AU2011269024A1 - Quaternized copolymer - Google Patents

Quaternized copolymer Download PDF

Info

Publication number
AU2011269024A1
AU2011269024A1 AU2011269024A AU2011269024A AU2011269024A1 AU 2011269024 A1 AU2011269024 A1 AU 2011269024A1 AU 2011269024 A AU2011269024 A AU 2011269024A AU 2011269024 A AU2011269024 A AU 2011269024A AU 2011269024 A1 AU2011269024 A1 AU 2011269024A1
Authority
AU
Australia
Prior art keywords
acid
copolymer
quaternized
alkyl
give
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Abandoned
Application number
AU2011269024A
Inventor
Harald Boehnke
Wolfgang Grabarse
Hannah Maria Koenig
Cornelia Roeger-Goepfert
Christian Tock
Ludwig Voelkel
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
BASF SE
Original Assignee
BASF SE
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by BASF SE filed Critical BASF SE
Publication of AU2011269024A1 publication Critical patent/AU2011269024A1/en
Abandoned legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F8/00Chemical modification by after-treatment
    • C08F8/44Preparation of metal salts or ammonium salts
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F210/00Copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • C08F210/04Monomers containing three or four carbon atoms
    • C08F210/08Butenes
    • C08F210/10Isobutene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F8/00Chemical modification by after-treatment
    • C08F8/30Introducing nitrogen atoms or nitrogen-containing groups
    • C08F8/32Introducing nitrogen atoms or nitrogen-containing groups by reaction with amines
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/234Macromolecular compounds
    • C10L1/236Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derivatives thereof
    • C10L1/2364Macromolecular 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
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/234Macromolecular compounds
    • C10L1/236Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derivatives thereof
    • C10L1/2366Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derivatives thereof homo- or copolymers derived from unsaturated compounds containing amine groups
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/234Macromolecular compounds
    • C10L1/236Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derivatives thereof
    • C10L1/2368Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derivatives thereof homo- or copolymers derived from unsaturated compounds containing heterocyclic compounds containing nitrogen in the ring
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/18Use of additives to fuels or fires for particular purposes use of detergents or dispersants for purposes not provided for in groups C10L10/02 - C10L10/16
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L2230/00Function and purpose of a components of a fuel or the composition as a whole
    • C10L2230/22Function and purpose of a components of a fuel or the composition as a whole for improving fuel economy or fuel efficiency

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Health & Medical Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)
  • Liquid Carbonaceous Fuels (AREA)

Abstract

The invention relates to a quaternized copolymer, which can be obtained by: (A) copolymerizing straight-chain, branched or cyclic ethylenically unsaturated C2 to C100 hydrocarbons, which can bear oxygen-functional or nitrogen-functional substituents which cannot be reacted with amines to obtain amides or imides, or with alcohols to obtain esters, with ethylenically unsaturated C

