, dans laquelle le distillat moyen contient 10 à 10 000 ppm d'un additif détergent azoté sans cendres A).
  4. Utilisation selon une ou plusieurs des revendications 1 à 3, dans laquelle l'additif détergent azoté sans cendres A) contient un radical alkyle de 15 à 500 atomes C.
  5. Utilisation selon la revendication 4, dans laquelle le radical alkyle est dérivé d'oligomères d'oléfines inférieures contenant 3 à 6 atomes C ou leurs mélanges.
  6. Utilisation selon la revendication 5, dans laquelle un mélange d'oligomères d'oléfines inférieures contenant 3 à 6 atomes C est utilisé, qui contient plus de 70 % en moles de 2-méthyl-2-butène, de 2,3-diméthyl 2-butène et/ou d'isobutène.
  7. Utilisation selon une ou plusieurs des revendications 1 à 6, dans laquelle l'additif détergent azoté sans cendres A) est fabriqué en utilisant des polyoléfines de faible poids moléculaire hautement réactives, qui présentent des poids moléculaires de 500 à 3 000 g/mol, ayant une proportion de doubles liaisons terminales d'au moins 75 % en moles.
  8. Utilisation selon la revendication 1, dans laquelle R9 représente l'hydrogène et q prend des valeurs d'au moins 3.
  9. Utilisation selon une ou plusieurs des revendications 1 à 8, dans laquelle l'additif détergent azoté sans cendres A) comprend un radical alkyle soluble dans les huiles et un groupe de tête polaire, et le radical alkyle soluble dans les huiles et le groupe de tête polaire sont reliés l'un avec l'autre par une liaison C-N ou par une liaison ester, amide ou imide.
  10. Utilisation selon une ou plusieurs des revendications 1 à 9, dans laquelle l'additif détergent azoté sans cendres A) présente un poids moléculaire moyen déterminé par osmométrie sous pression de vapeur supérieur à 800 g/mol.
  11. Utilisation selon une ou plusieurs des revendications 1 à 10, dans laquelle les polymères en peigne agissant en tant qu'agent de nucléation pour la cristallisation de paraffines présentent une proportion de chaînes latérales alkyle contenant au moins 20 atomes C, par rapport à la quantité totale des chaînes latérales alkyle du polymère en peigne, d'au moins 10 % en moles.
  12. Utilisation selon une ou plusieurs des revendications 1 à 11, dans laquelle les polymères en peigne agissant en tant qu'agent de nucléation pour la cristallisation de paraffines portent des chaînes latérales contenant 22 à 60 atomes C.
  13. Utilisation selon une ou plusieurs des revendications 1 à 12, dans laquelle les chaînes latérales alkyle des polymères en peigne sont linéaires.
  14. Utilisation selon une ou plusieurs des revendications 1 à 13, dans laquelle les polymères en peigne agissant en tant qu'agent de nucléation pour la cristallisation de paraffines contiennent un squelette constitué par des acides monocarboxyliques éthyléniquement insaturés, des acides polycarboxyliques ou un mélange de ceux-ci.
  15. Utilisation selon une ou plusieurs des revendications 1 à 14, dans laquelle les chaînes latérales alkyle des polymères en peigne sont reliées au squelette polymère par un groupe ester, amide, imide ou ammonium.
  16. Utilisation selon une ou plusieurs des revendications 1 à 13 et 15, dans laquelle les polymères en peigne agissant en tant qu'agent de nucléation pour la cristallisation de paraffines sont des polycondensats contenant des unités structurales dérivées de composés aromatiques d'alkyle, qui comprennent des radicaux alkyle d'au moins 20 atomes C.
  17. Utilisation selon la revendication 16, dans laquelle les radicaux alkyle sont reliés aux composés aromatiques par une liaison C-C ou par un groupe ester ou éther.
  18. Utilisation selon une ou plusieurs des revendications 1 à 17, dans laquelle le rapport de quantités entre l'additif détergent A) et le polymère en peigne agissant en tant qu'agent de nucléation pour la cristallisation de paraffines B) dans l'huile supplémentée est de 0,01 à 10 parties en poids d'agent de nucléation par partie en poids d'additif détergent, à chaque fois par rapport à l'agent actif.
  19. Distillats moyens ayant une teneur en soufre inférieure à 100 ppm et un point de distillation à 90 % inférieur à 360 °C, contenant :
    a) au moins un additif détergent azoté sans cendres A), qui est un composé amphiphile soluble dans les huiles, qui comprend au moins un radical alkyle ou alcényle, qui est relié à un groupe polaire, le radical alkyle ou alcényle comprenant 10 à 500 atomes C et le groupe polaire comprenant 2 atomes d'azote ou plus, l'additif détergent azoté sans cendres A) comprenant une fraction polaire, qui est dérivée de polyamines de formule