Description

1 Quaternized copolymer Description 5 The present invention relates to a quaternized copolymer which by the reaction steps of (A) copolymerization of one or more straight-chain, branched or cyclic, ethylenically unsaturated C2 to C100 hydrocarbons (monomer M1), which may bear one or 10 more oxygen- or nitrogen-functional substituents which cannot be reacted with amines to give amides or imides or with alcohols to give esters, with one or more ethylenically unsaturated C3- to C12-carboxylic acids or C3- to C 12 -carboxylic acid derivatives (monomer M2), which bear one or two carboxylic acid functions and can be reacted with amines to give amides or imides or with alcohols to give 15 esters, to give a copolymer (CP) with a number-average molecular weight Ma of 500 to 20 000; (B) partial or full amidation or imidation or esterification of the carboxylic acid functions of the (M2) units in the copolymer (CP) by reacting them with one or 20 more oligoamines (OA) having 2 to 6 nitrogen atoms or alcoholamines (AA), each of which comprises at least one primary or secondary nitrogen atom or at least one hydroxyl group and at least one quaternizable tertiary nitrogen atom; (C) partial or full quaternization of the at least one tertiary nitrogen atom in the OA or 25 AA units with at least one quaternizing agent (QM); where the sequence of steps (B) and (C) may also be reversed, such that the partial or full amidation or imidation of esterification of the carboxylic acid functions of the (M2) units in the copolymer (CP) can be effected by reacting with the oligoamines (OA) or 30 alcoholamines (AA) already quaternized in reaction step (C). The present invention further relates to a process for preparing such a quaternized copolymer. 35 The present invention also relates to fuels having a content of such a quaternized copolymer. The present invention further relates to the use of this quaternized copolymer as a fuel additive for reducing or preventing deposits in the injection systems of direct-injection 40 diesel engines, especially in common-rail injection systems, for reducing fuel consumption in direct-injection diesel engines, especially in diesel engines with common-rail injection systems, and for minimizing power loss in direct-injection diesel engines, especially in diesel engines with common-rail injection systems.
2 In direct-injection diesel engines, the fuel is injected and distributed ultrafinely (nebulized) by a multihole injection nozzle which reaches directly into the combustion chamber in the engine, instead of being introduced into a prechamber or swirl chamber 5 as in the case of the conventional (chamber) diesel engine. The advantage of the direct-injection diesel engines lies in their high performance for diesel engines and a nevertheless low fuel consumption. Moreover, these engines achieve a very high torque even at low speeds. 10 At present, essentially three methods are being used to inject the fuel directly into the combustion chamber of the diesel engine: the conventional distributor injection pump, the pump-nozzle system (unit-injector system or unit-pump system) and the common rail system. 15 In the common-rail system, the diesel fuel is conveyed by a pump with pressures up to 2000 bar into a high-pressure line, the common rail. Proceeding from the common rail, branch lines run to the different injectors which inject the fuel directly into the combustion chamber. The full pressure is always applied to the common rail, which enables multiple injection or a specific injection form. In the other injection systems, in 20 contrast, only one injection is possible. The injection in the common rail is divided essentially into three groups: (1.) pre-injection, by which essentially softer combustion is achieved, such that hard combustion noises ("nailing") are reduced and the engine appears to run quietly; (2.) main injection, which is responsible especially for a good torque profile; and (3.) post-injection, which especially ensures a low NOx value. In this 25 post-injection, the fuel is generally not combusted, but instead evaporated by residual heat in the cylinder. The exhaust gas/fuel mixture formed is transported to the exhaust gas system, where the fuel, in the presence of suitable catalysts, acts as a reducing agent for the nitrogen oxides NOx. 30 The variable, cylinder-individual injection in the common-rail injection system can positively influence the pollutant emission of the engine, for example the emission of nitrogen oxides (NOx), carbon monoxide (CO) and especially of particulates (soot). This makes it possible, for example, that engines equipped with common-rail injection systems can meet the Euro 4 standard theoretically even without additional particulate 35 filters. In modern common-rail diesel engines, under particular conditions, for example when biodiesel-containing fuels or fuels with metal impurities such as zinc compounds are used, deposits can form on the injector orifices, which adversely affect the injection 40 performance of the fuel and hence impair the performance of the engine, i.e. especially reduce the power, but in some cases also worsen the combustion. The formation of deposits is enhanced further by further developments of the injector construction, especially by the change in the geometry of the nozzles (narrower, conical orifices with 3 rounded outlet). For lasting optimal functioning of engine and injectors, such deposits in the nozzle orifices must be prevented or reduced by suitable fuel additives. It was therefore an object of the present invention to provide fuel additives which 5 remedy the shortcomings outlined above, i.e. more particularly prevent or reduce deposits in the injection systems, in particular in the injectors, of direct-injection diesel engines, reduce fuel consumption in direct-injection diesel engines and minimize power losses in such engines. 10 The prior art discloses CB- to C20 0 -alkyl- or -alkenylsuccinimides as detergent additives for fuels such as middle distillate fuels and gasoline fuels. For instance, WO 02/092645 (1) describes polyalkenylsuccinimides such as polyisobutenylsuccinimides as additives to fuels such as diesel fuel, heating oil or gasoline fuel, or to lubricants, which - obviously as a result of the preparation - may 15 comprise up to 30% by weight of the corresponding polyalkenylsuccinamides or -succinic monoamides. These polyalkenylsuccinimides are said to counteract engine deposits and deposits on the injection nozzles. WO 2006/100083 (2) discloses that particular detergent additives reduce the amount of 20 particulates in the exhaust gas emissions of direct-injection diesel engines such as diesel engines with common-rail injection systems. Detergent additives include additives comprising moieties which are derived from succinic anhydride and have hydroxyl and/or amino and/or amido and/or imido groups, such as the corresponding derivatives of polyisobutenylsuccinic anhydride, especially derivatives with aliphatic 25 polyamines. The moieties with hydroxyl and/or amino and/or amido and/or imido groups are, for example, carboxylic acid groups, acid amides of monoamines, acid amides of di- or polyamines, which still have free amino groups as well as the amide function, succinic acid derivatives with one acid and one amide function, carboximides with monoamines, carboximides with di- or polyamines, which still have free amine 30 groups as well as the imide function, or diimides which are formed by reaction of di- or polyamines with two succinic acid derivatives. EP 1 887 074 Al (3) describes a process for removing or reducing injector deposits in diesel engines using reaction products between a hydrocarbyl-substituted succinic acid 35 or anhydride thereof, for example polyisobutenylsuccinic anhydride, and hydrazine. Among these reaction products, monohydrazide structures are also mentioned. WO 2006/135881 (4) describes the condensation of hydrocarbyl-substituted acylating agents, which are obtainable by ene reaction of olefins with maleic anhydride, with 40 mines having an additional tertiary amino group and subsequent quaternization of the tertiary amino group to give quaternary ammonium salts, which are suitable as fuel additives for cleaning and keeping clean intake systems of internal combustion engines.
4 The above-described C 8
-C
200 -alkyl- or -alkenylsuccinimides which are known from the prior art and frequently used in practice, such as polyisobutenylsuccinimides and related systems, are capable of achieving the specific object outlined only to an 5 insufficient degree; however, the additional use thereof in the present invention as further fuel additives in a minor amount is not harmful. This object is achieved by the use of the quaternized copolymer cited at the outset, which is obtainably by reaction steps (A), (B) and (C). 10 The present application also provides a process for preparing a quaternized copolymer, which comprises performing the following reaction steps: (A) copolymerization of one or more straight-chain, branched or cyclic, ethylenically 15 unsaturated C2 to Cio hydrocarbons (monomer Ml), which may bear one or more oxygen- or nitrogen-functional substituents which cannot be reacted with amines to give amides or imides or with alcohols to give esters, with one or more ethylenically unsaturated C3- to C 1 2-carboxylic acids or C3- to C12-carboxylic acid derivatives (monomer M2), which bear one or two carboxylic acid functions and 20 can be reacted with amines to give amides or imides or with alcohols to give esters, to give a copolymer (CP) with a number-average molecular weight M, of 500 to 20 000; (B) partial or full amidation or imidation or esterification of the carboxylic acid 25 functions of the (M2) units in the copolymer (CP) by reacting them with one or more oligoamines (OA) having 2 to 6 nitrogen atoms or alcoholamines (AA), each of which comprises at least one primary or secondary nitrogen atom or at least one hydroxyl group and at least one quaternizable tertiary nitrogen atom; 30 (C) partial or full quaternization of the at least one tertiary nitrogen atom in the OA or AA units with at least one quaternizing agent (QM); where the sequence of steps (B) and (C) may also be reversed, such that the partial or full amidation or imidation of esterification of the carboxylic acid functions of the (M2) 35 units in the copolymer (CP) can be effected by reacting with the oligoamines (OA) or alcoholamines (AA) already quaternized in reaction step (C). The copolymer (CP) obtained in reaction step (A) is known in principle from EP-A 307 815 (6). The use of the copolymer (CP) in the form of the alkali metal or alkaline earth 40 metal salts is recommended therein for prevention or reduction of wear phenomena on the valves of gasoline engines and for simultaneous reduction of corrosion in gasoline engines.
5 Examples of optional oxygen- or nitrogen-functional substitutes which may occur in the monomers (Ml) in reaction step (A) are ether oxygen atoms or carboxamide moieties. In a preferred embodiment, the monomers (Ml) in reaction step (A) are selected from 5 C2- to C40-alkenes, C3- to Clo-cycloolefins, alkyl vinyl ethers having 1 to 30 carbon atoms in the alkyl group, cycloalkyl vinyl ethers having 3 to 10 carbon atoms in the alkyl group and oligo- or polyisobutenes having 8 to 96 carbon atoms. Examples of very suitable straight-chain or branched C2- to C4o-alkenes are ethylene, 10 propylene, butene-1, isobutene, pentene-1, 3-methylbutene-1, hexene-1, 4-methyl pentene-1,3,3-dimethylbutene-1, heptene-1, 4-methylhexene-1, 5-methylhexene-1, 4,4 dimethylpentene-1, octene-1, 2,4,4-trimethylpentene- 1, 2,4,4-trimethylpentene-2, isomer mixture of 2,4,4-trimethylpentene-1 and 2,4,4-trimethylpentene-2 ("diisobutene"), 4,4-dimethylhexene-1, decene-1, dodecene-1, tetradecene-1, 15 hexadecene-1, octadecene-1, C2 0 -olefin-1, C 22 -olefin-1, C24-olefin-1, C20-olefin-1, C28 olefin-1, C 3 o-olefin-1, C 40 -olefin-1, C20-24-olefin-1, C 22
/
24 -olefin-1, C24-2 8 -olefin-1, and mixtures of the alkenes mentioned with one another. Among these, preference is given to straight-chain or branched C12- to C 30 -alkenes, especially straight-chain or branched C1e- to C2-alkenes, in particular straight-chain or branched C20- to C 24 -alkenes. 20 Examples of very suitable C3- to Clo-cycloolefins are cyclobutene, cyclopentene, cyclohexene, cycloheptene and cyclooctene, and mixtures of the cycloolefins mentioned with one another. Among these, cyclopentene and cyclohexene are preferred. 25 Examples of very suitable alkyl vinyl ethers having 1 to 30 carbon atoms in the straight chain or branched alkyl group are methyl vinyl ether, ethyl vinyl ether, n-propyl vinyl ether, isopropyl vinyl ether, n-butyl vinyl ether, isobutyl vinyl ether, tert-butyl vinyl ether, n-pentyl vinyl ether, n-hexyl vinyl ether, 2-methylpentyl vinyl ether, n-heptyl vinyl ether, 30 n-octyl vinyl ether, 2-ethylhexyl vinyl ether, 2,2,4-trimethylpentyl vinyl ether, n-decyl vinyl ether, 2-propylheptyl vinyl ether, n-dodecyl vinyl ether, isododecyl vinyl ether, n tridecyl vinyl ether, isotridecyl vinyl ether, n-tetradecyl vinyl ether, n-hexadecyl vinyl ether, n-octadecyl vinyl ether, n-eicosyl vinyl ether, n-docosyl vinyl ether, n-tetracosyl vinyl ether, n-hexacosyl vinyl ether, n-octacosyl vinyl ether, oleyl vinyl ether, and 35 mixtures of the alkyl vinyl ethers mentioned with one another. Among these, preference is given to alkyl vinyl ethers with straight-chain or branched Ca- to C2-alkyl groups, especially straight-chain or branched C12- to C24-alkyl groups, in particular straight chain or branched C16- to C 22 -alkyl groups. 40 Examples of very suitable cycloalkyl vinyl ethers having 3 to 10 carbon atoms in the cycloalkyl group are cyclobutyl vinyl ether, cyclopentyl vinyl ether, cyclohexyl vinyl ether, cycloheptyl vinyl ether and cyclooctyl vinyl ether, and mixtures of the cycloalkyl 6 vinyl ethers mentioned with one another. Among these, preference is give to cyclopentyl vinyl ether and cyclohexyl vinyl ether. Useful oligo- or polyisobutenes having 8 to 96 carbon atoms, especially 44 to 92 5 carbon atoms, are in particular polyisobutenes with a high content of terminal (a) double bonds, typically of at least 70 mol%, especially of at least 80 mol%, for example those with a number-average molecular weight Mn of 550, 700 or 1000. In addition to the preferred monomers (M1) mentioned, it is, for example, also possible 10 to use acrylamides or methacrylamides such as N-(C-Cao-alkyl)acrylamides, N,N-di (C-C3o-alkyl)acrylamides, N-(C1-C3-alky)methacrylamides or N,N-di(C-Cso-alkyl) methacrylamides as monomers (Mi). The monomers (M1) in reaction step (A) preferably bear the polymerizable ethylenically 15 unsaturated double bond in the a position, i.e. the ethylenically unsaturated double bond is in the terminal position in the form of the structural element >C=H 2 in the monomer (Mi). In a preferred embodiment, the monomers (M2) in reaction step (A) are selected from 20 acrylic acid, methacrylic acid, maleic acid, fumaric acid and itaconic acid, and the anhydrides thereof, halides thereof, i.e. the fluorides, chlorides, bromides or iodides thereof, and esters thereof, especially the Cj- to Co-alkyl esters thereof. Particular preference is given to maleic acid and maleic anhydride. 25 In addition to the preferred monomers (M2) mentioned, it is, for example, also possible to use crotonic acid, isocrotonic acid, but-1-enecarboxylic acid, pent-1-enecarboxylic acid, hex-1-enecarboxylic acid, hept-1-enecarboxylic acid, oct-1-enecarboxylic acid, non-1-enecarboxylic acid, dec-1-enecarboxylic acid, undec-1-enecarboxylic acid, citraconic acid or mesaconic acid, and the anhydrides thereof, halides thereof, i.e. the 30 fluorides, chlorides, bromides or iodides thereof, and esters thereof, especially the Cj to Co-alkyl esters thereof, as monomers (M2). Typically, the monomer units (M1) and (M2) are present in a weight ratio of 30:70 to 70:30, especially 40:60 to 60:40, in the copolymer (CP) of reaction step (A). 35 The copolymer (CP) has a number-average molecular weight Mn of 500 to 20 000, especially of 1000 to 18 000, in particular of 4000 to 16 000 (determined in each case by gel permeation chromatography), and generally a polydispersity (quotient of weight average molecular weight and number-average molecular weight: PDI = Mw/Mn) of 1.3 40 to 10, especially of 1.6 to 5, in particular of 2.0 to 2.5. The two monomer units (M1) and (M2) are generally present in alternating or random distribution in the copolymer (CP). However, it is possible in principle by particular 7 process regimes known to those skilled in the art also to obtain block copolymers from the monomers (MI) and (M2). The monomers (M1) and (M2) are generally copolymerized by free-radical means. The 5 copolymerization makes use of known customary polymerization techniques, such as bulk polymerization, suspension polymerization, precipitation polymerization or solution polymerization. It is generally initiated with the customary free-radical initiators, for example with acetylcyclohexanesulfonyl peroxide, diacetyl peroxydicarbonate, dicyclohexyl peroxydicarbonate, di-2-ethylhexyl peroxydicarbonate, tert-butyl 10 perneodecanoate, 2,2'-azobis(4-methoxy-2,4-dimethylvaleronitrile), tert-butyl perpivalate, tert-butyl per-2-ethylhexanoate, tert-butyl permaleate, 2,2'-azobis (isobutyronitrile), bis(tert-butyl peroxide)cyclohexane, tert-butyl peroxyisopropylcarbonate, tert-butyl peracetate, dicumyl peroxide, di-tert-amyl peroxide, di-tert-butyl peroxide, p-methane hydroperoxide, cumene hydroperoxide, tert 15 butyl hydroperoxide or mixtures of the free-radical initiators mentioned. Typically, these free-radical initiators are used in amounts of 0.1 to 10% by weight, especially 0.2 to 5% by weight, calculated using the total amount of monomers used. In general, the copolymerization is effected at temperatures of 40 to 250*C, especially 20 80 to 2200C, appropriately working under pressure when using volatile monomers (Ml) with boiling points below the copolymerization temperature. The copolymerization is typically perfomed with exclusion of air or oxygen, i.e. if it is not possible to work under boiling conditions, inertizing agents such as nitrogen are used, since oxygen retards the copolymerization. The additional use of redox coinitiators, for example benzoin, 25 dimethylaniline, ascorbic acid, and organic-soluble complexes of heavy metals such as copper, cobalt, manganese, iron, nickel and chromium, can accelerate the copolymerization. To control the molecular weight, especially to obtain a copolymer with relatively low 30 molecular weight, regulators can be used additionally. Suitable regulators are, for example, allyl alcohols and organic mercapto compounds, such as 2-mercaptoethanol, 2-mercaptopropanol, mercaptoacetic acid, mercaptopropionic acid, tert-buty mercaptan, n-octyl mercaptan, n-dodecyl mercaptan or tert-dodecyl mercaptan, which are typically used in amounts of 0.1 to 10% by weight, based on the total amount of the 35 monomers used. When the polymerization technique of suspension polymerization, precipitation polymerization or solution polymerization is employed in the preparation of (CP), the use of a suitable inert solvent or solvent mixture is required. Suitable for this purpose 40 are generally - of course always specifically for the particular polymerization technique employed - for example aliphatic and cycloaliphatic hydrocarbons such as pentane, hexane, heptane, octane, isooctane, cyclohexane, methylcyclohexane, ethylcyclohexane, dimethylcyclohexane or diethylcyclohexane, aromatic hydrocarbons 8 such as toluene, xylenes, ethylbenzene or cumene, technical-grade mixtures of relatively high-boiling aromatic hydrocarbons, as commercially available under the "Solvesso" name in particular, for example Solvesso 150 or Solvesso 200, aliphatic halohydrocarbons such as dichloromethane, chloroform, tetrachloromethane, 1,1- or 5 1,2-dichloroethane, 1,1,1- or 1,1,2-trichloroethane, 1,1,2-trichloroethylene, tetrachloroethylene, 1,2-dichloropropane, butyl chloride, 1,1,2-trichloro-1,2,2 trifluoroethane, 1,1,1,2-tetrachloro-2,2-difluoroethane or 1,1,2,2-tetrachloro-1,2 difluoroethane, and ethers such as diethyl ether, dipropyl ether, dibutyl ether, methyl tert-butyl ether, dioxane, tetrahydrofuran, diethylene glycol dimethyl ether and mixtures 10 of the solvents mentioned. In precipitation polymerization and suspension polymerization, the additional use of protective colloids is, respectively, appropriate and necessary. Protective colloids are usually polymeric substances which have good solubility in the solvent used and do not 15 enter into any reactions with the monomers. Suitable protective colloids which can be used in the preparation of (CP) are, for example, copolymers of maleic anhydride with vinyl alkyl ethers and/or olefins having 8 to 20 carbon atoms, and the monoesters thereof with C10- to C 20 -alcohols, or the mono- or diamides thereof with C10- to C20 alkylamines, and also polyalkyl vinyl ethers whose alkyl groups comprise 1 to 20 20 carbon atoms, for example polymethyl, polyethyl, polyisobutyl or polyoctadecyl vinyl ether. The amounts of protective colloids added are typically 0.05 to 4% by weight, especially 0.1 to 2% by weight, and it is often advantageous to combine a plurality of protective colloids. 25 The reaction equation depicted below shows, in accordance with the present invention, by way of example, the structures of a copolymer CP formed from C2 2 -olefin-1 and maleic anhydride ("MA") (where "MW" is the number-average molecular weight Mn), the corresponding amidation product with 3-(N,N-dimethylamino)propylamine ("DMPAP") and the corresponding quaternization product with propylene oxide ("PO") / acetic acid 30 ("HOAc"): 9 * nC0H O DMAPA : nC 22H N N C22-Olefin-MA Copolymer MW 4000-16000 0 HOAc, PO nC 22 4 5 OH N ni 0 The oligoamines (OA) used in reaction step (B) preferably have a total of 2 to 4 nitrogen atoms, especially a total of 2 or 3 nitrogen atoms, in particular a total of 2 5 nitrogen atoms, at least one of which in each case is a quaternizable tertiary nitrogen atom. The alcoholamines (AA) used in reaction step (B) have preferably I to 3 nitrogen atoms, at least one of which is a quaternizable tertiary nitrogen atom, and 1 to 3 10 hydroxyl groups, especially one quaternizable nitrogen atom and 1 to 3 hydroxyl groups, in particular one quaternizable tertiary nitrogen atom and one hydroxyl group. The hydroxyl groups are generally alcoholic hydroxyl groups, i.e. they are borne by an sp 3 -hybridized carbon atom. 15 The oligoamines (OA) and alcoholamines (AA) used in reaction step (B) typically have a total carbon number of not more than 75, especially of not more than 50, in -particular of not more than 30. For the partial or full amidation or imidation of the carboxylic acid functions of the units 20 (M2) in (CP) in reaction step (B), suitable oligoamines (OA) in a preferred embodiment are compounds of the general formula (la)
R
1
R
2
N-(CH
2
),-NR
3 R4 (la) 25 in which the variables R 1 and R 2 are each hydrogen or C1- to C2 0 -alkyl groups, where at least one of the variables R 1 and R 2 is hydrogen, 30 the variables R 3 and R 4 each independently denote C 1 - to C20-alkyl groups or, together with the nitrogen atom to which they are bonded, form a saturated, partly unsaturated 10 or unsaturated five-membered or six-membered heterocyclic ring, and the variable n is from 1 to 12, especially from 2 to 6, in particular 2 or 3. 5 For the partial or full esterification of the carboxylic acid functions of the units (M2) in (CP) in reaction step (B), suitable alcoholamines (AA) in a preferred embodiment are compounds of the general formula (Ib)
[HO-(CH
2 )m]xN(R 5 )y(R)z (I b) 10 in which the variables R 5 and R 6 each independently denote C1- to C 23 -alkyl groups or, in the case that y = z = 1, together with the nitrogen atom to which they are bonded, form a 15 saturated, partly unsaturated or unsaturated five-membered or six-membered heterocyclic ring, the variable m is from 1 to 12, especially from 2 to 6, in particular 2 or 3, and 20 the variables x, y and z are each 0, 1, 2 or 3, where the sum of x + y + z must give the value of 3. Examples of useful C1- to C2 0 -alkyl groups which may occur as substituents in the compounds of the general formulae (la) and (Ib) include methyl, ethyl, n-propyl, iso 25 propyl, n-butyl, isobutyl, sec-butyl, tert-butyl, n-pentyl, sec-pentyl, tert-pentyl, n-hexyl, n-heptyl, n-octyl, 2-ethylhexyl, n-nonyl, isononyl, 2-propylheptyl, n-decyl, n-dodecyl, n tridecyl, isotridecyl, n-tetradecyl, n-hexydecyl, n-octadecyl and eicosyl. Preferably C 1 to Ca-alkyl groups occur here, especially Ci- to C 4 -alkyl groups. 30 Examples of useful saturated, partly unsaturated or unsaturated five-membered or six membered heterocyclic rings which may form the variables R 3 and R 4 or R 5 and R 6 together with the nitrogen atom to which are they are bonded include imidazoles, benzimidazoles, pyrazoles, imidazolines, piperazines, piperidines or pyridines. 35 Examples of compounds of the general formula (]a) are 2-(N,N-dimethylamino) ethylamine, 2-(N,N-diethylamino)ethylamine, 2-(N,N-di-n-propylamino)ethylamine, 2 (N,N-diisopropylamino)ethylamine, 2-(N,N-di-n-butylamino)ethylamine, 3-(N,N dimethylamino)propylamine, 3-(N,N-diethylamino)propylamine, 3-(N,N-di-n propylamino)propylamine, 3-(N,N-diisopropylamino)propylamine, 3-(N,N-di-n 40 butylamino)propylamine, N-(2-aminoethyl)imidazole, N-(2-aminoethyl)benzimidazole, N-(3-aminopropyl)imidazole, N-(3-aminopropyl)benzimidazole, N-methylpiperazine, N ethylpiperazine, N-n-propylpiperazine, N-isopropylpiperazine and N-n-butylpiperazine.
11 Examples of the compounds of the general formula (Ib) are triethanolamine, tri-n propanolamine, triisopropanolamine, N-methyldiethanolamine, N-methyl-di-n-propanol amine, N-methyl-diisopropanolamine, N,N-dimethylethanolamine, N,N dimethylpropanolamine, N,N-dimethylisopropanolamine, N-(2-hydroxyethyl)imidazole, 5 N-(2-hydroxyethyl)benzimidazole, N-(3-hydroxypropyl)imidazole, N-(3-hydroxypropyl) benzimidazole, N-(2-hydroxyethyl)piperidine and N-(3-hydroxypropyl)piperidine. The amidation, imidation or esterification in reaction step (B) is typically performed in a suitable solvent or solvent mixture, for example in aliphatic and cycloaliphatic 10 hydrocarbons such as pentane, hexane, heptane, octane, isooctane, cyclohexane, methylcyclohexane, ethylcyclohexane, dirmethylcyclohexane or diethylcyclohexane, aromatic hydrocarbons such as toluene, xylenes, ethylbenzene or cumene, technical grade mixtures of relatively high-boiling aromatic hydrocarbons, as commercially available under the "Solvesso" name in particular, for example Solvesso 150 or 15 Solvesso 200, aliphatic halohydrocarbons such as dichloromethane, chloroform, tetrachloromethane, 1,1- or 1,2-dichloroethane, 1,1,1- or 1,1,2-trichloroethane, 1,1,2 trichloroethylene, tetrachloroethylene, 1,2-dichloropropane, butyl chloride, 1,1,2 trichloro-1,2,2-trifluoroethane, 1,1,1,2-tetrachloro-2,2-difluoroethane or 1,1,2,2 tetrachloro-1,2-difluoroethane, and ethers such as diethyl ether, dipropyl ether, dibutyl 20 ether, methyl tert-butyl ether, dioxane, tetrahydrofuran, diethylene glycol dimethyl ether and mixtures of the solvents mentioned. In the amidation and the esterification, the conditions are generally temperatures of 20 to 150"C, especially of 25 to 120"C; the reaction is complete when all volatile 25 compounds released in the reaction, such as water, hydrogen halide or alcohols, have been removed. In the case that an imide is obtained, the procedure in reaction step (B) preferably has two stages, by first performing an amidation - as described above - at temperatures of 20 to 150*C, especially of 25 to 120*C, and then heating to higher temperatures, appropriately to 120 to 250 0 C, especially to 150 to 200"C; it is advisable 30 here to use a correspondingly higher-boiling solvent or solvent mixture, such as Solvesso 150 or Solvesso 200, and/or to apply reduced pressure. Useful quaternizing agents (QM) for reaction step (C) are in principle all compounds suitable as such. In a preferred embodiment, however, the quaternization in reaction 35 step (C) of the at least one quaternizable tertiary nitrogen atom is effected with at least one quaternizing agent selected from epoxides, dialkyl sulfates, dialkyl sulfites, alkyl halides, arylalkyl halides, alkyl carboxylates and dialkyl carbonates. Suitable epoxides are, for example, C2-C12-alkylene oxides such as ethylene oxide, 40 propylene oxide, 1,2-butylene oxide, 2,3-butylene oxide, 2-methyl-1,2-propene oxide (isobutene oxide), 1,2-pentene oxide, 2,3-pentene oxide, 2-methyl-1,2-butene oxide, 3 methyl-1,2-butene oxide, 1,2-hexene oxide, 2,3-hexene oxide, 3,4-hexene oxide, 2 methyl-1,2-pentene oxide, 2-ethyl-1,2-butene oxide, 3-methyl-1,2-pentene oxide, 1,2- 12 decene oxide, 1,2-dodecene oxide or 4-methyl-1,2-pentene oxide, and aromatic substituted ethylene oxides such as styrene oxide or 4-methylstyrene oxide. In the case of use of epoxides as quaternizing agents, they are preferably used in 5 combination with protic acids, especially with C1-2-monocarboxylic acids such as formic acid, acetic acid or propionic acid, or C2-C1 2 -dicarboxylic acids such as oxalic acid or adipic acid; also suitable, however, are sulfonic acids such as benzenesulfonic acid or toluenesulfonic acid, or aqueous mineral acids such as sulfuric acid or hydrochloric acid. 10 Suitable dialkyl sulfates are preferably di(C-C 2 0 -alkyl) sulfates, especially di(Cr-C 4 alkyl) sulfates such as dimethyl sulfate or diethyl sulfate. On completion of quaternization, the monoalkyl sulfates and sulfates formed as counterions can be removed, i.e. exchanged, by treatment with anion exchangers. 15 Suitable dialkyl sulfites are preferably di(Cl-C2 0 -alkyl) sulfites, especially di(CI-C 4 -alkyl) sulfites such as dimethyl sulfite or diethyl sulfite. On completion of quaternization, the monoalkyl sulfites and sulfites formed as counterions can be removed, i.e. exchanged, by treatment with anion exchangers. 20 Suitable alkyl halides are preferably C-C2 0 -alkyl fluorides, chlorides, bromides or iodides, especially C 1
-C
4 -alkyl fluorides, chlorides, bromides or iodides, such as methyl chloride, methyl bromide, methyl iodide, ethyl chloride, ethyl bromide or ethyl iodide. On completion of quaternization, halide anions formed as counterions can be removed, 25 i.e. exchanged, by treatment with anion exchangers. Suitable benzyl halides are, for example, benzyl chloride, benzyl bromide or benzyl iodide; the benzene ring of the benzyl radical may in principle also bear one or more substituents such as C 1
-C