            (R9)2N-[A-N(R9)]q-(R9)

    dans laquelle les R9 représentent chacun indépendamment les uns des autres l'hydrogène, un radical alkyle ou hydroxyalkyle contenant jusqu'à 24 atomes C, un radical polyoxyalkylène -(A-O)r- ou un radical polyiminoalkylène -[A-N(R9)]s-(R9), au moins un R9 représentant toutefois l'hydrogène, q représente un nombre entier de 1 à 19, A représente un radical alkylène de 1 à 6 atomes C, et r et s représentent indépendamment l'un de l'autre des nombres entiers de 1 à 50, et
    b) au moins un composé B) soluble dans les huiles, agissant en tant qu'agent de nucléation pour la cristallisation de paraffines, choisi parmi les polymères en peigne qui portent des chaînes latérales alkyle d'une longueur d'au moins 18 atomes C en moyenne molaire, ainsi que
    c) au moins un agent d'amélioration de l'écoulement à froid des huiles minérales C) différent de B), des composés azotés polaires solubles dans les huiles étant utilisés en tant qu'agents d'amélioration de l'écoulement à froid C), qui sont des produits de réaction de composés de formule NR6R7R8, dans laquelle R6, R7 et R8 peuvent être identiques ou différents, et au moins un de ces groupes représente alkyle en C8-C36, cycloalkyle en C6-C36, alcényle en C8-C36, notamment alkyle en C12-C24, alcényle en C12-C24 ou cyclohexyle, et les autres groupes signifient soit hydrogène, alkyle en C1-C36, alcényle en C2-C36, cyclohexyle, soit un groupe de formule -(A-O)x-E ou-(CH2)n-NYZ, A représentant un groupe éthyle ou propyle, x signifiant un nombre de 1 à 50, E = H, alkyle en C1-C30, cycloalkyle en C5-C12 ou aryle en C6-C30, et n = 2, 3 ou 4, et Y et Z signifiant indépendamment l'un de l'autre H, alkyle en C1-C30 ou -(A-O)x, avec des composés qui contiennent au moins un groupe acyle, et dans lesquels 10 à 10 000 ppm de l'additif détergent azoté sans cendres A), ainsi que, par partie en poids de ce constituant A), 0,1 à 10 parties en poids du composé B) soluble dans les huiles, agissant en tant qu'agent de nucléation pour la cristallisation de paraffines, sont contenus.
EP08759257.2A 2007-06-20 2008-06-17 Huiles minérales contenant des additifs détergents dotées d'une fluidité à froid améliorée Active EP2162513B1 (fr)

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DE102007028305A DE102007028305A1 (de) 2007-06-20 2007-06-20 Detergenzadditive enthaltende Mineralöle mit verbesserter Kältefließfähigkeit
PCT/EP2008/004851 WO2008155089A1 (fr) 2007-06-20 2008-06-17 Huiles minérales contenant des additifs détergents dotées d'une fluidité à froid améliorée

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Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7875747B2 (en) * 2006-10-10 2011-01-25 Afton Chemical Corporation Branched succinimide dispersant compounds and methods of making the compounds
DE102007028307A1 (de) * 2007-06-20 2008-12-24 Clariant International Limited Detergenzadditive enthaltende Mineralöle mit verbesserter Kältefließfähigkeit
DE102007028304A1 (de) * 2007-06-20 2008-12-24 Clariant International Limited Detergenzadditive enthaltende Mineralöle mit verbesserter Kältefließfähigkeit
DE102007028306A1 (de) * 2007-06-20 2008-12-24 Clariant International Limited Detergenzadditive enthaltende Mineralöle mit verbesserter Kältefließfähigkeit
US20130239465A1 (en) * 2012-03-16 2013-09-19 Baker Hughes Incorporated Cold Flow Improvement of Distillate Fuels Using Alpha-Olefin Compositions
WO2018064270A1 (fr) 2016-09-29 2018-04-05 Ecolab USA, Inc. Inhibiteurs de paraffine, compositions de suppression de paraffine et procédés
RU2752630C2 (ru) 2016-09-29 2021-07-29 ЭКОЛАБ ЮЭсЭй, ИНК. Композиции парафинового супрессанта и способы
GB201810852D0 (en) 2018-07-02 2018-08-15 Innospec Ltd Compositions, uses and methods
BR112021007666A2 (pt) 2018-10-29 2021-07-27 Championx Usa Inc. método para inibir a formação de aglomerados de hidratos de gás natural, composição, e, uso do composto à base de succinimida.
JP2023539763A (ja) 2020-09-01 2023-09-19 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ エンジン油組成物
JP2023541114A (ja) 2020-09-14 2023-09-28 エコラボ ユーエスエー インコーポレイティド プラスチック由来の合成原料のための低温流動性添加剤
WO2023064375A1 (fr) 2021-10-14 2023-04-20 Ecolab Usa Inc. Agents antisalissure pour matières premières synthétiques dérivées du plastique