4 -alkyl groups. On completion of quaternization, the halide 30 anions formed as counterions can be removed, i.e. exchanged, by treatment with anion exchangers. Suitable alkyl carboxylates are preferably mono- or di(C-C 20 -alkyl) mono- or dicarboxylates, especially mono- or di(C-C 4 -alkyl) mono- or dicarboxylates, where the 35 parent mono- or dicarboxylic acid has 1 to 12 or 2 to 12 carbon atoms respectively, for example methyl formate or dimethyl oxalate. Similarly to the case of the epoxides, when using alkyl carboxylates as quaternizing agents, it is often advisable to use them preferably in combination with protic acids, especially with C-C1 2 -monocarboxylic acids such as formic acid, acetic acid or propionic acid, or C 2 -C1-dicarboxylic acids such as 40 oxalic acid or adipic acid, or else sulfonic acids such as benzenesulfonic acid or toluenesulfonic acid, or aqueous mineral acids such as sulfuric acid or hydrochloric acid.
13 Suitable alkyl carbonates are preferably di(Cr 1
C
20 -alkyl) carbonates, especially di(Cr C4-alkyl) carbonates such as dimethyl carbonate or diethyl carbonate. The quaternization of reaction step (C) - whether it be that of the isolated oligoamines 5 (OA) or alcoholamines (AA) or that of the (OA) or (AA) units in the already amidated, imidated or esterified copolymer (CP) - is performed by known techniques customary therefor. The conditions here are typically temperatures in the range from 15 to 180*C, especially from 20 to 1500C, and standard pressure or elevated pressure, at elevated pressure especially in the case of use of volatile quaternizing agents QM such as short 10 chain epoxides or alkyl halides, in which case it is appropriate to perform the quaternization reaction in a pressure vessel or autoclave. The quaternization reaction can be performed in an inert organic solvent such as toluene or xylene or in a technical-grade mixture of relatively high-boiling aromatic hydrocarbons, as commercially available under the "Solvesso" name in particular, for example in 15 Solvesso 150 or Solvesso 200. In general, 0.1 to 1.5 equivalents, especially 0.5 to 1.25 equivalents, of quaternizing agent are used per equivalent of quaternizable tertiary nitrogen atom, where the quaternizing agent may be a single chemical compound or a mixture of different chemical compounds suitable for quaternization. in the case of additional use of protic acids, they are typically used in equimolar amounts or in an up 20 to 2.5-fold excess to the quaternizing agent; in this case, it is possible to use a single protic acid or a mixture of different protic acids. The inventive quaternized copolymer is outstandingly suitable as a fuel additive and can in principle be used in any fuels. It brings about a whole series of advantageous 25 effects in the operation of internal combustion engines with fuels. The inventive quaternized copolymer is preferably used in gasoline fuels, but especially in middle distillate fuels. The present invention therefore also provides fuels, especially middle distillate fuels, 30 with a content of the inventive quaternized copolymer effective as an additive for achieving advantageous effects in the operation of internal combustion engines, for example of diesel engines, especially of direct-injection diesel engines, in particular of diesel engines with common-rail injection systems. This effective content (dosage) is generally 10 to 5000 ppm by weight, preferably 20 to 1500 ppm by weight, especially 35 25 to 1000 ppm by weight, in particular 30 to 750 ppm by weight, based in each case on the total amount of fuel. The fuel additized with the inventive quaternized copolymer is usually a gasoline fuel or especially a middle distillate fuel, in particular a diesel fuel. The fuel may comprise 40 further customary additives to improve efficacy and suppress wear. These include primarily customary detergent additives, carrier oils, lubricity additives, cetane number improvers, conductivity improvers, anticorrosion additives, antifoams and dehazers.
14 The customary detergent additives are preferably amphiphilic substances which possess at least one hydrophobic hydrocarbon radical with a number-average molecular weight (Me) of 85 to 20 000 and at least one polar moiety selected from: 5 (Da) mono- or polyamino groups having up to 6 nitrogen atoms, at least one nitrogen atom having basic properties; (Db) nitro groups, optionally in combination with hydroxyl groups; 10 (Dc) hydroxyl groups in combination with mono- or polyamino groups, at least one nitrogen atom having basic properties; (Dd) carboxyl groups or their alkali metal or alkaline earth metal salts; 15 (De) sulfonic acid groups or their alkali metal or alkaline earth metal salts; (Df) polyoxy-C2- to C4-alkylene moieties terminated by hydroxyl groups, mono- or polyamino groups, at least one nitrogen atom having basic properties, or by carbamate groups; 20 (Dg) carboxylic ester groups; (Dh) moieties derived from succinic anhydride and having hydroxyl and/or amino and/or amido and/or imido groups; and/or 25 (Di) moieties obtained by Mannich reaction of substituted phenols with aldehydes and mono- or polyamines. The hydrophobic hydrocarbon radical in the above detergent additives, which ensures 30 the adequate solubility in the fuel, has a number-average molecular weight (Mn) of 85 to 20 000, preferably of 113 to 10 000, more preferably of 300 to 5000, even more preferably of 300 to 3000, even more especially preferably of 500 to 2500 and especially of 700 to 2500, in particular of 800 to 1500. As typical hydrophobic hydrocarbon radicals, especially in conjunction with the polar especially polypropenyl, 35 polybutenyl and polyisobutenyl radicals with a number-average molecular weight M, of preferably in each case 300 to 5000, more preferably 300 to 3000, even more preferably 500 to 2500, even more especially preferably 700 to 2500 and especially 800 to 1500 into consideration. 40 Examples of the above groups of detergent additives include the following: Additives comprising mono- or polyamino groups (Da) are preferably polyalkenemono or polyalkenepolyamines based on polypropene or on high-reactivity (i.e. having 15 predominantly terminal double bonds) or conventional (i.e. having predominantly internal double bonds) polybutene or polyisobutene having Mn = 300 to 5000, more preferably 500 to 2500 and especially 700 to 2500. Such additives based on high reactivity polyisobutene, which can be prepared from the polyisobutene which may 5 comprise up to 20% by weight of n-butene units by hydroformylation and reductive amination with ammonia, monoamines or polyamines such as dimethylaminopropylamine, ethylenediamine, diethylenetriamine, triethylenetetramine or tetraethylenepentamine, are known especially from EP-A 244 616. When polybutene or polyisobutene having predominantly internal double bonds (usually in the I and y 10 positions) are used as starting materials in the preparation of the additives, a possible preparative route is by chlorination and subsequent amination or by oxidation of the double bond with air or ozone to give the carbonyl or carboxyl compound and subsequent amination under reductive (hydrogenating) conditions. The amines used here for the amination may be, for example, ammonia, monoamines or the 15 abovementioned polyamines. Corresponding additives based on polypropene are described in particular in WO-A 94/24231. Further preferred additives comprising monoamino groups (Da) are the hydrogenation products of the reaction products of polyisobutenes having an average degree of 20 polymerization P = 5 to 100 with nitrogen oxides or mixtures of nitrogen oxides and oxygen, as described in particular in WO-A 97/03946. Further preferred additives comprising monoamino groups (Da) are the compounds obtainable from polyisobutene epoxides by reaction with amines and subsequent 25 dehydration and reduction of the amino alcohols, as described in particular in DE-A 196 20262. Additives comprising nitro groups (Db), optionally in combination with hydroxyl groups, are preferably reaction products of polyisobutenes having an average degree of 30 polymerization P = 5 to 100 or 10 to 100 with nitrogen oxides or mixtures of nitrogen oxides and oxygen, as described in particular in WO-A 96/03367 and in WO-A 96/03479. These reaction products are generally mixtures of pure nitropolyisobutenes (e.g. a,p-dinitropolyisobutene) and mixed hydroxynitropolyisobutenes (e.g. a-nitro-P hydroxypolyisobutene). 35 Additives comprising hydroxyl groups in combination with mono- or polyamino groups (Dc) are in particular reaction products of polyisobutene epoxides obtainable from polyisobutene having preferably predominantly terminal double bonds and Mn = 300 to 5000, with ammonia or mono- or polyamines, as described in particular in EP-A 40 476 485. Additives comprising carboxyl groups or their alkali metal or alkaline earth metal salts (Dd) are preferably copolymers of C2- to C4o-olefins with maleic anhydride which have a 16 total molar mass of 500 to 20 000 and some or all of whose carboxyl groups have been converted to the alkali metal or alkaline earth metal salts and any remainder of the carboxyl groups has been reacted with alcohols or amines. Such additives are disclosed in particular by EP-A 307 815. Such additives serve mainly to prevent valve 5 seat wear and can, as described in WO-A 87/01126, advantageously be used in combination with customary fuel detergents such as poly(iso)buteneamines or polyetheramines, Additives comprising sulfonic acid groups or their alkali metal or alkaline earth metal 10 salts (De) are preferably alkali metal or alkaline earth metal salts of an alkyl sulfosuccinate, as described in particular in EP-A 639 632. Such additives serve mainly to prevent valve seat wear and can be used advantageously in combination with customary fuel detergents such as poly(iso)buteneamines or polyetheramines. 15 Additives comprising polyoxy-C2- to C4-alkylene moieties (Df) are preferably polyethers or polyetheramines which are obtainable by reaction of C2- to C 60 -alkanols, C6- to C30 alkanediols, mono- or di-C 2 - to Co-alkylamines, C- to Co-alkylcyclohexanols or C- to
C
3 0 -alkylphenols with I to 30 mol of ethylene oxide and/or propylene oxide and/or butylene oxide per hydroxyl group or amino group and, in the case of the 20 polyetheramines, by subsequent reductive amination with ammonia, monoamines or polyamines. Such products are described in particular in EP-A 310 875, EP-A 356 725, EP-A 700 985 and US-A 4 877 416. In the case of polyethers, such products also have carrier oil properties. Typical examples of these are tridecanol butoxylates, isotridecanol butoxylates, isononylphenol butoxylates and polyisobutenol butoxylates 25 and propoxylates and also the corresponding reaction products with ammonia. Additives comprising carboxylic ester groups (Dg) are preferably esters of mono-, di- or tricarboxylic acids with long-chain alkanols or polyols, in particular those having a minimum viscosity of 2 mm 2 /s at 100*C, as described in particular in DE-A 38 38 918. 30 The mono-, di- or tricarboxylic acids used may be aliphatic or aromatic acids, and particularly suitable ester alcohols or ester polyols are long-chain representatives having, for example, 6 to 24 carbon atoms. Typical representatives of the esters are adipates, phthalates, isophthalates, terephthalates and trimellitates of isooctanol, of isononanol, of isodecanol and of isotridecanol. Such products also have carrier oil 35 properties. Additives comprising moieties derived from succinic anhydride and having hydroxyl and/or amino and/or amido and/or especially imido groups (Dh) are preferably corresponding derivatives of alkyl- or alkenyl-substituted succinic anhydride and 40 especially the corresponding derivatives of polyisobutenylsuccinic anhydride which are obtainable by reacting conventional or high-reactivity polyisobutene having Mn = preferably 300 to 5000, more preferably 300 to 3000, even more preferably 500 to 2500, even more especially preferably 700 to 2500 and especially 800 to 1500, with 17 maleic anhydride by a thermal route in an ene reaction or via the chlorinated polyisobutene. The moieties having hydroxyl and/or amino and/or amido and/or imido groups are, for example, carboxylic acid groups, acid amides of monoamines, acid amides of di- or polyamines which, in addition to the amide function, also have free 5 amine groups, succinic acid derivatives having an acid and an amide function, carboximides with monoamines, carboximides with di- or polyamines which, in addition to the imide function, also have free amine groups, or diimides which are formed by the reaction of di- or polyamines with two succinic acid derivatives. In the presence of imido moieties D(h), the further detergent additive in the context of the present 10 invention is, however, used only up to a maximum of 100% of the weight of compounds with betaine structure. Such fuel additives are common knowledge and are described, for example, in documents (1) and (2). They are preferably the reaction products of alkyl- or alkenyl-substituted succinic acids or derivatives thereof with mines and more preferably the reaction products of polyisobutenyl-substituted succinic acids or 15 derivatives thereof with amines. Of particular interest in this context are reaction products with aliphatic polyamines (polyalkyleneimines) such as especially ethylenediamine, diethylenetriamine, triethylenetetramine, tetraethylenepentamine, pentaethylenehexamine and hexaethyleneheptamine, which have an imide structure. 20 Additives comprising moieties (Di) obtained by Mannich reaction of substituted phenols with aldehydes and mono- or polyamines are preferably reaction products of polyisobutene-substituted phenols with formaldehyde and mono- or polyamines such as ethylenediamine, diethylenetriamine, triethylenetetramine, tetraethylenepentamine or dimethylaminopropylamine. The polyisobutenyl-substituted phenols may stem from 25 conventional or high-reactivity polyisobutene having Mn = 300 to 5000. Such "polyisobutene Mannich bases" are described in particular in EP-A 831 141. One or more of the detergent additives mentioned can be added to the fuel in such an amount that the dosage of these detergent additives is preferably 25 to 2500 ppm by 30 weight, especially 75 to 1500 ppm by weight, in particular 150 to 1000 ppm by weight. Carrier oils additionally used may be of mineral or synthetic nature. Suitable mineral carrier oils are the fractions obtained in crude oil processing, such as brightstock or base oils having viscosities, for example, from the SN 500 to 2000 class; but also 35 aromatic hydrocarbons, paraffinic hydrocarbons and alkoxyalkanols. Likewise useful is a fraction which is obtained in the refining of mineral oil and is known as "hydrocrack oil" (vacuum distillate cut having a boiling range from about 360 to 500*C, obtainable from natural mineral oil which has been catalytically hydrogenated and isomerized under high pressure and also deparaffinized). Likewise suitable are mixtures of the 40 abovementioned mineral carrier oils. Examples of suitable synthetic carrier oils are polyolefins (polyalphaolefins or polyinternalolefins), (poly)esters, (poly)alkoxylates, polyethers, aliphatic polyether- 18 amines, alkylphenol-started polyethers, alkylphenol-started polyetheramines and carboxylic esters of long-chain alkanols. Examples of suitable polyolefins are olefin polymers having Mo = 400 to 1800, in 5 particular based on polybutene or polyisobutene (hydrogenated or unhydrogenated). Examples of suitable polyethers or polyetheramines are preferably compounds comprising polyoxy-C2- to C4-alkylene moieties which are obtainable by reacting C2- to
C
6 o-alkanols, C- to Co-alkanediols, mono- or di-C 2 - to C 30 -alkylamines, Ci- to C30 10 alkylcyclohexanols or C- to C3 0 -alkylphenols with 1 to 30 mol of ethylene oxide and/or propylene oxide and/or butylene oxide per hydroxyl group or amino group, and, in the case of the polyetheramines, by subsequent reductive amination with ammonia, monoamines or polyamines. Such products are described in particular in EP-A 310 875, EP-A 356 725, EP-A 700 985 and US-A 4,877,416. For example, the 15 polyetheramines used may be poly-C2- to C-alkylene oxide amines- or functional derivatives thereof. Typical examples thereof are tridecanol butoxylates or isotridecanol butoxylates, isononylphenol butoxylates and also polyisobutenol butoxylates and propoxylates, and also the corresponding reaction products with ammonia. 20 Examples of carboxylic esters of long-chain alkanols are in particular esters of mono-, di- or tricarboxylic acids with long-chain alkanols or polyols, as described in particular in DE-A 38 38 918. The mono-, di- or tricarboxylic acids used may be aliphatic or aromatic acids; suitable ester alcohols or polyols are in particular long-chain representatives having, for example, 6 to 24 carbon atoms. Typical representatives of 25 the esters are adipates, phthalates, isophthalates, terephthalates and trimellitates of isooctanol, isononanol, isodecanol and isotridecanol, for example di(n- or isotridecyl) phthalate. Further suitable carrier oil systems are described, for example, in DE-A 38 26 608, 30 DE-A 41 42 241, DE-A 43 09 074, EP-A 452 328 and EP-A 548 617. Examples of particularly suitable synthetic carrier oils are alcohol-started polyethers having about 5 to 35, preferably about 5 to 30, more preferably 10 to 30 and especially 15 to 30 C3- to C 6 -alkylene oxide units, for example selected from propylene oxide, n 35 butylene oxide and isobutylene oxide units, or mixtures thereof, per alcohol molecule. Nonlimiting examples of suitable starter alcohols are long-chain alkanols or phenols substituted by long-chain alkyl in which the long-chain alkyl radical is in particular a straight-chain or branched C6- to C 18 -alkyl radical. Preferred examples include tridecanol and nonylphenol. Particularly preferred alcohol-started polyethers are the 40 reaction products (polyetherification products) of monohydric aliphatic C6- to C18 alcohols with C3- to C-alkylene oxides. Examples of monohydric aliphatic C-C1 alcohols are hexanol, heptanol, octanol, 2-ethylhexanol, nonyl alcohol, decanol, 3 propylheptanol, undecanol, dodecanol, tridecanol, tetradecanol, pentadecanol, 19 hexadecanol, octadecanol and the constitutional and positional isomers thereof. The alcohols can be used either in the form of the pure isomers or in the form of technical grade mixtures. A particularly preferred alcohol is tridecanol. Examples of C3- to Ce alkylene oxides are propylene oxide, such as 1,2-propylene oxide, butylene oxide, such 5 as 1,2-butylene oxide, 2,3-butylene oxide, isobutylene oxide or tetrahydrofuran, pentylene oxide and hexylene oxide. Particular preference among these is given to C3 to C4-alkylene oxides, i.e. propylene oxide such as 1,2-propylene oxide and butylene oxide such as 1,2-butylene oxide, 2,3-butylene oxide and isobutylene oxide. Especially butylene oxide is used. 10 Further suitable synthetic carrier oils are alkoxylated alkylphenols, as described in DE-A 10 102 913. Preferred carrier oils are synthetic carrier oils, particular preference being given to the 15 above-described alcohol-started polyethers. The carrier oil or the mixture of different carrier oils is added to the fuel in an amount of preferably 1 to 1000 ppm by weight, more preferably of 10 to 500 ppm by weight and especially of 20 to 100 ppm by weight. 20 It is also possible for the fuel to comprise further customary additives and coadditives in the amounts customary therefor. In the case of middle distillate fuels, especially diesel fuels, these are in particular cold flow improvers, lubricity improvers, corrosion inhibitors, demulsifiers, dehazers, antifoams, cetane number improvers, combustion 25 improvers, antioxidants or stabilizers, antistats, metallocenes, metal deactivators, dyes and/or solvents. In the case of gasoline fuels, these are in particular friction modifiers, corrosion inhibitors, demulsifiers, dehazers, antifoams, combustion improvers, antioxidants or stabilizers, antistats, metallocenes, metal deactivators, dyes and/or solvents. 30 Suitable cold flow improvers are in principle all organic compounds which are capable of improving the flow performance of middle distillate fuels or diesel fuels under cold conditions. For the intended purpose, they must have sufficient oil solubility. In particular, useful cold flow improvers for this purpose are the cold flow improvers 35 (middle distillate flow improvers, MDFIs) typically used in the case of middle distillates of fossil origin, i.e. in the case of customary mineral diesel fuels. However, it is also possible to use organic compounds which partly or predominantly have the properties of a wax antisettling additive (WASA) when used in customary diesel fuels. They can also act partly or predominantly as nucleators. It is, though, also possible to use 40 mixtures of organic compounds effective as MDFIs and/or effective as WASAs and/or effective as nucleators.
20 The cold flow improver is typically selected from (KI) copolymers of a C2- to C 40 -olefin with at least one further ethylenically unsaturated monomer; 5 (K2) comb polymers; (K3) polyoxyalkylenes; (K4) polar nitrogen compounds; (K5) sulfocarboxylic acids or sulfonic acids or derivatives thereof; and (K6) poly(meth)acrylic esters. 10 It is possible to use either mixtures of different representatives from one of the particular classes (K1) to (K6) or mixtures of representatives from different classes (KI) to (K6). 15 Suitable C2- to C40-olefin monomers for the copolymers of class (K1) are, for example, those having 2 to 20 and especially 2 to 10 carbon atoms, and 1 to 3 and preferably 1 or 2 carbon-carbon double bonds, especially having one carbon-carbon double bond. In the latter case, the carbon-carbon double bond may be arranged either terminally (a olefins) or internally. However, preference is given to a-olefins, more preferably a 20 olefins having 2 to 6 carbon atoms, for example propene, 1-butene, 1-pentene, 1 hexene and in particular ethylene. In the copolymers of class (K1), the at least one further ethylenically unsaturated monomer is preferably selected from alkenyl carboxylates, (meth)acrylic esters and 25 further olefins. When further olefins are also copolymerized, they are preferably higher in molecular weight than the abovementioned C2- to C4 0 -olefin base monomer. When, for example, the olefin base monomer used is ethylene or propene, suitable further olefins are in 30 particular Cio- to C40--olefins. Further olefins are in most cases only additionally copolymerized when monomers with carboxylic ester functions are also used. Suitable (meth)acrylic esters are, for example, esters of (meth)acrylic acid with C1- to
C
20 -alkanols, especially C1- to C1o-alkanols, in particular with methanol, ethanol, 35 propanol, isopropanol, n-butanol, sec-butanol, isobutanol, tert-butano, pentanol, hexanol, heptanol, octanol, 2-ethylhexanol, nonanol and decanol, and structural isomers thereof. Suitable alkenyl carboxylates are, for example, C2- to C 1 4 -alkenyl esters, for example 40 the vinyl and propenyl esters, of carboxylic acids having 2 to 21 carbon atoms, whose hydrocarbon radical may be linear or branched. Among these, preference is given to the vinyl esters. Among the carboxylic acids with a branched hydrocarbon radical, preference is given to those whose branch is in the a-position to the carboxyl group, 21 the a-carbon atom more preferably being tertiary, i.e. the carboxylic acid being a so called neocarboxylic acid. However, the hydrocarbon radical of the carboxylic acid is preferably linear. 5 Examples of suitable alkenyl carboxylates are vinyl acetate, vinyl propionate, vinyl butyrate, vinyl 2-ethylhexanoate, vinyl neopentanoate, vinyl hexanoate, vinyl neononanoate, vinyl neodecanoate and the corresponding propenyl esters, preference being given to the vinyl esters. A particularly preferred alkenyl carboxylate is vinyl acetate; typical copolymers of group (K1) resulting therefrom are ethylene-vinyl acetate 10 copolymers ("EVAs"), which are some of the most frequently used. Ethylene-vinyl acetate copolymers usable particularly advantageously and their preparation are described in WO 99/29748. Suitable copolymers of class (KI) are also those which comprise two or more different 15 alkenyl carboxylates in copolymerized form, which differ in the alkenyl function and/or in the carboxylic acid group. Likewise suitable are copolymers which, as well as the alkenyl carboxylate(s), comprise at least one olefin and/or at least one (meth)acrylic ester in copolymerized form. 20 Terpolymers of a C2- to C 4 0-a-olefin, a Ci- to C20-alkyl ester of an ethylenically unsaturated monocarboxylic acid having 3 to 15 carbon atoms and a C2- to C14-alkenyl ester of a saturated monocarboxylic acid having 2 to 21 carbon atoms are also suitable as copolymers of class (KI). Terpolymers of this kind are described in WO 2005/054314. A typical terpolymer of this kind is formed from ethylene, 2-ethyihexyl 25 acrylate and vinyl acetate. The at least one or the further ethylenically unsaturated monomer(s) are copolymerized into the copolymers of class (K1) in an amount of preferably 1 to 50% by weight, especially 10 to 45% by weight and in particular 20 to 40% by weight, based on the 30 overall copolymer. The main proportion in terms of weight of the monomer units in the copolymers of class (K1) therefore originates generally from the C2 to C40 base olefins. The copolymers of class (KI) preferably have a number-average molecular weight M, of 1000 to 20 000, more preferably 1000 to 10 000 and in particular 1000 to 8000. 35 Typical comb polymers of component (K2) are, for example, obtainable by the copolymerization of maleic anhydride or fumaric acid with another ethylenically unsaturated monomer, for example with an ct-olefin or an unsaturated ester, such as vinyl acetate, and subsequent esterification of the anhydride or acid function with an 40 alcohol having at least 10 carbon atoms. Further suitable comb polymers are copolymers of a-olefins and esterified comonomers, for example esterified copolymers of styrene and maleic anhydride or esterified copolymers of styrene and fumaric acid. Suitable comb polymers may also be polyfumarates or polymaleates. Homo- and 22 copolymers of vinyl ethers are also suitable comb polymers. Comb polymers suitable as components of class (K2) are, for example, also those described in WO 2004/035715 and in "Comb-Like Polymers. Structure and Properties", N. A. Plat6 and V. P. Shibaev, J. Poly. Sci. Macromolecular Revs. 8, pages 117 to 253 (1974)". 5 Mixtures of comb polymers are also suitable. Polyoxyalkylenes suitable as components of class (K3) are, for example, polyoxyalkylene esters, polyoxyalkylene ethers, mixed polyoxyalkylene ester/ethers and mixtures thereof. These polyoxyalkylene compounds preferably comprise at least 10 one linear alkyl group, preferably at least two linear alkyl groups, each having 10 to 30 carbon atoms and a polyoxyalkylene group having a number-average molecular weight of up to 5000. Such polyoxyalkylene compounds are described, for example, in EP-A 061 895 and also in US 4,491,455. Preferred polyoxyalkylene compounds are based on polyethylene glycols and polypropylene glycols having a number-average molecular 15 weight of 100 to 5000. Additionally suitable are polyoxyalkylene mono- and diesters of fatty acids having 10 to 30 carbon atoms, such as stearic acid or behenic acid. Polar nitrogen compounds suitable as components of class (K4) may be either ionic or nonionic and preferably have at least one substituent, in particular at least two 20 substituents, in the form of a tertiary nitrogen atom of the general formula >NR 7 in which R T is a CB- to C4 0 -hydrocarbon radical. The nitrogen substituents may also be quaternized, i.e. be in cationic form. An example of such nitrogen compounds is that of ammonium salts and/or amides which are obtainable by the reaction of at least one amine substituted by at least one hydrocarbon radical with a carboxylic acid having 1 to 25 4 carboxyl groups or with a suitable derivative thereof. The amines preferably comprise at least one linear C 8 - to C40-alkyl radical. Primary amines suitable for preparing the polar nitrogen compounds mentioned are, for example, octylamine, nonylamine, decylamine, undecylamine, dodecylamine, tetradecylamine and the higher linear homologs. Secondary amines suitable for this purpose are, for example, 30 dioctadecylamine and methylbehenylamine. Also suitable for this purpose are amine mixtures, in particular amine mixtures obtainable on the industrial scale, such as fatty amines or hydrogenated tallamines, as described, for example, in Ullmann's Encyclopedia of Industrial Chemistry, 6th Edition, "Amines, aliphatic" chapter. Acids suitable for the reaction are, for example, cyclohexane-1,2-dicarboxylic acid, 35 cyclohexene-1,2-dicarboxylic acid, cyclopentane-1,2-dicarboxylic acid, naphthalenedicarboxylic acid, phthalic acid, isophthalic acid, terephthalic acid, and succinic acids substituted by long-chain hydrocarbon radicals. In particular, the component of class (K4) is an oil-soluble reaction product of poly(C 2 40 to C20-carboxylic acids) having at least one tertiary amino group with primary or secondary amines. The poly(C 2 - to C 20 -carboxylic acids) which have at least one tertiary amino group and form the basis of this reaction product comprise preferably at least 3 carboxyl groups, especially 3 to 12 and in particular 3 to 5 carboxyl groups. The 23 carboxylic acid units in the polycarboxylic acids have preferably 2 to 10 carbon atoms, and are especially acetic acid units. The carboxylic acid units are suitably bonded to the polycarboxylic acids, usually via one or more carbon and/or nitrogen atoms. They are preferably attached to tertiary nitrogen atoms which, in the case of a plurality of 5 nitrogen atoms, are bonded via hydrocarbon chains. The component of class (K4) is preferably an oil-soluble reaction product based on poly(C2- to C20-carboxylic acids) which have at least one tertiary amino group and are of the general formula la or lIb 10 HOOCB B'COOH HOOCB 'A 'N BCOOH B A B(lla) HOOC B'N B'COOH 'COOH (lib) 15 in which the variable A is a straight-chain or branched C2- to C 6 -alkylene group or the moiety of the formula Ill HOOC'B N'CH2-CH 2 CH 2
-CH