Family Cites Families (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4022589A (en) * 1974-10-17 1977-05-10 Phillips Petroleum Company Fuel additive package containing polybutene amine and lubricating oil
US4108613A (en) * 1977-09-29 1978-08-22 Chevron Research Company Pour point depressants
US4261703A (en) * 1978-05-25 1981-04-14 Exxon Research & Engineering Co. Additive combinations and fuels containing them
US4211534A (en) 1978-05-25 1980-07-08 Exxon Research & Engineering Co. Combination of ethylene polymer, polymer having alkyl side chains, and nitrogen containing compound to improve cold flow properties of distillate fuel oils
FR2426730A1 (fr) * 1978-05-25 1979-12-21 Exxon Research Engineering Co Compositions d'additifs pour ameliorer l'ecoulement et la filtrabilite des fuel-oils distilles
US4357148A (en) * 1981-04-13 1982-11-02 Shell Oil Company Method and fuel composition for control or reversal of octane requirement increase and for improved fuel economy
DE3405843A1 (de) * 1984-02-17 1985-08-29 Bayer Ag, 5090 Leverkusen Copolymere auf basis von maleinsaeureanhydrid und (alpha), (beta)-ungesaettigten verbindungen, ein verfahren zu ihrer herstellung und ihre verwendung als paraffininhibitoren
GB2174102A (en) * 1985-04-24 1986-10-29 Shell Int Research Diesel fuel composition
US4968321A (en) * 1989-02-06 1990-11-06 Texaco Inc. ORI-inhibited motor fuel composition
DE3916366A1 (de) 1989-05-19 1990-11-22 Basf Ag Neue umsetzungsprodukte von aminoalkylenpolycarbonsaeuren mit sekundaeren aminen und erdoelmitteldestillatzusammensetzungen, die diese enthalten
US5006130A (en) * 1989-06-28 1991-04-09 Shell Oil Company Gasoline composition for reducing intake valve deposits in port fuel injected engines
DE3926992A1 (de) * 1989-08-16 1991-02-21 Hoechst Ag Verwendung von umsetzungsprodukten von alkenylspirobislactonen und aminen als paraffindispergatoren
GB9213870D0 (en) * 1992-06-30 1992-08-12 Exxon Chemical Patents Inc Oil additives and compositions
GB9222458D0 (en) * 1992-10-26 1992-12-09 Exxon Chemical Patents Inc Oil additives and compositions
US5286264A (en) * 1992-12-21 1994-02-15 Texaco Inc. Gasoline detergent additive composition and motor fuel composition
ES2110124T3 (es) * 1993-01-06 1998-02-01 Clariant Gmbh Termopolimeros a base de anhidridos de acidos carboxilicos alfa,beta-insaturados, de compuestos alfa,beta-insaturados y de polioxialquileneteres de alcoholes inferiores insaturados.
GB9315205D0 (en) * 1993-07-22 1993-09-08 Exxon Chemical Patents Inc Additives and fuel compositions
DE4430294A1 (de) 1994-08-26 1996-02-29 Basf Ag Polymermischungen und ihre Verwendung als Zusatz für Erdölmitteldestillate
GB9610363D0 (en) * 1996-05-17 1996-07-24 Ethyl Petroleum Additives Ltd Fuel additives and compositions
ATE223953T1 (de) * 1997-01-07 2002-09-15 Clariant Gmbh Verbesserung der fliessfähigkeit von mineralölen und mineralöldestillaten unter verwendung von alkylphenol-aldehydharzen
US6733550B1 (en) * 1997-03-21 2004-05-11 Shell Oil Company Fuel oil composition
GB9725579D0 (en) * 1997-12-03 1998-02-04 Exxon Chemical Patents Inc Additives and oil compositions
DE10155748B4 (de) * 2001-11-14 2009-04-23 Clariant Produkte (Deutschland) Gmbh Schwefelarme Mineralöldestillate mit verbesserten Kälteeigenschaften, umfassend einen Ester eines alkoxylierten Polyols und ein Copolymer aus Ethylen und ungesättigten Estern
ES2554978T3 (es) * 2005-12-22 2015-12-28 Clariant Produkte (Deutschland) Gmbh Aceites minerales que contienen unos aditivos para conferir detergencia con una mejorada capacidad para fluir en frío
DE102007028304A1 (de) * 2007-06-20 2008-12-24 Clariant International Limited Detergenzadditive enthaltende Mineralöle mit verbesserter Kältefließfähigkeit
DE102007028306A1 (de) * 2007-06-20 2008-12-24 Clariant International Limited Detergenzadditive enthaltende Mineralöle mit verbesserter Kältefließfähigkeit
DE102007028307A1 (de) * 2007-06-20 2008-12-24 Clariant International Limited Detergenzadditive enthaltende Mineralöle mit verbesserter Kältefließfähigkeit

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
None *

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KR101553225B1 (ko) 2015-09-15
US20100180492A1 (en) 2010-07-22
JP5517924B2 (ja) 2014-06-11
WO2008155089A1 (fr) 2008-12-24
CA2691067A1 (fr) 2008-12-24
RU2010101618A (ru) 2011-07-27
DE102007028305A1 (de) 2008-12-24
EP2162513A1 (fr) 2010-03-17
RU2475517C2 (ru) 2013-02-20
PL2162513T3 (pl) 2019-10-31
JP2010530452A (ja) 2010-09-09

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