2 20 and the variable B is a C- to C19-alkylene group. The compounds of the general formulae Ila and lIb especially have the properties of a WASA. Moreover, the preferred oil-soluble reaction product of component (K4), especially that of the general formula Ila or llb, is an amide, an amide-ammonium salt or an 25 ammonium salt in which no, one or more carboxylic acid groups have been converted to amide groups. Straight-chain or branched C2- to Ce-alkylene groups of the variable A are, for example, 1,1-ethylene, 1,2-propylene, 1,3-propylene, 1,2-butylene, 1,3-butylene, 1,4-butylene, 30 2-methyl-1,3-propylene, 1,5-pentylene, 2-methyl-1,4-butylene, 2,2-dimethyl-1,3 propylene, 1,6-hexylene (hexamethylene) and in particular 1,2-ethylene. The variable A comprises preferably 2 to 4 and especially 2 or 3 carbon atoms. C- to Cig-alkylene groups of the variable B are, for example, 1,2-ethylene, 35 1,3-propylene, 1,4-butylene, hexamethylene, octamethylene, decamethylene, dodecamethylene, tetradecamethylene, hexadecamethylene, octadecam ethylene, 24 nonadecamethylene and especially methylene. The variable B comprises preferably 1 to 10 and especially I to 4 carbon atoms. The primary and secondary amines as a reaction partner for the polycarboxylic acids to 5 form component (K4) are typically monoamines, especially aliphatic monoamines. These primary and secondary amines may be selected from a multitude of amines which bear hydrocarbon radicals which are optionally bonded to one another if appropriate. 10 These parent amines of the oil-soluble reaction products of component (K4) are usually secondary amines and have the general formula HN(R 8
)
2 in which the two variables Ra are each independently straight-chain or branched CO- to C3o-alkyl radicals, especially C4- to C2 4 -alkyl radicals. These relatively long-chain alkyl radicals are preferably straight-chain or only slightly branched. In general, the secondary amines mentioned, 15 with regard to their relatively long-chain alkyl radicals, derive from naturally occurring fatty acid and from derivatives thereof. The two R3 radicals are preferably identical. The secondary amines mentioned may be bonded to the polycarboxylic acids by means of amide structures or in the form of the ammonium salts; it is also possible for 20 only a portion to be present as amide structures and another portion as ammonium salts. Preferably only few, if any, free acid groups are present. The oil-soluble reaction products of component (K4) are preferably present completely in the form of the amide structures. 25 Typical examples of such components (K4) are reaction products of nitrilotriacetic acid, of ethylenediaminetetraacetic acid or of propylene-1,2-diaminetetraacetic acid with in each case 0.5 to 1.5 mol per carboxyl group, especially 0.8 to 1.2 mol per carboxyl group, of dioleylamine, dipalmitinamine, dicoconut fatty amine, distearylamine, dibehenylamine or especially ditallow fatty amine. A particularly preferred component 30 (K4) is the reaction product of I mol of ethylenediaminetetraacetic acid and 4 mol of hydrogenated ditallow fatty amine. Further typical examples of component (K4) include the N,N-dialkylammonium salts of 2-N',N'-dialkylamidobenzoates, for example the reaction product of 1 mol of phthalic 35 anhydride and 2 mol of ditallow fatty amine, the latter being hydrogenated or unhydrogenated, and the reaction product of 1 mol of an alkenylspirobislactone with 2 mol of a dialkylamine, for example ditallow fatty amine and/or tallow fatty amine, the last two being hydrogenated or unhydrogenated. 40 Further typical structure types for the component of class (K4) are cyclic compounds with tertiary amino groups or condensates of long-chain primary or secondary amines with carboxylic acid-containing polymers, as described in WO 93/18115.
25 Sulfocarboxylic acids, sulfonic acids or derivatives thereof which are suitable as cold flow improvers of class (K5) are, for example, the oil-soluble carboxamides and carboxylic esters of ortho-sulfobenzoic acid, in which the sulfonic acid function is present as a sulfonate with alkyl-substituted ammonium cations, as described in 5 EP-A 261 957. Poly(meth)acrylic esters suitable as cold flow improvers of class (K6) are either homo or copolymers of acrylic and methacrylic esters. Preference is given to copolymers of at least two different (meth)acrylic esters which differ with regard to the esterified alcohol. 10 Optionally, the copolymer comprises another different olefinically unsaturated monomer in copolymerized form. The weight-average molecular weight of the polymer is preferably 50 000 to 500 000. A particularly preferred polymer is a copolymer of methacrylic acid and methacrylic esters of saturated C14 and C15 alcohols, the acid groups having been neutralized with hydrogenated tallamine. Suitable 15 poly(meth)acrylic esters are described, for example, in WO 00/44857. The cold flow improver or the mixture of different cold flow improvers is added to the middle distillate fuel or diesel fuel in a total amount of preferably 10 to 5000 ppm by weight, more preferably of 20 to 2000 ppm by weight, even more preferably of 50 to 20 1000 ppm by weight and especially of 100 to 700 ppm by weight, for example of 200 to 500 ppm by weight. Suitable lubricity improvers or friction modifiers are based typically on fatty acids or fatty acid esters. Typical examples are tall oil fatty acid, as described, for example, in 25 WO 98/004656, and glyceryl monooleate. The reaction products, described in US 6 743 266 B2, of natural or synthetic oils, for example triglycerides, and alkanolamines are also suitable as such lubricity improvers. Suitable corrosion inhibitors are, for example, succinic esters, in particular with polyols, 30 fatty acid derivatives, for example oleic esters, oligomerized fatty acids, substituted ethanolamines, and products sold under the trade name RC 4801 (Rhein Chemie Mannheim, Germany) or HiTEC 536 (Ethyl Corporation). Suitable demulsifiers are, for example, the alkali metal or alkaline earth metal salts of 35 alkyl-substituted phenol- and naphthalenesulfonates and the alkali metal or alkaline earth metal salts of fatty acids, and also neutral compounds such as alcohol alkoxylates, e.g. alcohol ethoxylates, phenol alkoxylates, e.g. tert-butylphenol ethoxylate or tert-pentylphenol ethoxylate, fatty acids, alkylphenols, condensation products of ethylene oxide (EO) and propylene oxide (PO), for example including in the 40 form of EO/PO block copolymers, polyethyleneimines or else polysiloxanes.
26 Suitable dehazers are, for example, alkoxylated phenol-formaldehyde condensates, for example the products available under the trade names NALCO 7D07 (Nalco) and TOLAD 2683 (Petrolite). 5 Suitable antifoams are, for example, polyether-modified polysiloxanes, for example the products available under the trade names TEGOPREN 5851 (Goldschmidt), Q 25907 (Dow Corning) and RHODOSIL (Rhone Poulenc). Suitable cetane number improvers are, for example, aliphatic nitrates such as 10 2-ethylhexyl nitrate and cyclohexyl nitrate and peroxides such as di-tert-butyl peroxide. Suitable antioxidants are, for example substituted phenols, such as 2,6-di-tert butylphenol and 6-di-tert-butyl-3-methylphenol, and also phenylenediamines such as N,N'-di-sec-butyl-p-phenylenediamine. 15 Suitable metal deactivators are, for example, salicylic acid derivatives such as N,N'-disalicylidene-1,2-propanediamine. Suitable solvents are, for example, nonpolar organic solvents such as aromatic and 20 aliphatic hydrocarbons, for example toluene, xylenes, white spirit and products sold under the trade names SHELLSOL (Royal DUtch/Shell Group) and EXXSOL (ExxonMobil), and also polar organic solvents, for example, alcohols such as 2-ethylhexanol, decanol and isotridecanol. Such solvents are usually added to the diesel fuel together with the aforementioned additives and coadditives, which they are 25 intended to dissolve or dilute for better handling. Middle distillate fuels such as diesel fuels or heating oils are preferably mineral oil raffinates which typically have a boiling range from 100 to 400*C. These are usually distillates having a 95% point up to 360"C or even higher. These may also be so-called 30 "ultra low sulfur diesel" or "city diesel", characterized by a 95% point of, for example, not more than 3450C and a sulfur content of not more than 0.005% by weight or by a 95% point of, for example, 285"C and a sulfur content of not more than 0.001% by weight. In addition to the mineral middle distillate fuels or diesel fuels obtainable by refining, those obtainable by coal gasification or gas liquefaction ["gas to liquid" (GTL) 35 fuels] or by biomass liquefaction ["biomass to liquid" (BTL) fuels] are also suitable. Also suitable are mixtures of the aforementioned middle distillate fuels or diesel fuels with renewable fuels, such as biodiesel or bioethanol. The qualities of the heating oils and diesel fuels are laid down in detail, for example, in 40 DIN 51603 and EN 590 (cf. also Ullmann's Encyclopedia of Industrial Chemistry, 5th edition, Volume A12, p. 617 ff.).
27 in addition to the use thereof in the abovementioned middle distillate fuels of fossil, vegetable or animal origin, which are essentially hydrocarbon mixtures, the inventive quaternized copolymer can also be used in mixtures of such middle distillates with biofuel oils (biodiesel). Such mixtures are also encompassed by the term "middle 5 distillate fuel" in the context of the present invention. They are commercially available and usually comprise the biofuel oils in minor amounts, typically in amounts of 1 to 30% by weight, especially of 3 to 10% by weight, based on the total amount of middle distillate of fossil, vegetable or animal origin and biofuel oil. 10 Biofuel oils are generally based on fatty acid esters, preferably essentially on alkyl esters of fatty acids which derive from vegetable and/or animal oils and/or fats. Alkyl esters are typically understood to mean lower alkyl esters, especially Cr1C4-alkyl esters, which are obtainable by transesterifying the glycerides which occur in vegetable and/or animal oils and/or fats, especially triglycerides, by means of lower alcohols, for 15 example ethanol or in particular methanol ("FAME"). Typical lower alkyl esters based on vegetable and/or animal oils and/or fats, which find use as a biofuel oil or component thereof, are, for example, sunflower methyl ester, palm oil methyl ester ("PME"), soya oil methyl ester ("SME") and especially rapeseed oil methyl ester ("RME"). 20 The middle distillate fuels or diesel fuels are more preferably those having a low sulfur content, i.e. having a sulfur content of less than 0.05% by weight, preferably of less than 0.02% by weight, more particularly of less than 0.005% by weight and especially of less than 0.001 % by weight of sulfur. 25 Useful gasoline fuels include all commercial gasoline fuel compositions. One typical representative which shall be mentioned here is the Eurosuper base fuel to EN 228, which is customary on the market. In addition, gasoline fuel compositions of the specification according to WO 00/47698 are also possible fields of use for the present 30 invention. The inventive quaternized copolymer is especially suitable as a fuel additive in fuel compositions, especially in diesel fuels, for overcoming the problems outlined at the outset in direct-injection diesel engines, in particular in those with common-rail injection 35 systems. The present invention thus also provides for the use of the inventive quaternized copolymer as a fuel additive for reducing or preventing deposits in the injection systems, especially in the injectors, or direct-injection diesel engines, especially in 40 common-rail injection systems. In addition, the present invention therefore also provides for the use of the inventive quaternized copolymer as a fuel additive for reducing the fuel consumption of direct- 28 injection diesel engines, especially of diesel engines with common-rail injection systems, In addition, the present invention therefore also provides for the use of the inventive 5 quaternized copolymer as a fuel additive for minimizing power loss in direct-injection diesel engines, especially in diesel engines with common-rail injection systems. The examples which follow those to illustrate the invention without restricting it. 10 Preparation example Example 1a: Preparation of a C20-2o4-olefin-1-maleic anhydride copolymer The copolymer was prepared by free-radical solution polymerization according to the 15 teaching of EP-A 307 815. To this end, the C20-2 4 -olefin-1 (400 g, corresponding to 1.35 mol) was melted at 80"C and dissolved in Soivesso 150 (400 g) at 150"C. Subsequently, di-tert-butyl peroxide (5.4 g, 0.037 mol), dissolved in Solvesso 150 (30 g), and the liquid maleic anhydride (132 g, 1.35 mol) heated in a dropping funnel heated to 70*C, were simultaneously added dropwise to the olefin solution in Solvesso 20 150 heated to 150*C over the course of 5 hours. The copolymer obtained possessed a hydrolysis number (HN) of 107.4 mg KOH/g, a number-average molecular weight (Mn) of 1470 g/mol, a weight-average molecular weight (Mw) of 3290 g/mol and a polydispersity (PDI) of 2.2. 25 Example 1b: Imidation of the C 20 -2 4 -olefin-1-maleic anhydride copolymer The copolymer prepared in example 1a was reacted with 3-(N,N-dimethylamino) propylamine in a molar ratio of the carboxylic anhydride functions in the copolymer to the amine of 1:1 to give the corresponding imidated copolymer with repeat N-(3 30 dimethylaminopropyl)succinamide units. For this purpose, the C 20 -2 4 -olefin-1 -maleic anhydride copolymer dissolved in Solvesso 150 was reacted with the abovementioned amine at 25*C in an addition reaction. The resulting amide precipitated out of the reaction mixture after a short time. The imidation was effected at 170*C and a pressure of I mbar within 2 hours. 35 Example 1c: Quaternization of the imidated copolymer with propylene oxide The imidated copolymer from example I b was reacted with propylene oxide in an equimolar ratio to the tertiary nitrogen atom in the oligoamine radical, in the presence 40 of an equimolar amount of acetic acid. This was done by dissolving the imidated copolymer in Soivesso 150 in an autoclave, admixing with the acetic acid and heating to 1300C. Nitrogen was used to set an initial pressure of 5 bar, then the propylene oxide was metered in over the course of 20 minutes, and the mixture was stirred at 29 130"C for a further 6 hours. The quaternized copolymer was obtained in quantitative yield in the form of a dark-colored solution. Use example 5 Example 2: Measurement of power losses in a direct-injection diesel engine To study the influence of the inventive quaternized terpolymer on the performance of direct-injection diesel engines, the power loss was determined on the basis of the 10 official test method CEC F-98-08. The power loss (or the power increase in the case of negative values) is a direct measure of formation or elimination of deposits in the injectors. A standard direct-injection diesel engine with a common-rail system was used. 15 The fuel used was a commercial diesel fuel from Haltermann (RF-06-03). To artificially induce the formation of deposits at the injectors, 1 ppm by weight of zinc didodecanoate was added thereto. The table which follows shows the results of the power loss determinations at 4000 rpm 20 after 10 minutes and 1 hour, and the quaternized copolymer was used in the form of the solution obtained in example 1c: Test run No. Fuel additive Dosage Power loss Power loss [ppm by weight 10 minutes 1 hour 25 of active substance] Blank none - 3.59 % 1.83 % with quaternized CP from ex. 1c 100 0.59% -1.50% 30 with quaternized CP from ex. Ic 200 -1.76% -1.13%

Claims (13)

1. A quaternized copolymer obtainable by the reaction steps of (A) copolymerization of one or more straight-chain, branched or cyclic, 5 ethylenically unsaturated C2 to Cioo hydrocarbons (monomer M1), which may bear one or more oxygen- or nitrogen-functional substituents which cannot be reacted with amines to give amides or imides or with alcohols to give esters, with one or more ethylenically unsaturated C3- to C12-carboxylic acids or Cs- to C 12 -carboxylic acid derivatives (monomer M2), which bear 10 one or two carboxylic acid functions and can be reacted with amines to give amides or imides or with alcohols to give esters, to give a copolymer (CP) with a number-average molecular weight M, of 500 to 20 000; (B) partial or full amidation or imidation or esterification of the carboxylic acid 15 functions of the (M2) units in the copolymer (CP) by reacting them with one or more oligoamines (OA) having 2 to 6 nitrogen atoms or alcoholamines (AA), each of which comprises at least one primary or secondary nitrogen atom or at least one hydroxyl group and at least one quaternizable tertiary nitrogen atom; 20 (C) partial or full quaternization of the at least one tertiary nitrogen atom in the OA or AA units with at least one quaternizing agent (QM); where the sequence of steps (B) and (C) may also be reversed, such that the par 25 tial or full amidation or imidation of esterification of the carboxylic acid functions of the (M2) units in the copolymer (CP) can be effected by reacting with the oligoamines (OA) or alcoholamines (AA) already quaternized in reaction step (C).
2. A quaternized copolymer according to claim 1, obtainable by reaction steps (A), (B) 30 and (C), wherein the monomers (M1) in reaction step (A) are selected from C2- to C40-alkenes, C3- to Cio-cycloolefins, alkyl vinyl ethers having 1 to 30 carbon atoms in the alkyl group, cycloalkyl vinyl ethers having 3 to 10 carbon atoms in the cycloalkyl group and oligo- or polyisobutenes having 8 to 96 carbon atoms. 35
3. A quaternized copolymer according to claim 1 or 2, obtainable by reaction steps (A), (B) and (C), wherein the monomers (M1) in reaction step (A) bear the polymerizable ethylenically unsaturated double bond in the a position.
4. A quaternized copolymer according to claims I to 3, obtainable by reaction steps 40 (A), (B) and (C), wherein the monomers (M2) in reaction step (A) are selected from acrylic acid, methacrylic acid, maleic acid, fumaric acid and itaconic acid, and the anhydrides, halides and esters thereof. 31
5. A quaternized copolymer according to claims 1 to 4, obtainable by reaction steps (A), (B) and (C), wherein the monomer units (Ml) and (M2) are present in a weight ratio of 30:70 to 70:30 in the copolymer (CP) of reaction step (A). 5
6. A quaternized copolymer according to claims 1 to 5, obtainable by reaction steps (A), (B) and (C), wherein the oligoamines (OA) used in reaction step (B) are com pounds of the general formula (la) R'R 2 N-(CH 2 )n-NR 3 R4 (la) 10 in which the variables R' and R 2 are each hydrogen or C- to C 2 0 -alkyl groups, where at least one of the variables R' and R 2 is hydrogen, 15 the variables R 3 and R 4 each independently denote C- to C 2 0 -alkyl groups or, to gether with the nitrogen atom to which they are bonded, form a saturated, partly unsaturated or unsaturated five-membered or six-membered heterocyclic ring, and 20 the variable n is from 1 to 12, especially from 2 to 6, in particular 2 or 3.
7. A quaternized copolymer according to claims 1 to 5, obtainable by reaction steps (A), (B) and (C), wherein the alcoholamines (AA) used in reaction step (B) are 25 compounds of the general formula (Ib) [HO-(CH2)m]xN(R 5 )y(R 6 )z (Ib) in which 30 the variables R 5 and R 6 each independently denote C- to C20-alkyl groups or, in the case that y = z = 1, together with the nitrogen atom to which they are bonded, form a saturated, partly unsaturated or unsaturated five-membered or six-membered heterocyclic ring, 35 the variable m is from 1 to 12, especially from 2 to 6, in particular 2 or 3, and the variables x, y and z are each 0, 1, 2 or 3, where the sum of x + y + z must give the value of 3. 40
8. A quaternized copolymer according to claims 1 to 7, obtainable by reaction steps (A), (B) and (C), wherein the quaternization of reaction step C is effected with at least one quaternizing agent (QM) selected from epoxides, dialkyl sulfates, 32 dialkyl sulfites, alkyl halides, arylalkyl halides, alkyl carboxylates and dialkyl car bonates.
9. A process for preparing a quaternized copolymer, which comprises performing 5 the following reaction steps: (A) copolymerization of one or more straight-chain, branched or cyclic, ethylenically unsaturated C 2 to Cioo hydrocarbons (monomer M1), which may bear one or more oxygen- or nitrogen-functional substituents which cannot be reacted with 10 amines to give amides or imides or with alcohols to give esters, with one or more ethylenically unsaturated C 3 - to C1 2 -carboxylic acids or C 3 - to C12-carboxylic acid derivatives (monomer M2), which bear one or two carboxylic acid functions and can be reacted with amines to give amides or imides or with alcohols to give es ters, to give a copolymer (CP) with a number-average molecular weight Mn of 500 15 to 20 000; (B) partial or full amidation or imidation or esterification of the carboxylic acid func tions of the (M2) units in the copolymer (CP) by reacting them with one or more oligoamines (OA) having 2 to 6 nitrogen atoms or alcoholamines (AA), each of 20 which comprises at least one primary or secondary nitrogen atom or at least one hydroxyl group and at least one quaternizable tertiary nitrogen atom; (C) partial or full quaternization of the at least one tertiary nitrogen atom in the OA or AA units with at least one quaternizing agent (QM); 25 where the sequence of steps (B) and (C) may also be reversed, such that the partial or full amidation or imidation of esterification of the carboxylic acid func tions of the (M2) units in the copolymer (CP) can be effected by reacting with the oligoamines (OA) or alcoholamines (AA) already quaternized in reaction step (C). 30
10. A fuel comprising 10 to 5000 ppm by weight of a quaternized copolymer ac cording to claims 1 to 8.
11. The use of a quaternized copolymer according to claims 1 to 8 as a fuel additive 35 for reducing or preventing deposits in the injection systems of direct-injection diesel engines, especially in common-rail injection systems.
12. The use of a quaternized copolymer according to claims 1 to 8 as a fuel additive for reducing the fuel consumption of direct-injection diesel engines, especially of 40 diesel engines with common-rail injection systems. 33
13. The use of a quaternized copolymer according to claims I to 8 as a fuel additive for minimizing power loss in direct-injection diesel engines, especially in diesel engines with common-rail injection systems.
AU2011269024A 2010-06-25 2011-06-22 Quaternized copolymer Abandoned AU2011269024A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
EP10167372 2010-06-25
EP10167372.1 2010-06-25
PCT/EP2011/060429 WO2011161149A1 (en) 2010-06-25 2011-06-22 Quaternized copolymer

Publications (1)

Publication Number Publication Date
AU2011269024A1 true AU2011269024A1 (en) 2013-01-10

Family

ID=44627379

Family Applications (1)

Application Number Title Priority Date Filing Date
AU2011269024A Abandoned AU2011269024A1 (en) 2010-06-25 2011-06-22 Quaternized copolymer

Country Status (11)

Country Link
EP (1) EP2585498B1 (en)
JP (1) JP2013531097A (en)
KR (1) KR20130038909A (en)
CN (1) CN102958949A (en)
AU (1) AU2011269024A1 (en)
BR (1) BR112012032534A2 (en)
CA (1) CA2803207A1 (en)
ES (1) ES2680571T3 (en)
MX (1) MX2012014797A (en)
PL (1) PL2585498T3 (en)
WO (1) WO2011161149A1 (en)

Families Citing this family (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9006158B2 (en) 2010-12-09 2015-04-14 Basf Se Polytetrahydrobenzoxazines and bistetrahydrobenzoxazines and use thereof as a fuel additive or lubricant additive
US9222046B2 (en) * 2013-04-26 2015-12-29 Afton Chemical Corporation Alkoxylated quaternary ammonium salts and diesel fuels containing the salts
DE102013217662A1 (en) * 2013-09-04 2015-03-05 Leibniz-Institut Für Polymerforschung Dresden E.V. POLYMERS WITH IONIC AND REACTIVE GROUPING, METHOD FOR THEIR PREPARATION AND USE
PL3483234T3 (en) 2013-09-20 2021-12-13 Basf Se Use of specialised derivatives of quaternised nitrogen compounds as additives in fuels
EP3099720B1 (en) * 2014-01-29 2018-07-04 Basf Se Use of polycarboxylic-acid-based additives for fuels
CN106459811B (en) * 2014-01-29 2020-02-18 巴斯夫欧洲公司 Corrosion inhibitors for fuels and lubricants
US11085001B2 (en) 2015-07-16 2021-08-10 Basf Se Copolymers as additives for fuels and lubricants
SG11201800399TA (en) * 2015-07-16 2018-02-27 Basf Se Corrosion inhibitors for fuels and lubricants
FR3041349B1 (en) 2015-09-18 2020-01-24 Total Marketing Services COPOLYMER FOR USE AS A FUEL DETERGENT ADDITIVE
FR3041362B1 (en) * 2015-09-18 2017-10-13 Total Marketing Services DETERGENT ADDITIVE FOR FUEL
US11078418B2 (en) 2016-07-05 2021-08-03 Basf Se Corrosion inhibitors for fuels and lubricants
EP3555244B1 (en) 2016-12-15 2023-05-31 Basf Se Polymers as diesel fuel additives for direct injection diesel engines
WO2018188986A1 (en) 2017-04-13 2018-10-18 Basf Se Polymers as additives for fuels and lubricants
EP3990585A1 (en) 2019-06-26 2022-05-04 Basf Se New additive packages for gasoline fuels

Family Cites Families (39)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4464182A (en) 1981-03-31 1984-08-07 Exxon Research & Engineering Co. Glycol ester flow improver additive for distillate fuels
JPS58138791A (en) 1982-02-10 1983-08-17 Nippon Oil & Fats Co Ltd Fluidity improver for fuel oil
US4690687A (en) 1985-08-16 1987-09-01 The Lubrizol Corporation Fuel products comprising a lead scavenger
DE3611230A1 (en) 1986-04-04 1987-10-08 Basf Ag POLYBUTYL AND POLYISOBUTYLAMINE, METHOD FOR THE PRODUCTION THEREOF AND THE FUEL AND LUBRICANT COMPOSITIONS CONTAINING THE SAME
DE3615855A1 (en) * 1986-05-10 1987-11-12 Akzo Gmbh PAPER SIZING AGENTS, THEIR PRODUCTION AND THEIR USE
IN184481B (en) 1986-09-24 2000-08-26 Exxon Chemical Patents Inc
ATE74620T1 (en) 1987-09-15 1992-04-15 Basf Ag FUELS FOR GASOLINE ENGINES.
DE3732908A1 (en) 1987-09-30 1989-04-13 Basf Ag FUELS CONTAINING POLYETHERAMINE FOR OTTO ENGINES
US4877416A (en) 1987-11-18 1989-10-31 Chevron Research Company Synergistic fuel compositions
DE3826608A1 (en) 1988-08-05 1990-02-08 Basf Ag FUELS CONTAINING POLYETHERAMINE OR POLYETHERAMINE DERIVATIVES FOR OTTO ENGINES
DE3838918A1 (en) 1988-11-17 1990-05-23 Basf Ag FUELS FOR COMBUSTION ENGINES
DE4030164A1 (en) 1990-09-24 1992-03-26 Basf Ag FUELS FOR COMBUSTION ENGINES AND LUBRICANTS CONTAINING HIGHLY MOLECULAR AMINO ALCOHOLS
US5254138A (en) * 1991-05-03 1993-10-19 Uop Fuel composition containing a quaternary ammonium salt
DE4142241A1 (en) 1991-12-20 1993-06-24 Basf Ag FUELS FOR OTTO ENGINES
GB9204709D0 (en) 1992-03-03 1992-04-15 Exxon Chemical Patents Inc Additives for oils
DE4309074A1 (en) 1993-03-20 1994-09-22 Basf Ag Mixtures suitable as fuel additives
DE4313088A1 (en) 1993-04-22 1994-10-27 Basf Ag Poly-1-n-alkeneamines and fuel and lubricant compositions containing them
AT400149B (en) 1993-08-17 1995-10-25 Oemv Ag ADDITIVE FOR UNLEADED FUEL AND THIS CONTAINING FUEL
DE4425834A1 (en) 1994-07-21 1996-01-25 Basf Ag Reaction products made of polyisobutenes and nitrogen oxides or mixtures of nitrogen oxides and oxygen and their use as fuel and lubricant additives
DE4425835A1 (en) 1994-07-21 1996-01-25 Basf Ag Use of reaction products made of polyolefins and nitrogen oxides or mixtures of nitrogen oxides and oxygen as additives for fuels
DE4430294A1 (en) * 1994-08-26 1996-02-29 Basf Ag Polymer mixtures and their use as additives for petroleum middle distillates
DE4432038A1 (en) 1994-09-09 1996-03-14 Basf Ag Fuels containing polyetheramines for gasoline engines
DE19525938A1 (en) 1995-07-17 1997-01-23 Basf Ag Process for the production of organic nitrogen compounds, special organic nitrogen compounds and mixtures of such compounds and their use as fuel and lubricant additives
DE19620262A1 (en) 1996-05-20 1997-11-27 Basf Ag Process for the preparation of polyalkenamines
FR2751982B1 (en) 1996-07-31 2000-03-03 Elf Antar France ONCTUOSITY ADDITIVE FOR ENGINE FUEL AND FUEL COMPOSITION
GB9618546D0 (en) 1996-09-05 1996-10-16 Bp Chemicals Additives Dispersants/detergents for hydrocarbons fuels
DE19754039A1 (en) 1997-12-05 1999-06-24 Basf Ag Process for the production of ethylene copolymers in segmented tubular reactors and use of the copolymers as flow improvers
GB9827366D0 (en) 1998-12-11 1999-02-03 Exxon Chemical Patents Inc Macromolecular materials
DE19905211A1 (en) 1999-02-09 2000-08-10 Basf Ag Fuel composition
WO2001072930A2 (en) 2000-03-31 2001-10-04 Texaco Development Corporation Fuel additive composition for improving delivery of friction modifier
DE10102913A1 (en) 2001-01-23 2002-07-25 Basf Ag Alkoxylated alkylphenols used as additives for fuel or lubricant compositions, have a long-chain alkyl group with tertiary or quaternary carbon atoms
DE10123553A1 (en) 2001-05-15 2002-11-21 Basf Ag Production of polyalkenyl succinimides useful as fuel and lubricant additives comprises using an alcohol or phenol to reduce foaming
DE10247795A1 (en) 2002-10-14 2004-04-22 Basf Ag Use of an additive mixture containing homopolymer of a hydrocarbylvinyl ether for improving the action of a cold flow improver for fuel oil compositions and for decreasing the Cold Filter Plugging Point with avoidance of aspiration
DE10356595A1 (en) 2003-12-04 2005-06-30 Basf Ag Fuel oil compositions with improved cold flow properties
EP1705234A1 (en) 2005-03-24 2006-09-27 Basf Aktiengesellschaft Use of detergent additives to inhibit or reduce the formation of injection system deposits in direct injection diesel engines
CA2611306C (en) 2005-06-16 2015-11-24 The Lubrizol Corporation Quaternary ammonium salt detergents for use in fuels
DE102005035277B4 (en) * 2005-07-28 2007-10-11 Clariant Produkte (Deutschland) Gmbh Mineral oils with improved conductivity and cold flowability
EP1887074B1 (en) 2006-08-04 2011-09-14 Infineum International Limited Method and use for the prevention of fuel injector deposits
EP2291494B1 (en) * 2008-05-15 2016-07-06 The Lubrizol Corporation Fuels containing quaternary salts as surfactants in dispersions

Also Published As

Publication number Publication date
CA2803207A1 (en) 2011-12-29
WO2011161149A1 (en) 2011-12-29
KR20130038909A (en) 2013-04-18
CN102958949A (en) 2013-03-06
BR112012032534A2 (en) 2019-09-24
EP2585498A1 (en) 2013-05-01
JP2013531097A (en) 2013-08-01
MX2012014797A (en) 2013-04-03
ES2680571T3 (en) 2018-09-10
EP2585498B1 (en) 2018-05-30
PL2585498T3 (en) 2018-10-31

Similar Documents

Publication Publication Date Title
US8911516B2 (en) Quaternized copolymer
US8790426B2 (en) Quaternized terpolymer
AU2017202811B2 (en) Use of quaternised alkyl amines as additives in fuels and lubricants
US10689326B2 (en) Quaternized ammonium salts of hydrocarbyl epoxides and use thereof as additives in fuels and lubricants
AU2011269024A1 (en) Quaternized copolymer
US10150927B2 (en) Polymers as additives for fuels and lubricants
US10815444B2 (en) Use of specific derivatives of quaternized nitrogen compounds as additives in fuels and lubricants
CA2914279C (en) Use of nitrogen compounds quaternised with alkylene oxide and hydrocarbyl-substituted polycarboxylic acid as additives in fuels and lubricants
CA2840524C (en) Quaternized nitrogen compounds and use thereof as additives in fuels and lubricants
US20160251588A1 (en) Use of quaternized alkyl amines as additive in fuels and lubricants
EP3010998A2 (en) Betaine compounds as additives for fuels
AU2011246506A1 (en) Quaternized terpolymer
AU2012331073A1 (en) Quaternized polyetheramines and use thereof as additives in fuels and lubricants

Legal Events

Date Code Title Description
DA3 Amendments made section 104

Free format text: THE NATURE OF THE AMENDMENT IS: AMEND THE NAME OF THE INVENTOR TO READ GRABARSE, WOLFGANG; KOENIG, HANNAH MARIA; TOCK, CHRISTIAN; ROEGER-GOEPFERT, CORNELIA; VOELKEL, LUDWIG AND BOEHNKE, HARALD

MK4 Application lapsed section 142(2)(d) - no continuation fee paid for the application